1

M EMORANDUM

DATE: October 26 , 2010

SUBJECT: Developments in Practices, Processes, and Control Technologies for Pesticide Active Ingredient Production, Polyether P olyols Production , and Group IV Polymers and Resins

FROM: Alden West, EC/R Inc.

Lesley Stobert, EC/R Inc.

TO: Paula Hirtz, EPA

Nick Parsons, EPA

The purpose of this memorandum is to present the re sults of an investigation to identify any developments in practices, processes, and control technologies for hazardous air pollutant (HAP) emission sources in three source categories that are undergoing a Risk and Technology Review (RTR) of the MACT standa rds for those source categories. This analysis is part of EPA’s review efforts in accordance with section 112(d)(6) of the Clean Air Act. The source categories subject to this review are Pesticide Active Ingredient Production (PAI), Polyether Polyols Pro duction (PEPO) and Group IV Polymers & Resins (P&R IV) at 40 CFR 63 Subparts MMM, PPP, and JJJ respectively. Section 1 provides background information on section 112(d)(6), the three source categories, and the requirements of the national emission standa rds for HAP (NESHAP) that address emi ssion from these categories. Section 2 discusses the exploration of developments in practices, processes, and control technologies that have occurred since the original development of these NESHAP, and section 3 provide s the conclusions of this investigation.

1.0 BACKGROUND

1.1 Section 112(d)(6) Section 112 of the Clean Air Act requires EPA to establish technology

- based standards for listed source categories. These technology

- based standards are often referred to as max imum achievable control technology, or MACT, standards. Section 112 also contains provisions requiring EPA to revisit these standards. Specifically, paragraph 112(d)(6) section states:

(6) REVIEW AND REVISION.

– The Administrator shall review, and revise as necessary (taking into account developments in practices, processes, and control te chnologies), emission standards promulgated under this section no less often than every 8 years.

1.2 Description of Source Categories and MACT Standards

The current regulatory RTR action reviews three source categories . Two of the source categories, PAI and P&R IV , are an aggregate of multiple source categories which have process2

equipment, emission characteristics and control technologies that are sufficiently simil ar to regulate under a single NESHAP. The three source categories subject to this investigation are describe d below.

The PAI NESHAP regulates HAP emissions from major sources in 11 source categories that manufacture organic pesticide active ingredient used in herbicides, insecticides, and fungicides. The 11 source categories regulated by the PAI NESHAP are 4

- Chlror

- 2

- Methyl Acid Production, 2,4 Salts & Esters Production , 4,6

- dinitro

- o

- cresol Production , Butadiene Furfural, Cotrimer , Captafol Production , Captan Production , Chloroneb Production, Chlorothalonil Production , Dacthal (tm) production , Sodiu m Pentachlorophenate Production, and Tordon (tm) Acid Production

. The PEPO NESHAP regulates HAP emissions from polyether polyols manufacturing units (PMPU) at major sources. Polyether polyols fall into two main classes based on the properties of the polymer . T he first class of polyether polyols are high

- molecular

- weight , linear or slightly branched (urethanes) and are used in flexible applications such as re action injection molding, sealants and coatings. The second class of polyether polyols are low

- molecular weight , highly branched (non

- urethanes) and are used in rigid applications such as rigid foams, plastics and solvent resistant coatings. The PEPO NES HAP is divided into two subcategories, polyether polyols made from the polymerization of epoxides (such as ethylene oxide and propylene oxide) and polyether polyols made from the polymerization of tetrahydrofuran (THF). The P&R IV NESHAP regulates HAP emi ssions from major sources in seven source categories that manufacture thermoplastic resins . The seven source categories include Acrylonitrile Butadiene Styrene (ABS), Methyl Methacrylate Acrylonitrile Butadiene Styrene (MABS), Methyl Methacrylate Butadien e Styrene (MBS), Polyethylene Terephthalate (PET), Polystyrene , Styrene Acrylonitrile (SAN), and Nitrile Resin. ABS is used extensively in the automotive industry for components such as mirror housings and grilles, as well as in weatherproofing applicatio ns for swimming pools and recreational vehicles. MBS is used in high strength and transparency applications and as an impact modifier for PVC. PET has good moisture barrier properties and is primarily used to make plastic bottles. Polystyrene has poor b arrier properties

an d is used in the manufacture of furniture and foam for packaging. S AN is primarily used to make ABS and has little use on its own. There are no known facilities that currently produce MABS or nitrile resin. The following list provi des the proposal and promulgation dates for the MACT standards :

 The PAI MACT standard was originally proposed on November 10, 1997 ( 62 FR 60579 ) and promulgated on June 23, 1999 ( 64 FR 33549 );

 The PEPO MACT standard was originally proposed on September 4, 1997 ( 62 FR 46818 ) and promulgated on June 1, 1999 ( 64 FR 29419 );

 The P&R IV MACT standard was originally proposed on March 3, 1995 ( 60 FR 16090 ) and promulgated on September 12, 1996 ( 61 FR 48208 ).

All three MACT standards regulate emissions from storage vessels, equipment leaks, wastewater, process vents and heat exchangers

. The PAI MACT also regulates bag dumps and product dryers. The MACT s include a combination of equipment standards, work practice standards, operational standards and performance sta ndards for each of the emission sources noted above. Various control technologies were considered in the development of the MACT3

standards and are generally included with established operating parameters in the monitoring requirements of each standard

. Ad ditional information on control technologies was found in the Basis and Purpose Documents and Supplementary Information Documents used to support the PAI, PEPO and P&R IV NESHAP rulemaking.

2.0 PRACTICES, PROCESSES, AND CONTROL TECHNOLOGIES For the pu rpose of this exercise, EPA considered a ―development‖ to be:

 Any add

- on control technology or other equipment (e.g., floating roofs for storage tanks) that was not identified and considered during MACT development,

 Any improvements in add

- on control techn ology or other equipment (that was identified and considered during MACT development) that could result in significant additional emission reduction,

 Any work practice or operational procedure that was not identified and considered during MACT development, and

 Any process change or pollution prevention alternative that could be broadly applied that was not identified and considered during MACT development. Table 1 summarizes the practices, processes, and control technologies considered during the developme nt of the MACT standards for these categories. This is followed by descriptions of the searches for developments since that time. The specific information sources that were consulted in this effort included EPA regulatory efforts conducted subsequent to th ese rulemakings (section 2.1), EPA’s RACT/BACT/LAER clearinghouse (section 2.2) , and the California Air Resources Board’s Statewide BACT clearinghouse (section 2.3).4

2.1 Subsequent Regulatory Development Efforts

As noted above, the P&R IV MACT stand ards were promulgated in 1996 . Since that time, EPA has developed air toxics regulations for a number of additional source categories that emit organic HAP from the same type of emission sources that are present at three source categories analyzed in this document . In the subsequent air toxic regulatory actions, EPA consistently evaluated any new practices, processes, and control techniques. Table 2 lists the regulatory actions and which emission sources overlap between each category and these categories. We reviewed the regulatory requirements and/or technical analyses associated with each of these subsequent regulatory actions to identify any practices, processes, and control techniques considered in these efforts that could possibly be applied to the se ven source categories addressed in the current rulemaking action. Table 2 also summarizes the general practices, processes, and control technologies considered and evaluated in the subsequent air toxics rulemakings. Table 3 summarizes the findings of this review.567

As can be seen in Table 3, two practices were identified that were not considered in the development of the PAI, PEPO, and P&R IV MACT standards. The Polymers and Resins III and MON MACT standards contain emission limits to allow the use of pollution prevention measures to achieve compliance, but t hese practices are unique to these industries and would not be applicable to any of the other sour ce categories addressed in the current rulemaking action.

2.2 RACT/BACT/LAER Clearinghouse Under EPA's New Source Review (NSR) program, if a company is planning to build a new plant or modify an existing plant such that air pollution emissions will incr ease by a large amount, then the company must obtain an NSR permit. The NSR permit is a construction permit which requires the company to minimize air pollution emissions by changing the process to prevent air pollution and/or installing air pollution cont rol equipment. T he terms "RACT," "BACT," and "LAER" are acronyms for different program requirements under the NSR program. RACT, or Reasonably Available Control Technology, is required on source s in areas that are not meeting national ambient air quality s tandards (i.e., nonattainment areas). BACT, or Best Available Control Technology, is required on major new or modified sources in clean areas (i.e., attainment areas). LAER, or Lowest Achievable Emission Rate, is re quired on major new or modified sources i n non

- attainment areas.

BACT and LAER (and sometimes RACT) are determined on a case

- by

- case basis, usually by State or local permitting agencies. EPA established the RACT/BACT/LAER Clearinghouse, or RBLC, to provide a central data base of air pollution te chnology information (including past BACT and LAER decisions contained in NSR permits) to promote the sharing of information among permitting agencies and to aid in future case

- by

- case determinations. However, data in the RBLC are not limited to sources su bject to RACT, BACT, and LAER requirements. Noteworthy prevention and control technology decisions and information are included even if they are not related to past RACT, BACT, or LAER decisions. 1 The RBLC contains over 5,000 air pollution control permit d eterminations that can help identify appropriate technologies to mitigate most air pollutant emission streams. It was designed to help permit applicants and reviewers make pollution prevention and control technology decisions for stationary air pollution

s ources, and includes data submitted by several U.S. territorie s and all 50 States on over 200 different air pollutants and 1,000 industrial processes. The RB LC provides several options for searching the permit database on

- line to locate applicable control technologies. We conducted a n advanced search of the RBLC, which allows the user t o spe cify a large number of relevant categories . Our search specified processes in Agricultural Chemical Manufacturing (for PAI

1 Technology Transfer Network: Clean Air Technology Center. RACT/BACT/LAER Clearinghouse Basic Information. Available: http://www.epa.gov/ttn/catc/rblc/htm/welcome_eg.html . Accessed 10/5/11.8

controls) , Pol ymer and Resin Production (for P &R IV controls) , and the Synthetic Organic Chemical Manufacturing Industry (SOCMI) (for PAI, PEPO, and P&R IV controls) with permits dating back to the pro mulgation dates of each MACT regulation

. S earch results included the following data fields:

 Facility Name, County, and State

 Pollutant Name and Group

 Process Description

 Control Technology and Percent Efficiency The following processes, practices, and control technologies were found in the RBLC for the Agricultural Chemicals, Polymers and Resins and SOCM I categories. More detailed example results of the search are presented in the RBLC search documents in A ttach ment 1

.  Regenerative Thermal Oxidation

— VOC emissions are captured within the building by two concentrators by adsorption, and then desorbed by hea t and incinerated by the thermal oxidizer.

 Thermal oxidizer

 Oxidizer

 Oxidation catalyst

 Steam stripping of solvent

— Emissions stream from stripping operation is collected and routed to flare.

 Leak Detection and Repair

 Plant process flare (high pressure, low pressure and smokeless)

 Scrubber offgas incinerator

 Fixed roof tanks

 Internal floating roof tanks with use of submerged fill

 Concentrator

 Chilled water

- cooled condenser and liquid nitrogen cooled condenser

 P acked tower scrubber

 Vapor recovery system

 LDAR program

 Process heater/burner These practices, processes, and control technologies are all examples of the types of emission reduction techniques that were considered in the development of the PAI, PEPO, and P&R IV MACT standards. Therefore, this exercis e did not reveal any developments in practices, processes, or control technologies. 2.3 California Air Resources Board BACT Clearinghouse The California Air Resources Board provides a database of control technologies determined to be BACT. The database contains information on emission sources and facilities within the State of California, and does not duplicate any information in the RACT/BACT/LAER Clearinghouse. Information can be obtained from the database by searching the pollutant, source category, district, SIC code, or NAICS code. For the purposes of this investigation, all relevant source categories were searched for emissions of VOC in all districts. Table 4 presents the emission source types and VOC control technologies that were discovered i n the search.9

These control technologies are all examples of the types of emission reduction techniques that were considered in the development of the PAI, PEPO, and P&R IV MACT standards. Therefore, this exercise did not reveal any developments in p ractices, processes, or control technologies.

3.0 CONCLUSIONS In order to identify developments in practices, processes, or control technologies tha t could be used to further reduce emissions from PAI, PEPO and P&R IV sources, the following sources of in formation were searched: control evaluations conducted during regulatory efforts conducted subsequent to the PAI, PEPO and P&R IV rulemaking , EPA’s RACT/BACT/LAER clearinghouse , and California Air Resources Board’s BACT clearinghouse

. Through these efforts , we did not identify any practices, processes, and control technologies applicable to the emission sources in these categories that were not identified and evaluated during the original MACT development.Attachment 1Previous Page

NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: PRYOR PLANT CHEMICAL

RBLC ID: OK-0134 + Corporate/Company Name: PRYOR PLANT CHEMICAL COMPANY + Facility Name: PRYOR PLANT CHEMICAL Facility County: MAYES Facility State: OK Facility ZIP Code: 73107 + SIC Code: 2873 NAICS Code: 325311 Permit Issuance Date: 02/23/2009 ACT

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: Primary Reformer (EUID #101, EUG#1-NH3 Plant #4) + Process Type: 61.012

Pollutant Information: PRYOR PLANT CHEMICAL - Primary Reformer (EUID #101, EUG#1-NH3 Plant #4)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: Good Combustion + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: Low NOx Burners/Good Combustion + Percent Efficiency:

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method+ Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: Natural Gas + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: Condensate Steam Flash Drum (EUID 102, EUG 1, Ammonia Plant 4) + Process Type: 61.999

Pollutant Information: PRYOR PLANT CHEMICAL - Condensate Steam Flash Drum (EUID 102, EUG 1, Ammonia Plant 4)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: Good operation practices + Percent Efficiency:

+ Pollutant Name Methanol Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: Good operation practices + Percent Efficiency:+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: Nitric Acid Plant No. 1 (EU 301, EUG No. 3) + Process Type: 62.014

Pollutant Information: PRYOR PLANT CHEMICAL - Nitric Acid Plant No. 1 (EU 301, EUG No. 3)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: Existing Control, extended absorption with NSCR and good operating pracitices + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: Nitric Acid Plant No.3 (EU 302, EUG No. 3) + Process Type: 62.014

Pollutant Information: PRYOR PLANT CHEMICAL - Nitric Acid Plant No.3 (EU 302, EUG No. 3)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: Extended Absorption with NSCR (existing) and good operation practices + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: Nitric Acid Plant No. 4, (EU 303, EUG 3) + Process Type: 62.014Pollutant Information: PRYOR PLANT CHEMICAL - Nitric Acid Plant No. 4, (EU 303, EUG 3)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: SCR /good operation practices + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: Nitric Acid Preheaters No. 1 (EU 401, EUG 4) + Process Type: 13.310

Pollutant Information: PRYOR PLANT CHEMICAL - Nitric Acid Preheaters No. 1 (EU 401, EUG 4)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: good combustion practices + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: Low NOx burners/good combustion practices + Percent Efficiency:

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Natural gas combustion + Percent Efficiency:

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Natural gas combustion + Percent Efficiency:+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: good combustion + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: natural gas combustion + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: Nitric Acid Preheater No3 (EU 402, EUG 4) + Process Type: 13.310

Pollutant Information: PRYOR PLANT CHEMICAL - Nitric Acid Preheater No3 (EU 402, EUG 4)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: good combustion + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: PRYOR PLANT CHEMICAL

RBLC ID: OK-0135 + Corporate/Company Name: PRYOR PLANT CHEMICAL COMPANY + Facility Name: PRYOR PLANT CHEMICAL Facility County: MAYES Facility State: OK Facility ZIP Code: 73107 + SIC Code: 2873 NAICS Code: 325311 Permit Issuance Date: 02/23/2009 ACTProcess Information: PRYOR PLANT CHEMICAL

+ Process Name: PRIMARY REFORMER + Process Type: 61.012

Pollutant Information: PRYOR PLANT CHEMICAL - PRIMARY REFORMER

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NO CONTROLS;GOOD COMBUSTION PRACTICES. + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS/GOOD COMBUSTION PRACTICE. + Percent Efficiency:

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N+ Control Method Description: + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: CONDENSATE STEAM FLASH DRUM-AMMONIA PLT 4 + Process Type: 61.999

Pollutant Information: PRYOR PLANT CHEMICAL - CONDENSATE STEAM FLASH DRUM-AMMONIA PLT 4

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: GOOD OPERATION PRACTICES + Percent Efficiency:

+ Pollutant Name Methanol Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: GOOD OPERATION PRACTICES + Percent Efficiency:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: NITRIC ACID PLANT #1 + Process Type: 62.014

Pollutant Information: PRYOR PLANT CHEMICAL - NITRIC ACID PLANT #1

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method+ Control Method Description: EXTENDED ABSORPTION WITH NSCR. + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: NITRIC ACID PLANT #3 + Process Type: 62.014

Pollutant Information: PRYOR PLANT CHEMICAL - NITRIC ACID PLANT #3

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: EXTENDED ABSORPTION WITH NSCR AND GOOD OPERATION PRACTICES. + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: NITRIC ACID PLANT #4 + Process Type: 62.014

Pollutant Information: PRYOR PLANT CHEMICAL - NITRIC ACID PLANT #4

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: SCR AND GOOD OPERATION PRACTICES. + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: NITRIC ACID PREHEATERS #1, #3, AND #4 + Process Type: 13.310

Pollutant Information: PRYOR PLANT CHEMICAL - NITRIC ACID PREHEATERS #1, #3, AND #4

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) )+ Control Method Code: P + Control Method Description: LOW-NOX BURNERS AND GOOD COMBUSTION PRACTICES. + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. + Percent Efficiency:

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: CARBON DIOXIDE VENT + Process Type: 61.999

Pollutant Information: PRYOR PLANT CHEMICAL - CARBON DIOXIDE VENT+ Pollutant Name Carbon Dioxide Pollutant Group(s): ( Acid Gasses/Mist , Greenhouse Gasses (GHG) , InOrganic Compounds ) + Control Method Code: N + Control Method Description: GOOD OPERATION PRACTICES. + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: AMMONIUM NITRATE PLANTS #1 AND #2 + Process Type: 61.012

Pollutant Information: PRYOR PLANT CHEMICAL - AMMONIUM NITRATE PLANTS #1 AND #2

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: IN-STACK CONDENSERS AND GOOD OPERATION PRACTICES + Percent Efficiency: 80.000

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: IN-STACK CONDENSERS AND GOOD OPERATION PRACTICES + Percent Efficiency: 80.000

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: GRANULATOR SCRUBBERS #1, #2, AND #3 + Process Type: 61.999

Pollutant Information: PRYOR PLANT CHEMICAL - GRANULATOR SCRUBBERS #1, #2, AND #3

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: GOOD OPERATION PRACTICES + Percent Efficiency: 80.000

+ Pollutant Name Particulate matter, total < 10 μ (TPM10)Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: GOOD OPERATION PRACTICES + Percent Efficiency: 80.000

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: BOILERS #1 AND #2 + Process Type: 13.310

Pollutant Information: PRYOR PLANT CHEMICAL - BOILERS #1 AND #2

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Formaldehyde Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description:+ Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW-NOX BURNERS AND GOOD COMBUSTION PRACTICES + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: COOLING TOWER #1 + Process Type: 61.999

Pollutant Information: PRYOR PLANT CHEMICAL - COOLING TOWER #1

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: MIST ELIMINATORS + Percent Efficiency:

Process Information: PRYOR PLANT CHEMICAL

+ Process Name: COOLING TOWER #2 + Process Type: 61.999

Pollutant Information: PRYOR PLANT CHEMICAL - COOLING TOWER #2

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: MIST ELIMINATORS + Percent Efficiency:

Previous PagePrevious PagePrevious Page

NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: ADM POLYMERS

RBLC ID: IA-0084 + Corporate/Company Name: ADM CORN PROCESSING - CLINTON + Facility Name: ADM POLYMERS Facility County: CLINTON Facility State: IA Facility ZIP Code: 52732 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 11/30/2006 ACT

Process Information: ADM POLYMERS

+ Process Name: ANTIFOAM STORAGE TANK + Process Type: 42.009

Pollutant Information: ADM POLYMERS - ANTIFOAM STORAGE TANK

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: BDO STORAGE TANK + Process Type: 42.009

Pollutant Information: ADM POLYMERS - BDO STORAGE TANK

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:Process Information: ADM POLYMERS

+ Process Name: FIRE PUMP ENGINE + Process Type: 17.210

Pollutant Information: ADM POLYMERS - FIRE PUMP ENGINE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: EMERGENCY GENERATOR + Process Type: 17.110

Pollutant Information: ADM POLYMERS - EMERGENCY GENERATOR

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: SEED FERMENTERS + Process Type: 64.003

Pollutant Information: ADM POLYMERS - SEED FERMENTERS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) )+ Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: MAIN FERMENTERS + Process Type: 64.003

Pollutant Information: ADM POLYMERS - MAIN FERMENTERS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: BROTH HOLDING TANKS + Process Type: 64.003

Pollutant Information: ADM POLYMERS - BROTH HOLDING TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: LEAKS FROM EQUIPMENT IN VOC SERVICE + Process Type: 64.002

Pollutant Information: ADM POLYMERS - LEAKS FROM EQUIPMENT IN VOC SERVICE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LDAR (LEAK DETECTION AND REPAIR)+ Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: POLYMER POWDER CONVEYING + Process Type: 64.005

Pollutant Information: ADM POLYMERS - POLYMER POWDER CONVEYING

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: EXTRUDER VACUUM PUMP + Process Type: 64.005

Pollutant Information: ADM POLYMERS - EXTRUDER VACUUM PUMP

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: PELLETIZER & DRYER + Process Type: 64.005

Pollutant Information: ADM POLYMERS - PELLETIZER & DRYER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:Process Information: ADM POLYMERS

+ Process Name: PELLET BLENDING SILOS + Process Type: 64.005

Pollutant Information: ADM POLYMERS - PELLET BLENDING SILOS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: PELLET STORAGE BIN + Process Type: 64.005

Pollutant Information: ADM POLYMERS - PELLET STORAGE BIN

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: LOADOUT SILOS + Process Type: 64.005

Pollutant Information: ADM POLYMERS - LOADOUT SILOS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: ADM POLYMERS+ Process Name: SOLVENT RECOVERY SYSTEM + Process Type: 64.003

Pollutant Information: ADM POLYMERS - SOLVENT RECOVERY SYSTEM

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: SCRUBBER + Percent Efficiency:

Process Information: ADM POLYMERS

+ Process Name: BIOMASS & POLYMER DRYERS + Process Type: 63.999

Pollutant Information: ADM POLYMERS - BIOMASS & POLYMER DRYERS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THERMAL OXIDIZER + Percent Efficiency: 98.000

Process Information: ADM POLYMERS

+ Process Name: LAIDIG TANKS + Process Type: 42.009

Pollutant Information: ADM POLYMERS - LAIDIG TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform)Facility Information: ANDREA ZEE CORP. DBA MARBLE PALACE

RBLC ID: CA-0782 + Corporate/Company Name: ANDREA ZEE CORP. DBA MARBLE PALACE + Facility Name: ANDREA ZEE CORP. DBA MARBLE PALACE Facility County: SAN JOAQUIN Facility State: CA Facility ZIP Code: + SIC Code: 3281 NAICS Code: Permit Issuance Date: 05/21/1997 ACT

Process Information: ANDREA ZEE CORP. DBA MARBLE PALACE

+ Process Name: POLYESTER RESIN OPERATION + Process Type: 63.026

Pollutant Information: ANDREA ZEE CORP. DBA MARBLE PALACE - POLYESTER RESIN OPERATION

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: SPRAY BOOTH WITH EXHAUST FILTERS AND AIR ASSISTED AIRLESS SPRAY EQUIPMENT + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: BASF CORPORATION

RBLC ID: MI-0304 + Corporate/Company Name: BASF CORPORATION + Facility Name: BASF CORPORATION Facility County: WAYNE Facility State: MI Facility ZIP Code: 48150 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 10/23/2001 ACTProcess Information: BASF CORPORATION

+ Process Name: REACTORS, ISOCYANATES + Process Type: 64.001

Pollutant Information: BASF CORPORATION - REACTORS, ISOCYANATES

+ Pollutant Name Methylene diphenyl diisocyanate Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CONTROL BY COMMON CARBON CANISTER. SEE POLLUTANT NOTES. + Percent Efficiency: 97.000

Process Information: BASF CORPORATION

+ Process Name: BULK LOADING, TDI & MDI + Process Type: 63.999

Pollutant Information: BASF CORPORATION - BULK LOADING, TDI & MDI

+ Pollutant Name Methylene diphenyl diisocyanate Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CARBON CANISTER, WITH MONITORING + Percent Efficiency: 97.000

Process Information: BASF CORPORATION

+ Process Name: DRUMMING + Process Type: 63.999

Pollutant Information: BASF CORPORATION - DRUMMING

+ Pollutant Name Methylene diphenyl diisocyanate Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: THROUGHPUT LIMIT 50000 T/YR, MDI. + Percent Efficiency:Process Information: BASF CORPORATION

+ Process Name: TANKS + Process Type: 64.004

Pollutant Information: BASF CORPORATION - TANKS

+ Pollutant Name Methylene diphenyl diisocyanate Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CARBON CANISTER WITH MONITORING + Percent Efficiency: 97.000

Process Information: BASF CORPORATION

+ Process Name: BLENDING TANKS, RESIN + Process Type: 64.005

Pollutant Information: BASF CORPORATION - BLENDING TANKS, RESIN

+ Pollutant Name Hydrochlorofluorocarbons (HCFC) Pollutant Group(s): ( Greenhouse Gasses (GHG) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: P + Control Method Description: 4000 T/YR THROUGHPUT LIMIT. ALSO 1000 T/YR LIMIT ON HCFC-22. + Percent Efficiency:

+ Pollutant Name Triethylamine Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 3179 LB/MONTH THROUGHPUT LIMIT + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform)Facility Information: BASF FREEPORT SITE

RBLC ID: TX-0578 + Corporate/Company Name: BASF CORPORATION + Facility Name: BASF FREEPORT SITE Facility County: BRAZORIA Facility State: TX Facility ZIP Code: 77541 + SIC Code: 2869 NAICS Code: 325199 Permit Issuance Date: 01/07/2011 ACT

Process Information: BASF FREEPORT SITE

+ Process Name: Sodium Acrylate polymer Production + Process Type: 63.999

Pollutant Information: BASF FREEPORT SITE - Sodium Acrylate polymer Production

+ Pollutant Name Acrylic Acid Pollutant Group(s): ( Acid Gasses/Mist , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: Scrubber + Percent Efficiency: 95.000

+ Pollutant Name Isopropyl Alcohol Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: A + Control Method Description: Scrubber System + Percent Efficiency: 95.000

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: CARPENTER CO.

RBLC ID: CA-0785 + Corporate/Company Name: CARPENTER CO. + Facility Name: CARPENTER CO.Facility County: SAN JOAQUIN Facility State: CA Facility ZIP Code: + SIC Code: 3086 NAICS Code: Permit Issuance Date: 12/06/1996 ACT

Process Information: CARPENTER CO.

+ Process Name: ADHESIVE APPLICATION PROCESS + Process Type: 41.016

Pollutant Information: CARPENTER CO. - ADHESIVE APPLICATION PROCESS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LOW-VOC ADHESIVES + Percent Efficiency:

Process Information: CARPENTER CO.

+ Process Name: NON-WOVEN POLYESTER FOAM LINE + Process Type: 63.999

Pollutant Information: CARPENTER CO. - NON-WOVEN POLYESTER FOAM LINE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NO CONTROL + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: CHEVRON PHILLIPS HOUSTON CHEMICAL COMPANY

RBLC ID: TX-0329 + Corporate/Company Name: PHILLIPS CHEMICAL COMPANY+ Facility Name: CHEVRON PHILLIPS HOUSTON CHEMICAL COMPANY Facility County: HARRIS Facility State: TX Facility ZIP Code: 77501 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 02/23/2000 ACT

Process Information: CHEVRON PHILLIPS HOUSTON CHEMICAL COMPANY

+ Process Name: (3) FLARE SYSTEM & (7) PE CATALYST ACTIVATION FAC + Process Type: 19.310

Pollutant Information: CHEVRON PHILLIPS HOUSTON CHEMICAL COMPANY - (3) FLARE SYSTEM & (7) PE CATALYST ACTIVATION FAC

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: CHEVRON PHILLIPS HOUSTON CHEMICAL COMPANY

+ Process Name: (12) PE CAT ACTIV FAC, (34) PE PLANTS, (17) HAC PP + Process Type: 63.999

Pollutant Information: CHEVRON PHILLIPS HOUSTON CHEMICAL COMPANY - (12) PE CAT ACTIV FAC, (34) PE PLANTS, (17) HAC PP

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:Process Information: CHEVRON PHILLIPS HOUSTON CHEMICAL COMPANY

+ Process Name: (3) FLARES, (5) PE CAT ACT FAC, (40) PE PLANTS + Process Type: 19.310

Pollutant Information: CHEVRON PHILLIPS HOUSTON CHEMICAL COMPANY - (3) FLARES, (5) PE CAT ACT FAC, (40) PE PLANTS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency: 98.000

Process Information: CHEVRON PHILLIPS HOUSTON CHEMICAL COMPANY

+ Process Name: (3) FLARES, (15) PE PLANTS, HYDROCARBON LOAD/UNL + Process Type: 19.310

Pollutant Information: CHEVRON PHILLIPS HOUSTON CHEMICAL COMPANY - (3) FLARES, (15) PE PLANTS, HYDROCARBON LOAD/UNL

+ Pollutant Name Hexene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: CUSTOM MARBLE & ONYX

RBLC ID: CA-0781 + Corporate/Company Name: CUSTOM MARBLE & ONYX + Facility Name: CUSTOM MARBLE & ONYX Facility County: STANISLAUS Facility State: CA Facility ZIP Code:+ SIC Code: 3281 NAICS Code: Permit Issuance Date: 04/04/1997 ACT

Process Information: CUSTOM MARBLE & ONYX

+ Process Name: POLYESTER RESIN OPERATION + Process Type: 63.026

Pollutant Information: CUSTOM MARBLE & ONYX - POLYESTER RESIN OPERATION

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LOW-VOC RESINS WITH A MONOMER WT. CONTENT + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LOW-VOC RESINS WITH A MONOMER WT. CONTENT + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: DA/PRO RUBBER INC.

RBLC ID: CA-0898 + Corporate/Company Name: DA/PRO RUBBER INC. + Facility Name: DA/PRO RUBBER INC. Facility County: LOS ANGELES Facility State: CA Facility ZIP Code: 91355 + SIC Code: 3069 NAICS Code: Permit Issuance Date: 07/30/1999 ACT

Process Information: DA/PRO RUBBER INC.

+ Process Name: RUBBER ROLL MILL, LUFKIN+ Process Type: 63.999

Pollutant Information: DA/PRO RUBBER INC. - RUBBER ROLL MILL, LUFKIN

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PERMIT REQUIRMENT IS TORIT MODEL DFT3-6 PULSE JET CLEANING BAGHOUSE WITH A FILTER AREA OF 1524 SQ. FT. + Percent Efficiency:

Process Information: DA/PRO RUBBER INC.

+ Process Name: SPRAY BOOTH, BINKS BENCH TYPE + Process Type: 41.016

Pollutant Information: DA/PRO RUBBER INC. - SPRAY BOOTH, BINKS BENCH TYPE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NO CONTROL. PERMIT LIMIT IS A RESTRICTION OF COATINGS TO < 200 GALLONS OF COATINGS PER YEAR. + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: DAK AMERICAS LLC-COOPER RIVER PLANT

RBLC ID: SC-0080 + Corporate/Company Name: DAK AMERICAS LLC + Facility Name: DAK AMERICAS LLC-COOPER RIVER PLANT Facility County: BERKELEY Facility State: SC Facility ZIP Code: 29461 + SIC Code: 2824 NAICS Code: 325222 Permit Issuance Date: 08/08/2002 ACT

Process Information: DAK AMERICAS LLC-COOPER RIVER PLANT+ Process Name: IPA MIX TANK, 440 CUBIC FOOT + Process Type: 63.999

Pollutant Information: DAK AMERICAS LLC-COOPER RIVER PLANT - IPA MIX TANK, 440 CUBIC FOOT

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FABRIC FILTER BAGHOUSE + Percent Efficiency:

Process Information: DAK AMERICAS LLC-COOPER RIVER PLANT

+ Process Name: SSP AMORPHOUS CHIP SILOS, TWO (2) + Process Type: 63.999

Pollutant Information: DAK AMERICAS LLC-COOPER RIVER PLANT - SSP AMORPHOUS CHIP SILOS, TWO (2)

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FABRIC FILTER BAG HOUSE + Percent Efficiency:

Process Information: DAK AMERICAS LLC-COOPER RIVER PLANT

+ Process Name: SSP AMORPHOUS CHIP SILO + Process Type: 63.999

Pollutant Information: DAK AMERICAS LLC-COOPER RIVER PLANT - SSP AMORPHOUS CHIP SILO

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FABRIC FILTER BAG HOUSE + Percent Efficiency:

Process Information: DAK AMERICAS LLC-COOPER RIVER PLANT+ Process Name: SSP FEED BIN

+ Process Type: 63.999

Pollutant Information: DAK AMERICAS LLC-COOPER RIVER PLANT - SSP FEED BIN

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FABRIC FILTER BAG HOUSE + Percent Efficiency:

Process Information: DAK AMERICAS LLC-COOPER RIVER PLANT

+ Process Name: AMORPHOUS CHIP DRYERS, THREE (3) + Process Type: 63.999

Pollutant Information: DAK AMERICAS LLC-COOPER RIVER PLANT - AMORPHOUS CHIP DRYERS, THREE (3)

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: DAK AMERICAS LLC-COOPER RIVER PLANT

+ Process Name: SSP PRECRYSTALLIZER + Process Type: 63.999

Pollutant Information: DAK AMERICAS LLC-COOPER RIVER PLANT - SSP PRECRYSTALLIZER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FABRIC FILTER BAG HOUSE + Percent Efficiency:

Process Information: DAK AMERICAS LLC-COOPER RIVER PLANT

+ Process Name: DRYER+ Process Type: 63.999

Pollutant Information: DAK AMERICAS LLC-COOPER RIVER PLANT - DRYER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: DAK AMERICAS LLC-COOPER RIVER PLANT

+ Process Name: SSP CHIP SILO + Process Type: 63.999

Pollutant Information: DAK AMERICAS LLC-COOPER RIVER PLANT - SSP CHIP SILO

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FABRIC FILTER BAG HOUSE + Percent Efficiency:

Process Information: DAK AMERICAS LLC-COOPER RIVER PLANT

+ Process Name: TWO (2) CHIP SILOS + Process Type: 63.999

Pollutant Information: DAK AMERICAS LLC-COOPER RIVER PLANT - TWO (2) CHIP SILOS

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FILTER FABRIC BAG HOUSE + Percent Efficiency:

Process Information: DAK AMERICAS LLC-COOPER RIVER PLANT

+ Process Name: RAILCAR LOADING,TWO (2) AMORPHOUS CHIP + Process Type: 63.999Pollutant Information: DAK AMERICAS LLC-COOPER RIVER PLANT - RAILCAR LOADING,TWO (2) AMORPHOUS CHIP

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FABRIC FILTER BAG HOUSE + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: DART CONTAINER CORPORATION LLC

RBLC ID: MS-0085 + Corporate/Company Name: DART CONTAINER CORPORATION LLC + Facility Name: DART CONTAINER CORPORATION LLC Facility County: CLARKE Facility State: MS Facility ZIP Code: 39355 + SIC Code: 3086 NAICS Code: 326140 Permit Issuance Date: 01/31/2007 ACT

Process Information: DART CONTAINER CORPORATION LLC

+ Process Name: NATURAL GAS FIRED BOILER + Process Type: 13.310

Pollutant Information: DART CONTAINER CORPORATION LLC - NATURAL GAS FIRED BOILER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: DART CONTAINER CORPORATION LLC+ Process Name: CUP MANUFACTURING PROCESS + Process Type: 63.031

Pollutant Information: DART CONTAINER CORPORATION LLC - CUP MANUFACTURING PROCESS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: PENTANE EMISSIONS ARE GATHERED AND ROUTED TO BOILERS FOR DESTRUCTION. + Percent Efficiency: 95.000

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: DEVRO-TEEPAK

RBLC ID: IL-0066 + Corporate/Company Name: DEVRO-TEEPAK + Facility Name: DEVRO-TEEPAK Facility County: VERMILION Facility State: IL Facility ZIP Code: 61832- + SIC Code: 3089 NAICS Code: 326199 Permit Issuance Date: 08/18/1998 ACT

Process Information: DEVRO-TEEPAK

+ Process Name: MACHINES, THREE PROCESS, #8-#10 + Process Type: 63.999

Pollutant Information: DEVRO-TEEPAK - MACHINES, THREE PROCESS, #8-#10

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: USE OF CONVENTIONAL VISCOSE PROCESS, OR AN ENHANCED PROCESS, REQUIRED. + Percent Efficiency:

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NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: FAGERDALA PAC-LITE INCORPORATED

RBLC ID: MI-0322 + Corporate/Company Name: FAGERDALA PAC-LITE INCORPORATED + Facility Name: FAGERDALA PAC-LITE INCORPORATED Facility County: ST. CLAIR Facility State: MI Facility ZIP Code: 48040 + SIC Code: 3086 NAICS Code: 326160 Permit Issuance Date: 02/01/2001 ACT

Process Information: FAGERDALA PAC-LITE INCORPORATED

+ Process Name: EXPANDABLE POLYPROPYLENE BEAD PRODUCTION + Process Type: 63.999

Pollutant Information: FAGERDALA PAC-LITE INCORPORATED - EXPANDABLE POLYPROPYLENE BEAD PRODUCTION

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THERMAL OXIDIZER. + Percent Efficiency: 85.000

Process Information: FAGERDALA PAC-LITE INCORPORATED

+ Process Name: EXTRUSION, POLYPROPYLENE + Process Type: 63.999

Pollutant Information: FAGERDALA PAC-LITE INCORPORATED - EXTRUSION, POLYPROPYLENE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method+ Control Method Description: HOODED DIE AREAS CONTROLLED BY THERMAL OXIDIZER. + Percent Efficiency: 37.000

Process Information: FAGERDALA PAC-LITE INCORPORATED

+ Process Name: EXTRUSION, POLYETHYLENE + Process Type: 63.999

Pollutant Information: FAGERDALA PAC-LITE INCORPORATED - EXTRUSION, POLYETHYLENE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: HOODED DIE AREAS CONTROLLED BY THERMAL OXIDIZER 12-20% CAPTURE TEST REQUIRED WITHIN 180 DAYS. + Percent Efficiency: 12.000

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: FORMOSA PLASTICS CORPORATION

RBLC ID: TX-0278 + Corporate/Company Name: FORMOSA PLASTICS CORPORATION + Facility Name: FORMOSA PLASTICS CORPORATION Facility County: CALHOUN Facility State: TX Facility ZIP Code: 77978 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 01/01/2000 EST

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: FINAL DEGASSER NO. 1 + Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - FINAL DEGASSER NO. 1

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: PELLETIZERS NO. 1 & 2 + Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - PELLETIZERS NO. 1 & 2

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: CATALYST FILLING VENT NO. 1 + Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - CATALYST FILLING VENT NO. 1

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: CATALYST FILLING VENT NO. 2+ Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - CATALYST FILLING VENT NO. 2

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: BUFFER SILO NO. 1 + Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - BUFFER SILO NO. 1

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: POWDER BIN NO. 1 + Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - POWDER BIN NO. 1

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: BLENDING SILOS NO. 1 & 2 + Process Type: 63.999Pollutant Information: FORMOSA PLASTICS CORPORATION - BLENDING SILOS NO. 1 & 2

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: PRODUCT SILOS NOS. 1 & 2 + Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - PRODUCT SILOS NOS. 1 & 2

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: HOPPER CAR SILOS AND LOADINGS NOS. 1 & 2 + Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - HOPPER CAR SILOS AND LOADINGS NOS. 1 & 2

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: TRUCK SILO NO. 1 + Process Type: 63.999Pollutant Information: FORMOSA PLASTICS CORPORATION - TRUCK SILO NO. 1

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: AUTO-PACKER SILO NO. 1 + Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - AUTO-PACKER SILO NO. 1

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: ADDITIVE FUGITIVES NOS. 1 & 2 + Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - ADDITIVE FUGITIVES NOS. 1 & 2

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: MASTER BATCHES NOS. 1 & 2 + Process Type: 63.999Pollutant Information: FORMOSA PLASTICS CORPORATION - MASTER BATCHES NOS. 1 & 2

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA PLASTICS CORPORATION

+ Process Name: PROCESS FUGITIVES + Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS CORPORATION - PROCESS FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: FORMOSA PLASTICS TEXAS

RBLC ID: TX-0438 + Corporate/Company Name: FORMOSA PLASTICS CORP. + Facility Name: FORMOSA PLASTICS TEXAS Facility County: CALHOUN Facility State: TX Facility ZIP Code: 77978 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 03/09/1999 ACT

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: POLYPROPYLENE RESIN REACTOR+ Process Type: 63.999

Pollutant Information: FORMOSA PLASTICS TEXAS - POLYPROPYLENE RESIN REACTOR

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: HDPE INCINERATOR + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONES OR BAG FILTERS + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: FORMOSA SPECIALTY PVC PLANT

RBLC ID: TX-0508 + Corporate/Company Name: FORMOSA PLASTICS CORPORATION TEXAS + Facility Name: FORMOSA SPECIALTY PVC PLANT Facility County: CALHOUN Facility State: TX Facility ZIP Code: 77978 + SIC Code: 308 NAICS Code: 221119 Permit Issuance Date: 04/04/2006 ACT

Process Information: FORMOSA SPECIALTY PVC PLANT

+ Process Name: INCINERATOR/SCRUBBERS + Process Type: 63.036

Pollutant Information: FORMOSA SPECIALTY PVC PLANT - INCINERATOR/SCRUBBERS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N+ Control Method Description: + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Hydrochloric Acid Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) , InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Chlorine / Chlorine Compounds Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:+ Pollutant Name Vinyl Chloride Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: FORMOSA SPECIALTY PVC PLANT

+ Process Name: TRAIN 1A/B DRYER EMISSIONS + Process Type: 63.036

Pollutant Information: FORMOSA SPECIALTY PVC PLANT - TRAIN 1A/B DRYER EMISSIONS

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: FORMOSA SPECIALTY PVC PLANT

+ Process Name: DRYER 1A/B + Process Type: 63.036

Pollutant Information: FORMOSA SPECIALTY PVC PLANT - DRYER 1A/B

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Vinyl Chloride Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Ethyl Alcohol Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:Process Information: FORMOSA SPECIALTY PVC PLANT

+ Process Name: TRAIN 2 DRYER EMISSIONS + Process Type: 63.036

Pollutant Information: FORMOSA SPECIALTY PVC PLANT - TRAIN 2 DRYER EMISSIONS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N+ Control Method Description: + Percent Efficiency:

Process Information: FORMOSA SPECIALTY PVC PLANT

+ Process Name: TRAIN 2 DRYER + Process Type: 63.036

Pollutant Information: FORMOSA SPECIALTY PVC PLANT - TRAIN 2 DRYER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Vinyl Chloride Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: FORMOSA SPECIALTY PVC PLANT

+ Process Name: TRAIN 3 DRYER EMISSIONS + Process Type: 63.036

Pollutant Information: FORMOSA SPECIALTY PVC PLANT - TRAIN 3 DRYER EMISSIONS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description:+ Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: FORMOSA SPECIALTY PVC PLANT

+ Process Name: TRAIN 3 DRYER + Process Type: 63.036

Pollutant Information: FORMOSA SPECIALTY PVC PLANT - TRAIN 3 DRYER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Vinyl Chloride Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) )+ Control Method Code: N + Control Method Description: + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

RBLC ID: TX-0272 + Corporate/Company Name: FORMOSA PLASTICS CORP + Facility Name: FORMOSA- HIGH DENSITY POLYETHYLENE II Facility County: CALHOUN Facility State: TX Facility ZIP Code: + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 09/08/1999 ACT

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: FLASH TANK CLEANOUT SCREEN + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - FLASH TANK CLEANOUT SCREEN

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: POWDER STORAGE TANK + Process Type: 63.999Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - POWDER STORAGE TANK

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: PELLET DRYER + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - PELLET DRYER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED. VOC CONCENTRATION IS ESTIMATED FROM A SIMILAR PHILLIPS PLANT AT 15 PPMV. A POST-EXTRUDER EMISSION. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: PELLET BLENDING AND STORAGE + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - PELLET BLENDING AND STORAGE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED. THE TOTAL PELLET EMISSIONS ARE LESS THAN 50 PPMW. + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED.+ Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: PELLET LOADOUT FILTER + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - PELLET LOADOUT FILTER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED. THE TOTAL PELLET EMISSIONS ARE LESS THAN 50 PPMW. + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: PROCESS FUGITIVES + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - PROCESS FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: A 28MID PROGRAM WILL BE USED. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: FLUFF HOPPER CAR LOADING FILTER + Process Type: 63.999Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - FLUFF HOPPER CAR LOADING FILTER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: PELLET HOPPER CAR LOADING FILTER + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - PELLET HOPPER CAR LOADING FILTER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: EXTRUDER FEED TANK VENT + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - EXTRUDER FEED TANK VENT

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method THE VOC EMISSIONS ARE UNCONTROLLED AND ARE+ Control Method Description: THE VOC EMISSIONS ARE UNCONTROLLED AND ARE ESTIMATED TO BE UP TO 200 PPMV IN THE EXHAUST. THE TOTAL UNCONTROLLED EMISSIONS FOR ALL VENTS ARE 54 LB VOC/MMLB PRODUCT. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: EXTRUDER BUILDING VACUUM FILTER + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - EXTRUDER BUILDING VACUUM FILTER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: HEPA FILTER VENT ACTIVATOR + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - HEPA FILTER VENT ACTIVATOR

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: HEPA FILTER IS CONTROL. + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II+ Process Name: QUENCH STATION VENT + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - QUENCH STATION VENT

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: RAW CATALYST CHARGE BLDG. FILTER + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - RAW CATALYST CHARGE BLDG. FILTER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: DRUM UNLOADING ENCLOSURE FILTER + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - DRUM UNLOADING ENCLOSURE FILTER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II+ Process Name: CATALYST FUGITIVES + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - CATALYST FUGITIVES

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: A 28MID PROGRAM WILL BE USED. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: CATALYST ACTIVATOR DIRECT HEATER + Process Type: 63.999

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - CATALYST ACTIVATOR DIRECT HEATER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GUARANTEED TO MEET 0.06 LB NOX/ MMBTU + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Sulfur Oxides (SOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P+ Control Method Description: FUEL GAS WITH < 3.6 PPMV H2S + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: ELEVATED FLARE + Process Type: 19.310

Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - ELEVATED FLARE

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: FORMOSA- HIGH DENSITY POLYETHYLENE II

+ Process Name: COOLING TOWER + Process Type: 99.009Pollutant Information: FORMOSA- HIGH DENSITY POLYETHYLENE II - COOLING TOWER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: WILL DO MONTHLY SAMPLING + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: JACUZZI WHIRLPOOL BATH

RBLC ID: CA-1106 + Corporate/Company Name: JACUZZI WHIRLPOOL BATH + Facility Name: JACUZZI WHIRLPOOL BATH Facility County: SAN BERNARDINO Facility State: CA Facility ZIP Code: 91708 + SIC Code: 3089 NAICS Code: 325211 Permit Issuance Date: 10/15/2002 ACT

Process Information: JACUZZI WHIRLPOOL BATH

+ Process Name: RESIN MANUFACTURING: POLYESTER RESIN OPERATIONSHAND AND SPRAY LAYUP + Process Type: 63.026

Pollutant Information: JACUZZI WHIRLPOOL BATH - RESIN MANUFACTURING: POLYESTER RESIN OPERATIONS- HAND AND SPRAY LAYUP

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CONCENTRATOR AND CATALYTIC OXIDIZER + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID.NOTE: Draft determinations are marked with a " * " beside the RBLC ID.

Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: LA PORTE POLYPROPYLENE PLANT

RBLC ID: TX-0378 + Corporate/Company Name: ATOFINA PETROCHEMICALS INC + Facility Name: LA PORTE POLYPROPYLENE PLANT Facility County: HARRIS Facility State: TX Facility ZIP Code: 77536 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 11/05/2001 ACT

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: COOLING TOWER + Process Type: 99.009

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - COOLING TOWER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: PACKAGE BOILER + Process Type: 19.600

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - PACKAGE BOILER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2)+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: STANDBY INCINERATOR + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - STANDBY INCINERATOR

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE INICINERATOR IS A VOC CONTROL + Percent Efficiency: 99.990

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Hydrochloric Acid Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) , InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: WASTE HEAT BOILER + Process Type: 19.600

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - WASTE HEAT BOILER

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:+ Pollutant Name Hydrochloric Acid Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) , InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE WASTE HEAT BOILER IS A VOC CONTROL DEVICE + Percent Efficiency: 99.990

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: REGENERATIVE GAS HEATER + Process Type: 19.600

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - REGENERATIVE GAS HEATER

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE REG. GAS HEATER IS A VOC CONTROL + Percent Efficiency: 99.990

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: MONUMENT NO. 2 FLARE + Process Type: 19.310

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - MONUMENT NO. 2 FLARE

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE FLARE IS A VOC CONTROL DEVICE + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: PACKAGE BOILER BO-4 + Process Type: 13.310

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - PACKAGE BOILER BO-4

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: ULTRA LOW-NOX BURNERS + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: (4) CARLOT SILO BLENDERS + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - (4) CARLOT SILO BLENDERS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAG FILTER+ Percent Efficiency:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: BAGFILTER + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: (4) PELLET LINE LOT BLENDER + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - (4) PELLET LINE LOT BLENDER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: PELLET OFFSPEC BIN + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - PELLET OFFSPEC BIN

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: BAGGING BIN VENT FILTER + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - BAGGING BIN VENT FILTER

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: FILTER + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FILTER + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: ALKYL SEAL POT + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - ALKYL SEAL POT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED+ Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: ADDITIVE FEED HOPPER VENT FILTER + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - ADDITIVE FEED HOPPER VENT FILTER

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: FILTER + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FILTER + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: (2) PELLET DRYER EXHAUST + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - (2) PELLET DRYER EXHAUST

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: COOLING WATER ADDITIVE TANKS + Process Type: 63.999Pollutant Information: LA PORTE POLYPROPYLENE PLANT - COOLING WATER ADDITIVE TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: BOILER WATER ADDITIVE TANKS + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - BOILER WATER ADDITIVE TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: (2) POWDER MASTERBATCH WEIGHT BIN VENT FILTER + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - (2) POWDER MASTERBATCH WEIGHT BIN VENT FILTER

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: FILTER + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FILTER+ Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FILTER + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: (2) PELLET REFEED BIN VENT + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - (2) PELLET REFEED BIN VENT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: (2) INLINE BLENDER VENT FILTER + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - (2) INLINE BLENDER VENT FILTER+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FILTER + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FILTER + Percent Efficiency:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: FILTER + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: FUGITIVES + Process Type: 63.999

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28 MID + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: VACUUM CLEANING SYSTEM + Process Type: 63.999Pollutant Information: LA PORTE POLYPROPYLENE PLANT - VACUUM CLEANING SYSTEM

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: TRAIN NO. 8 FLARE + Process Type: 19.310

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - TRAIN NO. 8 FLARE

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE FLARE IS A VOC CONTROL + Percent Efficiency: 98.000

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LA PORTE POLYPROPYLENE PLANT

+ Process Name: ALKYL FLARE + Process Type: 19.310

Pollutant Information: LA PORTE POLYPROPYLENE PLANT - ALKYL FLARE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE FLARE IS A VOC CONTROL DEVICE + Percent Efficiency: 98.000

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID.NOTE: Draft determinations are marked with a " * " beside the RBLC ID.

Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: LIMA CHEMICALS COMPLEX

RBLC ID: OH-0256 + Corporate/Company Name: BRITISH PETROLEUM CHEMICALS, INC. + Facility Name: LIMA CHEMICALS COMPLEX Facility County: ALLEN Facility State: OH Facility ZIP Code: 45802-0628 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 07/10/2003 ACT

Process Information: LIMA CHEMICALS COMPLEX

+ Process Name: MALEIC ANHYDRIDE REACTOR + Process Type: 63.015

Pollutant Information: LIMA CHEMICALS COMPLEX - MALEIC ANHYDRIDE REACTOR

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: A + Control Method Description: SOGI - SCRUBBER OFF-GAS INCINERATOR + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: SOGI - SCRUBBER OFF-GAS INCINERATOR + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: A + Control Method Description: INCORPORATES SCRUBBER OFF-GAS INCINERATOR (SOGI) + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC)+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: SCRUBBER OFFGAS INCINERATOR + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE, FABRIC FILTER + Percent Efficiency:

Process Information: LIMA CHEMICALS COMPLEX

+ Process Name: MALEIC ACID HYDROGENATION + Process Type: 63.015

Pollutant Information: LIMA CHEMICALS COMPLEX - MALEIC ACID HYDROGENATION

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: TWO ALTERNATIVE 1) PLANT PROCESS FLARE AND 2) HYDROGEN PLANT REFORMER FURNACE + Percent Efficiency: 98.000

Process Information: LIMA CHEMICALS COMPLEX

+ Process Name: BUTANEDIOL RECOVERY AND PURIFICATION + Process Type: 63.015

Pollutant Information: LIMA CHEMICALS COMPLEX - BUTANEDIOL RECOVERY AND PURIFICATION

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: TWO ALTERNATIVE CONTROL DEVICES 1)PLANT PROCESS FLARE SYSTEM AND 2) SCRUBBER OFFGAS INCINERATOR + Percent Efficiency: 98.000

+ Pollutant Name Hazardous Air Pollutants (HAP) Pollutant Group(s): ( Hazardous Air Pollutants (HAP) ) + Control Method Code: A+ Control Method Description: PLANT PROCESS FLARE OR SCRUBBER OFFGAS INCINERATOR + Percent Efficiency: 98.000

Process Information: LIMA CHEMICALS COMPLEX

+ Process Name: BUTANE FEEDSTOCK SUPPLY + Process Type: 63.015

Pollutant Information: LIMA CHEMICALS COMPLEX - BUTANE FEEDSTOCK SUPPLY

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: PLANT PROCESS FLARE SYSTEM, SCRUBBER OFFGAS INCINERATOR + Percent Efficiency: 98.000

Process Information: LIMA CHEMICALS COMPLEX

+ Process Name: HYDROGEN SUPPLY SYSTEM + Process Type: 63.015

Pollutant Information: LIMA CHEMICALS COMPLEX - HYDROGEN SUPPLY SYSTEM

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS, GOOD COMBUSTION CONTROL IN REFORMING FURNACE + Percent Efficiency:

Process Information: LIMA CHEMICALS COMPLEX

+ Process Name: COOLING TOWER + Process Type: 99.009Pollutant Information: LIMA CHEMICALS COMPLEX - COOLING TOWER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: DRIFT ELIMINATORS + LDAR PROGRAM + Percent Efficiency:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: P + Control Method Description: DRIFT ELIMINATORS + LDAR + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: DRIFT ELIMINATORS + LDAR PROGRAM + Percent Efficiency:

Process Information: LIMA CHEMICALS COMPLEX

+ Process Name: BUTANEDIOL PRODUCT STORAGE + Process Type: 63.015

Pollutant Information: LIMA CHEMICALS COMPLEX - BUTANEDIOL PRODUCT STORAGE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FIXED ROOF TANKS, INTERNAL FLOATING ROOF TANKS + USE OF SUBMERGED FILL AND LDAR PROGRAM. + Percent Efficiency:

Process Information: LIMA CHEMICALS COMPLEX

+ Process Name: TETRAHYDROFURAN BY-PRODUCT STORAGE + Process Type: 63.015

Pollutant Information: LIMA CHEMICALS COMPLEX - TETRAHYDROFURAN BY-PRODUCT STORAGE+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FIXED ROOF TANK WITH INTERNAL FLOATING ROOF AND LDAR PROGRAM. + Percent Efficiency:

Process Information: LIMA CHEMICALS COMPLEX

+ Process Name: PRODUCT LOADING + Process Type: 63.015

Pollutant Information: LIMA CHEMICALS COMPLEX - PRODUCT LOADING

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: SUBMERGED FILL AND LDAR PROGRAM + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

RBLC ID: TX-0268 + Corporate/Company Name: UNION CARBIDE CHEM & PLASTICS CO. INC. + Facility Name: LOW PRESSURE POLYETHYLENE PLANT NO. 2 Facility County: CALHOUN Facility State: TX Facility ZIP Code: 77979 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 03/06/1997 ACT

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: LARGE FLARE + Process Type: 19.310Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - LARGE FLARE

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Aluminum Oxide Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Hydrochloric Acid Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) , InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: NO. 2 SILICA ACTIVATOR + Process Type: 63.999Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - NO. 2 SILICA ACTIVATOR

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED. BACT IS APPLIED. + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: NO. 2 SILICA ACTIVATOR BLOW TANK + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - NO. 2 SILICA ACTIVATOR BLOW TANK

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. BACT IS APPLIED. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: SILICA BIN 6 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - SILICA BIN 6

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. BACT IS APPLIED. + Percent Efficiency:Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: SILICA BIN 7 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - SILICA BIN 7

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: G-3 BLENDER BLOW TANK + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - G-3 BLENDER BLOW TANK

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: CATALYST BINS 25, 26, 27, AND 28 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - CATALYST BINS 25, 26, 27, AND 28

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: MIDDLE, NORTH, SOUTH, AND CATALYST BLOW TANK (4) + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - MIDDLE, NORTH, SOUTH, AND CATALYST BLOW TANK (4)

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: G-1 NO. & SO., G-2 NO. & SO. CATALYST FEEDERS (4) + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - G-1 NO. & SO., G-2 NO. & SO. CATALYST FEEDERS (4)

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: G-1 & G-2 SEAL SYSTEM VENTS + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - G-1 & G-2 SEAL SYSTEM VENTS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PROCESS VENTS ROUTED TO ONE OF TWO FLARES. VENTS NOT ROUTED TO FLARES ARE EITHER INSIGNIFICANT, TECHNICALLY INFEASIBLE, OR ECONOMICALLY PROHBITIVE. IT IS NOT INDICATED WHICH ARE ROUTED TO FLARES.+ Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: G-1 AND G-2 FLUID BED COOLER + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - G-1 AND G-2 FLUID BED COOLER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PURGING IN BINS UPSTREAM REMOVES >95% OF ENTRAINED VOC. + Percent Efficiency:

+ Pollutant Name Ethylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: COMBINED ALLOWABLES- ENTRY NO. 1 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - COMBINED ALLOWABLES- ENTRY NO. 1

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PURGING IN THE BINS UPSTREAM REMOVES >95% OF ENTRAINED VOC. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: COMBINED ALLOWABLES- ENTRY NO. 2 + Process Type: 63.999Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - COMBINED ALLOWABLES- ENTRY NO. 2

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PURGING IN THE BINS UPSTREAM REMOVES >95% OF ENTRAINED VOC. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: NO. 1 TRIM VENT + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - NO. 1 TRIM VENT

+ Pollutant Name Ethylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: NO. 2 TRIM VENT + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - NO. 2 TRIM VENT

+ Pollutant Name Ethylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: RESIN BINS NOS. 101, 102, AND 103 + Process Type: 63.999Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - RESIN BINS NOS. 101, 102, AND 103

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PURGING IN THE BINS UPSTREAM REMOVES >95% OF ENTRAINED VOC. + Percent Efficiency:

+ Pollutant Name Ethylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: RESIN BINS NOS. 201, 202, AND 203 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - RESIN BINS NOS. 201, 202, AND 203

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PURGING IN THE BINS UPSTREAM REMOVES >95% OF ENTRAINED VOC. + Percent Efficiency:

+ Pollutant Name Ethylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: NOS. 1 & 2 TRANSFER CONV SEP & DED TRANS SYSTEM + Process Type: 63.999Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - NOS. 1 & 2 TRANSFER CONV SEP & DED TRANS SYSTEM

+ Pollutant Name Ethylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: NOS. 1 & 2 LOADING CONVEYOR SEPARATOR + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - NOS. 1 & 2 LOADING CONVEYOR SEPARATOR

+ Pollutant Name Ethylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: LOADING ADDITIVE TRANSFER SYSTEM + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - LOADING ADDITIVE TRANSFER SYSTEM

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description:+ Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: UNIT FUGITIVES BLOCK 26 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - UNIT FUGITIVES BLOCK 26

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: MONITORED BY 28M + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: ANALYZER VENTS + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - ANALYZER VENTS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PROCESS VENTS ARE ROUTED TO ONE OF TWO FLARE SYSTEMS. EACH PROVIDES 98% DRE. VENTS NOT ROUTED TO FLARES ARE EITHER INSIGNIFICANT, OR IT IS NOT TECHNICALLY OR ECONOMICALLY FEASIBLE. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: PELLETED MASTER BATCH BAGHOUSE + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - PELLETED MASTER BATCH BAGHOUSE

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A+ Control Method Description: BAGHOUSE + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: GRANULAR MASTER BATCH BAGHOUSE + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - GRANULAR MASTER BATCH BAGHOUSE

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: P1 TRIM BIN FILTER + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - P1 TRIM BIN FILTER

+ Pollutant Name Ethylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: P1 FEED HOPPER FILTER + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - P1 FEED HOPPER FILTER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P+ Control Method Description: PURGING IN THE BINS UPSTREAM REMOVES >95% OF ENTRAINED VOC. + Percent Efficiency:

+ Pollutant Name Ethylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: P1 ADDITIVE (GRANULAR) FILTER + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - P1 ADDITIVE (GRANULAR) FILTER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: P1 ADDITIVE (PELLETED) FILTER + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - P1 ADDITIVE (PELLETED) FILTER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: P1 PELLET DRYER EXHAUST + Process Type: 63.999Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - P1 PELLET DRYER EXHAUST

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PURGING IN THE BINS UPSTREAM REMOVES >95% OF ENTRAINED VOC. + Percent Efficiency:

+ Pollutant Name Ethylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: P1 ELUTRIATOR FILTER + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - P1 ELUTRIATOR FILTER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: SMALL FLARE + Process Type: 19.310

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - SMALL FLARE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE FLARE IS THE CONTROL DEVICE FOR VOC EMISSIONS. BACT IS APPLIED.+ Percent Efficiency: 98.000

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. BACT IS APPLIED. + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED. BACT IS APPLIED. + Percent Efficiency:

+ Pollutant Name Hydrochloric Acid Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) , InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. BACT IS APPLIED. + Percent Efficiency:

+ Pollutant Name Aluminum Oxide Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. BACT IS APPLIED. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: CATALYST BIN 29 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - CATALYST BIN 29

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: CATALYST BIN 30 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - CATALYST BIN 30

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: MICROTALC FILTER + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - MICROTALC FILTER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: FUGITIVES, BLOCK 12 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - FUGITIVES, BLOCK 12

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: MONITORED BY 28M + Percent Efficiency:Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: FUGITIVES, BLOCK 25 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - FUGITIVES, BLOCK 25

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: MONITORED BY 28M + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: FUGITIVES, BLOCK 17 + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - FUGITIVES, BLOCK 17

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: MONITORED BY 28M. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: ADDITIVE FEEDER + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - ADDITIVE FEEDER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED + Percent Efficiency:Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: NO. 1 GRANULAR MAKE BAGHOUSE + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - NO. 1 GRANULAR MAKE BAGHOUSE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PURGING IN THE BINS UPSTREAM REMOVES >95% OF ENTRAINED VOC. + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: NO. 2 GRANULAR MAKE BAGHOUSE + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - NO. 2 GRANULAR MAKE BAGHOUSE

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PURGING IN BINS UPSTREAM REMOVES >95% OF ENTRAINED VOC. + Percent Efficiency:Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: P-1 ADDITIVE CONVEYOR + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - P-1 ADDITIVE CONVEYOR

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Process Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2

+ Process Name: NOS. 1 & 2 LOADING ADDITIVE HOPPER + Process Type: 63.999

Pollutant Information: LOW PRESSURE POLYETHYLENE PLANT NO. 2 - NOS. 1 & 2 LOADING ADDITIVE HOPPER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED. + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: MARKEL CORPORATION

RBLC ID: PA-0168 + Corporate/Company Name: MARKEL CORPORATION + Facility Name: MARKEL CORPORATION Facility County: MONTGOMERY Facility State: PA Facility ZIP Code: 19404 + SIC Code: 3087NAICS Code: 325991 Permit Issuance Date: 03/22/2000 ACT

Process Information: MARKEL CORPORATION

+ Process Name: HORIZONTAL EXTRUDER + Process Type: 63.999

Pollutant Information: MARKEL CORPORATION - HORIZONTAL EXTRUDER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: EXHAUST INTO EXISTING CONTROL EQUIPMENT (CATALYTIC OXIDIZER). + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: MUSKOGEE MILL

RBLC ID: OK-0112 + Corporate/Company Name: FORT JAMES OPERATING CO + Facility Name: MUSKOGEE MILL Facility County: MUSKOGEE Facility State: OK Facility ZIP Code: + SIC Code: 2656 NAICS Code: 322121 Permit Issuance Date: 03/27/2006 ACT

Process Information: MUSKOGEE MILL

+ Process Name: PAPER MACHINE COMBUSTION #11-14 + Process Type: 19.600

Pollutant Information: MUSKOGEE MILL - PAPER MACHINE COMBUSTION #11-14

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N+ Control Method Description: EXISTING CONTROL - CLEAN FUEL + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: EXISTING CONTROL - CLEAN FUEL + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: EXISTING CONTROL - GOOD COMBUSTION PRACTICES + Percent Efficiency:

Process Information: MUSKOGEE MILL

+ Process Name: PAPER MACHINE + Process Type: 30.420

Pollutant Information: MUSKOGEE MILL - PAPER MACHINE

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NEW SUBSTANCE REVIEW + Percent Efficiency:

Process Information: MUSKOGEE MILL

+ Process Name: CONVERTING AREA VENT + Process Type: 30.290

Pollutant Information: MUSKOGEE MILL - CONVERTING AREA VENT

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: EXISTING CONTROL - BAGHOUSE + Percent Efficiency:

Process Information: MUSKOGEE MILL

+ Process Name: POLYETHYLENE FLEXOGRAPHIC PRINTING PRESS #2-4 + Process Type: 41.021

Pollutant Information: MUSKOGEE MILL - POLYETHYLENE FLEXOGRAPHIC PRINTING PRESS #2-4

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PERMANENT ENCLOSURE, RTO + Percent Efficiency:

Process Information: MUSKOGEE MILL

+ Process Name: POLYETHYLENE EXTRUDERS #2-4 + Process Type: 63.999

Pollutant Information: MUSKOGEE MILL - POLYETHYLENE EXTRUDERS #2-4

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) )+ Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: MUSKOGEE MILL

+ Process Name: NEW PLATE WASHER/MAKING + Process Type: 41.021

Pollutant Information: MUSKOGEE MILL - NEW PLATE WASHER/MAKING

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: WASHER INHERENT DESIGN + Percent Efficiency:

Process Information: MUSKOGEE MILL

+ Process Name: PULPING SYSTEM 5 + Process Type: 30.490

Pollutant Information: MUSKOGEE MILL - PULPING SYSTEM 5

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: EXISTING CONTROL - NO USE OF CHLORINE OR CHLORINE DIOXIDE + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: NAVIGATOR YACHTS

RBLC ID: CA-1067 + Corporate/Company Name: NAVIGATOR YACHTS + Facility Name: NAVIGATOR YACHTS Facility County: RIVERSIDEFacility State: CA Facility ZIP Code: 92370 + SIC Code: 2821 NAICS Code: 325210 Permit Issuance Date: 11/24/1999 ACT

Process Information: NAVIGATOR YACHTS

+ Process Name: RESIN MANUFACTURING: POLYESTER RESIN OPERATIONSHAND AND SPRAY LAYUP + Process Type: 63.026

Pollutant Information: NAVIGATOR YACHTS - RESIN MANUFACTURING: POLYESTER RESIN OPERATIONS- HAND AND SPRAY LAYUP

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CARBON ABSORBER/ON-SITE REGENERATION USING THERMAL OXIDIZER + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: OXY VINYLS COGENERATION UNIT NOS 1 AND 2

RBLC ID: TX-0510 + Corporate/Company Name: OXY VINYLS + Facility Name: OXY VINYLS COGENERATION UNIT NOS 1 AND 2 Facility County: HARRIS Facility State: TX Facility ZIP Code: + SIC Code: 351 NAICS Code: 333611 Permit Issuance Date: 02/28/2006 ACT

Process Information: OXY VINYLS COGENERATION UNIT NOS 1 AND 2

+ Process Name: NO. 1/2 HEAT RECOVERY STEAM GENERATION STACK + Process Type: 63.999Pollutant Information: OXY VINYLS COGENERATION UNIT NOS 1 AND 2 - NO. 1/2 HEAT RECOVERY STEAM GENERATION STACK

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: OXY VINYLS COGENERATION UNIT NOS 1 AND 2

+ Process Name: NO. 3 HEAT RECOVERY STEAM GENERATION STACK + Process Type: 63.999Pollutant Information: OXY VINYLS COGENERATION UNIT NOS 1 AND 2 - NO. 3 HEAT RECOVERY STEAM GENERATION STACK

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Previous PageNOTE: Draft determinations are marked with a " * " beside the RBLC ID.

Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: PHILLIPS CHEMICAL COMPANY

RBLC ID: TX-0236 + Corporate/Company Name: PHILLIPS CHEMICAL COMPANY + Facility Name: PHILLIPS CHEMICAL COMPANY Facility County: HARRIS Facility State: TX Facility ZIP Code: 77501 + SIC Code: 2821 NAICS Code: Permit Issuance Date: 12/15/1998 ACT

Process Information: PHILLIPS CHEMICAL COMPANY

+ Process Name: POLYOLEFINS - MFG. + Process Type: 63.999

Pollutant Information: PHILLIPS CHEMICAL COMPANY - POLYOLEFINS - MFG.

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: LAER W/FLARE MONITORING, VENT PRODUCT OFF-GASES/ PRODUCT LOADING EMISSIONS TO FLARE + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: PLAQUEMINE PVC PLANT

RBLC ID: LA-0204 + Corporate/Company Name: SHINTECH LOUISIANA LLC + Facility Name: PLAQUEMINE PVC PLANT Facility County: IBERVILLE Facility State: LA Facility ZIP Code: + SIC Code: 2821NAICS Code: 325211 Permit Issuance Date: 02/27/2009 ACT

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: ANALYZER VENT 2 (M-10) + Process Type: 63.999

Pollutant Information: PLAQUEMINE PVC PLANT - ANALYZER VENT 2 (M-10)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: BOILERS A & B (U-1 & U-2) + Process Type: 12.390

Pollutant Information: PLAQUEMINE PVC PLANT - BOILERS A & B (U-1 & U-2)

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND USE OF GASEOUS FUEL + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: LOW NOX BURNERS AND FLUE GAS RECIRCULATION + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND USE OF GASEOUS FUEL + Percent Efficiency:Process Information: PLAQUEMINE PVC PLANT

+ Process Name: BOILERS C & D (U-3 & U-4) + Process Type: 12.390

Pollutant Information: PLAQUEMINE PVC PLANT - BOILERS C & D (U-3 & U-4)

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND USE OF NATURAL GAS AS FUEL + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: LOW NOX BURNERS AND FLUE GAS RECIRCULATION + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND USE OF NATURAL GAS AS FUEL + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: CRACKING FURNACES A-D + Process Type: 13.310

Pollutant Information: PLAQUEMINE PVC PLANT - CRACKING FURNACES A-D

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND USE OF NATURAL GAS AS FUEL + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) )+ Control Method Code: B + Control Method Description: LOW NOX BURNERS AND SELECTIVE CATALYTIC REDUCTION (SCR) + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND USE OF NATURAL GAS AS FUEL + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: GAS THERMAL OXIDIZERS A & B (M-5 & M-6) + Process Type: 19.200

Pollutant Information: PLAQUEMINE PVC PLANT - GAS THERMAL OXIDIZERS A & B (M-5 & M-6)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: GOOD COMBUSTION PRACTICES AND SELECTIVE CATALYTIC REDUCTION (SCR) + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND USE OF GASEOUS FUEL + Percent Efficiency:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND USE OF GASEOUS FUEL + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: PVC DRYER SCRUBBERS A & B (P-1 & P-2) + Process Type: 63.036Pollutant Information: PLAQUEMINE PVC PLANT - PVC DRYER SCRUBBERS A & B (P-1 & P-2)

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE AND SCRUBBER + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: C/A COOLING TOWER (C-4) + Process Type: 99.009

Pollutant Information: PLAQUEMINE PVC PLANT - C/A COOLING TOWER (C-4)

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD DESIGN, MAINTENANCE, AND INTEGRATED DRIFT ELIMINATORS + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: VCM COOLING TOWER (M-7) + Process Type: 99.009

Pollutant Information: PLAQUEMINE PVC PLANT - VCM COOLING TOWER (M-7)

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD DESIGN, MAINTENANCE, AND INTEGRATED DRIFT ELIMINATORS + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: COOLING TOWER (P-15) + Process Type: 99.009Pollutant Information: PLAQUEMINE PVC PLANT - COOLING TOWER (P-15)

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD DESIGN, MAINTENANCE, AND INTEGRATED DRIFT ELIMINATORS + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: DELIVERY SILOS A-F (P-3 - P-8) + Process Type: 63.999

Pollutant Information: PLAQUEMINE PVC PLANT - DELIVERY SILOS A-F (P-3 - P-8)

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE FOLLOWED BY A BAGHOUSE + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: ROAD - FUGITIVE DUST + Process Type: 99.140

Pollutant Information: PLAQUEMINE PVC PLANT - ROAD - FUGITIVE DUST

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PAVINGS ROADS AS MUCH AS PRACTICABLE + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: H/C CLEANING SILO (P-9) + Process Type: 63.999

Pollutant Information: PLAQUEMINE PVC PLANT - H/C CLEANING SILO (P-9)+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE FOLLOWED BY A BAGHOUSE + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: LOADING HOPPERS (P-25, P-26, P-27) + Process Type: 63.036

Pollutant Information: PLAQUEMINE PVC PLANT - LOADING HOPPERS (P-25, P-26, P-27)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD DESIGN AND MAINTENANCE + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: SMALL EMERGENCY ENGINES + Process Type: 17.210

Pollutant Information: PLAQUEMINE PVC PLANT - SMALL EMERGENCY ENGINES

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND GASEOUS FUEL BURNING + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND GASEOUS FUEL BURNING + Percent Efficiency:

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P+ Control Method Description: GOOD COMBUSTION PRACTICES AND GASEOUS FUEL BURNING + Percent Efficiency:

Process Information: PLAQUEMINE PVC PLANT

+ Process Name: LARGE EMERGENCY ENGINES + Process Type: 17.110

Pollutant Information: PLAQUEMINE PVC PLANT - LARGE EMERGENCY ENGINES

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND GASEOUS FUEL BURNING + Percent Efficiency:

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND GASEOUS FUEL BURNING + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND GASEOUS FUEL BURNING + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: PLASTICS MANUFACTURING

RBLC ID: TX-0589 + Corporate/Company Name: EQUISTAR CHEMICALS, LP + Facility Name: PLASTICS MANUFACTURING Facility County: MATAGORDA Facility State: TXFacility ZIP Code: 77414 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 01/18/2011 ACT

Process Information: PLASTICS MANUFACTURING

+ Process Name: High Density Polyethylene manufacturing + Process Type: 63.999

Pollutant Information: PLASTICS MANUFACTURING - High Density Polyethylene manufacturing

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: A Flare controls process venting from the HD Polyethylene manufacturing as well as vent gases from maintenance, startup and shutdown (MSS) activities and emission events. The flare is expected to achieve at least 98% destruction efficiency. Supplemental fuel is added if needed to maintain the input gas heat content at a minimum of 300 Btu/scf. A thermocouple and alarm are installed on each pilot to monitor flame integrity. The flare is designed for smokeless operation. It has a liquid knockout system, a feed gas flow monitor analyzer and gas chromatograph analyzer. + Percent Efficiency: 98.000

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: SOLUTIA, INC.

RBLC ID: TX-0243 + Corporate/Company Name: SOLUTIA, INC. + Facility Name: SOLUTIA, INC. Facility County: BRAZORIA Facility State: TX Facility ZIP Code: 77512 + SIC Code: 2869 NAICS Code: Permit Issuance Date: 11/05/1998 ACTProcess Information: SOLUTIA, INC.

+ Process Name: ACRYLONITRILE MFG. + Process Type: 63.002

Pollutant Information: SOLUTIA, INC. - ACRYLONITRILE MFG.

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: WASTE HEAT BOILER (99.99% DRE), 28 LAER, GAS CHROMATOGRAPHY, FLARE (99% DRE) + Percent Efficiency:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: WASTE HEAT BOILER WITH NH3 INJECTION + Percent Efficiency:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: WASTE HEAT BOILER WITH NH3 INJECTION, FLARE + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: SPARTECH PLASTICS

RBLC ID: CA-1107 + Corporate/Company Name: SPARTECH PLASTICS + Facility Name: SPARTECH PLASTICS Facility County: LOS ANGELES Facility State: CA Facility ZIP Code: 90638 + SIC Code: 3089 NAICS Code: 326199Permit Issuance Date: 03/24/2000 ACT

Process Information: SPARTECH PLASTICS

+ Process Name: PLASTIC AND RESIN EXTRUSION + Process Type: 63.999

Pollutant Information: SPARTECH PLASTICS - PLASTIC AND RESIN EXTRUSION

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: AFTER BURNER + Percent Efficiency:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: WESTLAKE PETROCHEMICALS CORPORATION

RBLC ID: LA-0110 + Corporate/Company Name: WESTLAKE PETROCHEMICALS CORPORATION + Facility Name: WESTLAKE PETROCHEMICALS CORPORATION Facility County: CALCASIEU PARISH Facility State: LA Facility ZIP Code: 70602- + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 04/23/1997 ACT

Process Information: WESTLAKE PETROCHEMICALS CORPORATION

+ Process Name: POLYETHYLENE PLANT, PROCESS VENTS, FLARES + Process Type: 19.310

Pollutant Information: WESTLAKE PETROCHEMICALS CORPORATION - POLYETHYLENE PLANT, PROCESS VENTS, FLARES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A+ Control Method Description: FLARES + Percent Efficiency: 98.000

Process Information: WESTLAKE PETROCHEMICALS CORPORATION

+ Process Name: POLYETHYLENE PLANT + Process Type: 63.999

Pollutant Information: WESTLAKE PETROCHEMICALS CORPORATION - POLYETHYLENE PLANT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: STRIPPING ETHYLENE RESIDUE IN PE POWDER TO 60 PPMW + Percent Efficiency:

Previous PagePrevious Page

NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: ACE ETHANOL - STANLEY

RBLC ID: WI-0207 + Corporate/Company Name: ACE ETHANOL, LLC + Facility Name: ACE ETHANOL - STANLEY Facility County: CHIPPEWA Facility State: WI Facility ZIP Code: 547681085 + SIC Code: 2869 NAICS Code: 325193 Permit Issuance Date: 01/21/2004 ACT

Process Information: ACE ETHANOL - STANLEY

+ Process Name: DDGS DRYER, COOLING CYCLONE, P40, P41, P42 + Process Type: 19.600

Pollutant Information: ACE ETHANOL - STANLEY - DDGS DRYER, COOLING CYCLONE, P40, P41, P42

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW / ULTRA LOW NOX BURNERS Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE, RTO Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method+ Control Method Description: THERMAL OXIDIZER (REGENERATIVE) Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: A + Control Method Description: THERMAL OXIDIZER (REGENERATIVE) Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: BOILER, S50/B50, 60 MMBTU/H + Process Type: 13.310

Pollutant Information: ACE ETHANOL - STANLEY - BOILER, S50/B50, 60 MMBTU/H

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: NATURAL GAS/ PROPANE; GOOD COMBUSTION CONTROL Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNER Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: NATURAL GAS / PROPANE; GOOD COMBUSTION CONTROL Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: NATURAL GAS / PROPANE, GOOD COMBUSTION CONTROLS Cost Effectiveness:Process Information: ACE ETHANOL - STANLEY

+ Process Name: BOILER, S51/B51, 80 MMBTU/H + Process Type: 13.310

Pollutant Information: ACE ETHANOL - STANLEY - BOILER, S51/B51, 80 MMBTU/H

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: NAT. GAS / PROPANE, LOW NOX BURNER Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: NAT. GAS / PROPANE, GOOD COMBUSTION CONTROL Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: NAT. GAS / PROPANE; GOOD COMBUSTION CONTROL Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: NATURAL GAS, GOOD COMBUSTION CONTROL Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: BOILER, S52/B52, 11 MMBTU/H + Process Type: 13.310

Pollutant Information: ACE ETHANOL - STANLEY - BOILER, S52/B52, 11 MMBTU/H

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P+ Control Method Description: NATURAL GAS / PROPANE; GOOD COMBUSTION CONTROL Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: NATURAL GAS / PROPANE; LOW NOX BURNER Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: NATURAL GAS / PROPANE ; GOOD COMBUSTION CONTROL Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: NATURAL GAS / PROPANE; GOOD COMBUSTION CONTROL Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: BOILER, S53 / B53, 34 MMBTU/H + Process Type: 13.310

Pollutant Information: ACE ETHANOL - STANLEY - BOILER, S53 / B53, 34 MMBTU/H

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: NATURAL GAS / PROPANE; GOOD COMBUSTION CONTROL Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: NATURAL GAS / PROPANE; LOW NOX BURNER Cost Effectiveness:+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: NATURAL GAS / PROPANE; GOOD COMBUSTION CONTROL Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: NATURAL GAS / PROPANE; GOOD COMBUSTION CONTROL Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: IC ENGINE, DIESEL GENERATOR SET, B70 + Process Type: 17.110

Pollutant Information: ACE ETHANOL - STANLEY - IC ENGINE, DIESEL GENERATOR SET, B70

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: USE OF VERY LOW SULFUR DIESEL FUEL (0.05 WT % S). Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LIMIT ON HOURS OF OPERATION (16.7 HRS/MO, 12 MO. AVG.) Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: LIMITED OPERATION, DESIGN Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) )+ Control Method Code: P + Control Method Description: LIMITED OPERATION, DESIGN Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: FUGITIVE EMISSIONS (TRUCK TRAFFIC, GRAIN, DDGS) + Process Type: 99.190

Pollutant Information: ACE ETHANOL - STANLEY - FUGITIVE EMISSIONS (TRUCK TRAFFIC, GRAIN, DDGS)

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GENERAL FUGITIVE LIMITATIONS (E.G. WATER APPLICATION, SWEEPING) Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: STORAGE TANKS + Process Type: 42.009

Pollutant Information: ACE ETHANOL - STANLEY - STORAGE TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FIXED ROOF TANKS WITH INTERNAL FLOATING ROOF (SUBJECT TO NSPS) Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: LOADING RACK, F01/S35 + Process Type: 49.999

Pollutant Information: ACE ETHANOL - STANLEY - LOADING RACK, F01/S35

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method+ Control Method Description: FLARE Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: COOLING TOWERS, F06 + Process Type: 99.009

Pollutant Information: ACE ETHANOL - STANLEY - COOLING TOWERS, F06

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: MIST ELIMINATORS Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: MIST ELIMINATORS Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: MILLING, SURGE BIN (P01, P02, P15) + Process Type: 70.290

Pollutant Information: ACE ETHANOL - STANLEY - MILLING, SURGE BIN (P01, P02, P15)

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: GRAIN STORAGE BUILDING (P03) + Process Type: 70.290Pollutant Information: ACE ETHANOL - STANLEY - GRAIN STORAGE BUILDING (P03)

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD OPERATING PRACTICES Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: CORN DUMP PIT & AUGER; CORN ELEV., BIN, P10 - P14 + Process Type: 70.290

Pollutant Information: ACE ETHANOL - STANLEY - CORN DUMP PIT & AUGER; CORN ELEV., BIN, P10 - P14

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: DDGS DUMP PIT, AUGER, ELEV., SPOUT, S11, P16-P19 + Process Type: 70.290

Pollutant Information: ACE ETHANOL - STANLEY - DDGS DUMP PIT, AUGER, ELEV., SPOUT, S11, P16-P19

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: DISTILLATION, MOLECULAR SIEVES, EVAP., P46-P51; + Process Type: 64.003Pollutant Information: ACE ETHANOL - STANLEY - DISTILLATION, MOLECULAR SIEVES, EVAP., P46-P51;

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: WET SCRUBBER (PACKED TOWER) Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: DISTILLATION; MOL. SIEVES, EVAP., SLURRY, P24-P29 + Process Type: 64.003

Pollutant Information: ACE ETHANOL - STANLEY - DISTILLATION; MOL. SIEVES, EVAP., SLURRY, P24-P29

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: WET SCRUBBER (PACKED TOWER) Cost Effectiveness:

Process Information: ACE ETHANOL - STANLEY

+ Process Name: FERMENTATION, P20-P23, P30, P32-P35 + Process Type: 64.001

Pollutant Information: ACE ETHANOL - STANLEY - FERMENTATION, P20-P23, P30, P32-P35

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: WET SCRUBBER (PACKED TOWER) Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform)Facility Information: ADM POLYMERS

RBLC ID: IA-0084 + Corporate/Company Name: ADM CORN PROCESSING - CLINTON + Facility Name: ADM POLYMERS Facility County: CLINTON Facility State: IA Facility ZIP Code: 52732 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 11/30/2006 ACT

Process Information: ADM POLYMERS

+ Process Name: ANTIFOAM STORAGE TANK + Process Type: 42.009

Pollutant Information: ADM POLYMERS - ANTIFOAM STORAGE TANK

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: BDO STORAGE TANK + Process Type: 42.009

Pollutant Information: ADM POLYMERS - BDO STORAGE TANK

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: FIRE PUMP ENGINE + Process Type: 17.210Pollutant Information: ADM POLYMERS - FIRE PUMP ENGINE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: EMERGENCY GENERATOR + Process Type: 17.110

Pollutant Information: ADM POLYMERS - EMERGENCY GENERATOR

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: SEED FERMENTERS + Process Type: 64.003

Pollutant Information: ADM POLYMERS - SEED FERMENTERS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:Process Information: ADM POLYMERS

+ Process Name: MAIN FERMENTERS + Process Type: 64.003

Pollutant Information: ADM POLYMERS - MAIN FERMENTERS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: BROTH HOLDING TANKS + Process Type: 64.003

Pollutant Information: ADM POLYMERS - BROTH HOLDING TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: LEAKS FROM EQUIPMENT IN VOC SERVICE + Process Type: 64.002

Pollutant Information: ADM POLYMERS - LEAKS FROM EQUIPMENT IN VOC SERVICE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LDAR (LEAK DETECTION AND REPAIR) Cost Effectiveness:

Process Information: ADM POLYMERS+ Process Name: POLYMER POWDER CONVEYING + Process Type: 64.005

Pollutant Information: ADM POLYMERS - POLYMER POWDER CONVEYING

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: EXTRUDER VACUUM PUMP + Process Type: 64.005

Pollutant Information: ADM POLYMERS - EXTRUDER VACUUM PUMP

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: PELLETIZER & DRYER + Process Type: 64.005

Pollutant Information: ADM POLYMERS - PELLETIZER & DRYER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: PELLET BLENDING SILOS + Process Type: 64.005Pollutant Information: ADM POLYMERS - PELLET BLENDING SILOS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: PELLET STORAGE BIN + Process Type: 64.005

Pollutant Information: ADM POLYMERS - PELLET STORAGE BIN

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: LOADOUT SILOS + Process Type: 64.005

Pollutant Information: ADM POLYMERS - LOADOUT SILOS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: SOLVENT RECOVERY SYSTEM + Process Type: 64.003

Pollutant Information: ADM POLYMERS - SOLVENT RECOVERY SYSTEM+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: BIOMASS & POLYMER DRYERS + Process Type: 63.999

Pollutant Information: ADM POLYMERS - BIOMASS & POLYMER DRYERS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THERMAL OXIDIZER Cost Effectiveness:

Process Information: ADM POLYMERS

+ Process Name: LAIDIG TANKS + Process Type: 42.009

Pollutant Information: ADM POLYMERS - LAIDIG TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: AIR PRODUCTS BAYTOWN I I

RBLC ID: TX-0481 + Corporate/Company Name: AIR PRODUCTS LP+ Facility Name: AIR PRODUCTS BAYTOWN I I Facility County: HARRIS Facility State: TX Facility ZIP Code: 77520 + SIC Code: 492 NAICS Code: 486210 Permit Issuance Date: 11/02/2004 ACT

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: RECTISOL VENT + Process Type: 64.003

Pollutant Information: AIR PRODUCTS BAYTOWN I I - RECTISOL VENT

+ Pollutant Name Methanol Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbonyl Sulfide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I+ Process Name: FLARE (NORMAL OPERATION) + Process Type: 19.310

Pollutant Information: AIR PRODUCTS BAYTOWN I I - FLARE (NORMAL OPERATION)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: MSS-NONCONDENSIBLES (PROPYLENE VENTING) + Process Type: 64.003

Pollutant Information: AIR PRODUCTS BAYTOWN I I - MSS-NONCONDENSIBLES (PROPYLENE VENTING)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N+ Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Propylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: PARTS WASHER + Process Type: 99.999

Pollutant Information: AIR PRODUCTS BAYTOWN I I - PARTS WASHER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: FUGITIVES (4) + Process Type: 50.007

Pollutant Information: AIR PRODUCTS BAYTOWN I I - FUGITIVES (4)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbonyl Sulfide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Hydrogen Cyanide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Propylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Methanol Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: COOLING TOWER+ Process Type: 50.005

Pollutant Information: AIR PRODUCTS BAYTOWN I I - COOLING TOWER

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: SUPPLEMENTARY COOLING TOWER + Process Type: 50.005

Pollutant Information: AIR PRODUCTS BAYTOWN I I - SUPPLEMENTARY COOLING TOWER

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: BOILER STACK + Process Type: 11.390

Pollutant Information: AIR PRODUCTS BAYTOWN I I - BOILER STACK

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method+ Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: BOILER STACK (HIGH BTU FUEL) + Process Type: 11.390

Pollutant Information: AIR PRODUCTS BAYTOWN I I - BOILER STACK (HIGH BTU FUEL)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: BOILER STACK (START UP) + Process Type: 13.390

Pollutant Information: AIR PRODUCTS BAYTOWN I I - BOILER STACK (START UP)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: DIESEL FUEL TANK + Process Type: 42.005

Pollutant Information: AIR PRODUCTS BAYTOWN I I - DIESEL FUEL TANK

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: EMERGENCY GENERATOR + Process Type: 19.800

Pollutant Information: AIR PRODUCTS BAYTOWN I I - EMERGENCY GENERATOR

+ Pollutant Name Carbon Dioxide Pollutant Group(s): ( Acid Gasses/Mist , Greenhouse Gasses (GHG) , InOrganic CompoundsPollutant Group(s): ( Acid Gasses/Mist , Greenhouse Gasses (GHG) , InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: EMERGENCY GENERATOR TANK + Process Type: 19.800

Pollutant Information: AIR PRODUCTS BAYTOWN I I - EMERGENCY GENERATOR TANK

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method+ Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: PROCESS STEAM VENT + Process Type: 64.003

Pollutant Information: AIR PRODUCTS BAYTOWN I I - PROCESS STEAM VENT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: AIR PRODUCTS BAYTOWN I I

+ Process Name: MSS PROCESS STEAM VENT + Process Type: 64.003

Pollutant Information: AIR PRODUCTS BAYTOWN I I - MSS PROCESS STEAM VENT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: ATOFINA CHEMICALS INC.

RBLC ID: KY-0091 + Corporate/Company Name: ATOFINA CHEMICALS INC. + Facility Name: ATOFINA CHEMICALS INC. Facility County: MARSHALL Facility State: KYFacility ZIP Code: 42029 + SIC Code: 2813 NAICS Code: 325120 Permit Issuance Date: 12/05/2003 ACT

Process Information: ATOFINA CHEMICALS INC.

+ Process Name: CYLINDER EVACUATION AND FILLING + Process Type: 64.004

Pollutant Information: ATOFINA CHEMICALS INC. - CYLINDER EVACUATION AND FILLING

+ Pollutant Name Hydrochlorofluorocarbons (HCFC) Pollutant Group(s): ( Greenhouse Gasses (GHG) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: A + Control Method Description: SIX OUT OF THE SEVEN UNITS USE A VAPOR RECOVERY SYSTEM Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INC.

+ Process Name: LOADING, RAIL AND TANK TRUCK + Process Type: 64.005

Pollutant Information: ATOFINA CHEMICALS INC. - LOADING, RAIL AND TANK TRUCK

+ Pollutant Name Hydrochlorofluorocarbons (HCFC) Pollutant Group(s): ( Greenhouse Gasses (GHG) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: B + Control Method Description: VAPOR RECOVERY SYSTEM, THROUGHPUT LIMITS Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INC.

+ Process Name: FUGITIVES, PACKAGE AREA + Process Type: 64.002

Pollutant Information: ATOFINA CHEMICALS INC. - FUGITIVES, PACKAGE AREA

+ Pollutant Name Hydrochlorofluorocarbons (HCFC) Pollutant Group(s): ( Greenhouse Gasses (GHG) , Organic Compounds (all) , OrganicPollutant Group(s): ( Greenhouse Gasses (GHG) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: P + Control Method Description: LEAK DETECTION AND REPAIR (LDAR) PROGRAM, QUARTERLY MONITORING Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INC.

+ Process Name: DRYER DESICCANT CHANGE-OUT + Process Type: 64.999

Pollutant Information: ATOFINA CHEMICALS INC. - DRYER DESICCANT CHANGE-OUT

+ Pollutant Name Hydrochlorofluorocarbons (HCFC) Pollutant Group(s): ( Greenhouse Gasses (GHG) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: A + Control Method Description: VAPOR RECOVERY SYSTEM Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: ATOFINA CHEMICALS INCORPORATED

RBLC ID: TX-0354 + Corporate/Company Name: ATOFINA CHEMICALS INCORPORATED + Facility Name: ATOFINA CHEMICALS INCORPORATED Facility County: JEFFERSON Facility State: TX Facility ZIP Code: 77704 + SIC Code: 2869 NAICS Code: 325199 Permit Issuance Date: 12/19/2002 ACT

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: ACROLEIN UNIT COLUMN/ FILTER CLEANING + Process Type: 64.999Pollutant Information: ATOFINA CHEMICALS INCORPORATED - ACROLEIN UNIT COLUMN/ FILTER CLEANING

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: DIESEL TANK, D-215 + Process Type: 42.009

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - DIESEL TANK, D-215

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS FOR ROOF, SEAL, VENTS, AND MAINTENANCE AS DIRECTED BY NSPS ACCORDING TO YEAR OF CONSTRUCTION, CAPACITY, AND PRESSURE OF CONTENTS. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: METHANOL TANK, D-307 + Process Type: 64.004

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - METHANOL TANK, D-307

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS FOR ROOF, SEAL, VENTS, AND MAINTENANCE AS DIRECTED BY NSPS ACCORDING TO YEAR OF CONSTRUCTION, CAPACITY, AND PRESSURE OF CONTENTS. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: METHANOL TANK, D-310 + Process Type: 64.004Pollutant Information: ATOFINA CHEMICALS INCORPORATED - METHANOL TANK, D-310

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS FOR ROOF, SEAL, VENTS, AND MAINTENANCE AS DIRECTED BY NSPS ACCORDING TO YEAR OF CONSTRUCTION, CAPACITY, AND PRESSURE OF CONTENTS. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: GASOLINE TANK, D-398 + Process Type: 42.009

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - GASOLINE TANK, D-398

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS FOR ROOF, SEAL, VENTS, AND MAINTENANCE AS DIRECTED BY NSPS ACCORDING TO YEAR OF CONSTRUCTION, CAPACITY, AND PRESSURE OF CONTENTS. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: DIESEL TANK, D-399 + Process Type: 42.009

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - DIESEL TANK, D-399

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS FOR ROOF, SEAL, VENTS, AND MAINTENANCE AS DIRECTED BY NSPS ACCORDING TO YEAR OF CONSTRUCTION, CAPACITY, AND PRESSURE OF CONTENTS. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: METHANOL TANK, D-2307 + Process Type: 64.004Pollutant Information: ATOFINA CHEMICALS INCORPORATED - METHANOL TANK, D-2307

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS FOR ROOF, SEAL, VENTS, AND MAINTENANCE AS DIRECTED BY NSPS ACCORDING TO YEAR OF CONSTRUCTION, CAPACITY, AND PRESSURE OF CONTENTS. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: (2) DIESEL TANKS, 3191A - 3191B + Process Type: 42.009

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - (2) DIESEL TANKS, 3191A - 3191B

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS FOR ROOF, SEAL, VENTS, AND MAINTENANCE AS DIRECTED BY NSPS ACCORDING TO YEAR OF CONSTRUCTION, CAPACITY, AND PRESSURE OF CONTENTS. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: CAUSTIC TANK, D8540 + Process Type: 62.020

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - CAUSTIC TANK, D8540

+ Pollutant Name Sodium Hydroxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: SULFURIC ACID TANK, D8600 + Process Type: 62.020Pollutant Information: ATOFINA CHEMICALS INCORPORATED - SULFURIC ACID TANK, D8600

+ Pollutant Name Sulfuric Acid (mist, vapors, etc) Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: FLARE, STEADY STATE OPERATION + Process Type: 19.310

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - FLARE, STEADY STATE OPERATION

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS OF 40 CFR 60.18 Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS OF 40 CFR 60.18 Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS OF 40 CFR 60.18. SEE POLLUTANT NOTES. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFICATIONS OF 40 CFR 60.18Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW REQUIREMENTS OF 40 CFR 60.18 Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE FLARE IS A VOC CONTROL DEVICE Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: FLARE, SSM + Process Type: 19.310

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - FLARE, SSM

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: MEET THE REQUIREMENTS OF 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW THE REQUIREMENTS OF 40 CFR 60.18 Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: FOLLOW REQUIREMENTS OF 40 CFR 60.18 Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) )+ Control Method Code: P + Control Method Description: FOLLOW THE REQUIREMENTS OF 40 CFR 60.18. SEE THE POLLUTANT NOTES. Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW THE REQUIREMENTS OF 40 CFR 60.18 Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE FLARE IS A VOC CONTROL DEVICE Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: FLARE, TOTAL HOURLY AND ANNUAL + Process Type: 19.310

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - FLARE, TOTAL HOURLY AND ANNUAL

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW REQUIREMENTS OF 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW THE REQUIREMENTS OF 40 CFR 60.18 Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: FOLLOW THE REQUIREMENTS OF 40 CFR 60.18.Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FOLLOW THE REQUIREMENTS OF 40 CFR 60.18. SEE POLLUTANT NOTES. Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW THE REQUIREMENTS OF 40 CFR 60.18 Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE FLARE IS A VOC CONTROL DEVICE Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: HEAT TRANSFER FLUID HEATER, H202 + Process Type: 13.310

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - HEAT TRANSFER FLUID HEATER, H202

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2)Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FUEL GAS SHALL BE SWEET NATURAL GAS CONTAINING NO MORE THAN 5 GR S/100 DSCF. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: (2) SULFUR/METHANE HEATERS + Process Type: 19.600

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - (2) SULFUR/METHANE HEATERS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method+ Control Method Description: LOW-NOX TECHNOLOGY Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FUEL GAS SHALL BE SWEET NATURAL GAS CONTAINING NO MORE THAN 5 GR S/100 DSCF. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: HEAT TRANSFER FLUID HEATER, H2202 + Process Type: 13.310

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - HEAT TRANSFER FLUID HEATER, H2202

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FUEL GAS SHALL BE SWEET NATURAL GAS CONTAINING NO MORE THAN 0.5 GR S/100 DSCF. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: INCINERATOR + Process Type: 64.999

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - INCINERATOR

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: SULFUR STORAGE TANK, S-1 + Process Type: 64.004

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - SULFUR STORAGE TANK, S-1

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: SEE POLLUTANT NOTES Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: SULFUR PIT, S-2 + Process Type: 64.999Pollutant Information: ATOFINA CHEMICALS INCORPORATED - SULFUR PIT, S-2

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: SULFUR TRUCK, S-3 + Process Type: 64.005

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - SULFUR TRUCK, S-3

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: SULFOX CHILLER SYSTEM, SULFOX-CHLR + Process Type: 64.003

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - SULFOX CHILLER SYSTEM, SULFOX-CHLR+ Pollutant Name Hydrochlorofluorocarbons (HCFC) Pollutant Group(s): ( Greenhouse Gasses (GHG) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: SULFOX COOLING TOWER, SULFOX-CT + Process Type: 99.009

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - SULFOX COOLING TOWER, SULFOX-CT

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: SEE POLLUTANT NOTES. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: BAGFILTER, SULFOX-INH + Process Type: 64.999

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - BAGFILTER, SULFOX-INH

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGFILTER Cost Effectiveness:Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: THERMAL OXIDIZER, STEADY STATE SERVICE + Process Type: 64.003

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - THERMAL OXIDIZER, STEADY STATE SERVICE

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE INCINERATOR IS A VOC CONTROL Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P+ Control Method Description: FUEL GAS COMBUSTED IN EACH COMBUSTION EMISSION POINT NUMBER SHALL BE SWEET NATURAL GAS CONTAINING NO MORE THAN 5 GR S/100 DSCF. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: THERMAL OXIDIZER, SSM + Process Type: 64.003

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - THERMAL OXIDIZER, SSM

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FUEL GAS SHALL BE SWEET NATURAL GAS CONTAINING NO MORE THAN 5 GR S/100 DSCF. Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE OXIDIZER IS A VOC CONTROL. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: THERMAL OXIDIZER, TOTAL HOURLY AND ANNUAL + Process Type: 64.003

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - THERMAL OXIDIZER, TOTAL HOURLY AND ANNUAL

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: THE FUEL GAS SHALL BE SWEET NATURAL GAS CONTAINING NO MORE THAN 5 GR S/100 DSCF. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE INCINERATOR IS A VOC CONTROL. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10)Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: WASTEWATER TREATMENT PLANT, WWTP + Process Type: 64.006

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - WASTEWATER TREATMENT PLANT, WWTP

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: EMISSIONS FROM ANY VOC WATER SEPARATION EQUIPMENT SHALL BE VENTED TO A PERMITTED CONTROL DEVICE OR RECYCLED TO THE PROCESS. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: (2) STEAM BOILERS, X-426A AND X-426B + Process Type: 13.310

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - (2) STEAM BOILERS, X-426A AND X-426B

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FUEL GAS SHALL BE SWEET NATURAL GAS CONTAINING NO MORE THAN 5 GR S/100 DSCF. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: ACROLEIN PROCESS FUGITIVES, ACRO-FUG + Process Type: 64.002

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - ACROLEIN PROCESS FUGITIVES, ACRO-FUG

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD ENGINEERING PRACTICES AND PROCEDURES OF LEAK DETECTION (28 VHP LDAR), ISOLATION, AND REPAIR.Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: ACROLEIN STORAGE TANKS FUGITIVES, ACRO-TKSFUG + Process Type: 64.004

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - ACROLEIN STORAGE TANKS FUGITIVES, ACRO-TKSFUG

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: ACROLEIN WASTEWATER FUGITIVES, ACRO-WWFUG + Process Type: 64.006

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - ACROLEIN WASTEWATER FUGITIVES, ACRO-WWFUG

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. ALL ACROLEIN WW STORAGE TANKS SHALL VENT TO EPN SULFOX-TO. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: B1/B2 UNITS CHILLER SYSTEM + Process Type: 64.002

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - B1/B2 UNITS CHILLER SYSTEM

+ Pollutant Name Hydrochlorofluorocarbons (HCFC) Pollutant Group(s): ( Greenhouse Gasses (GHG) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N+ Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: TRAIN 1- ETSH OR TBM PRODUCTION FUGITIVES + Process Type: 64.002

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - TRAIN 1- ETSH OR TBM PRODUCTION FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: 28 CNTA Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES OF LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: TRAIN 1 - MESH PRODUCTION FUGITIVES + Process Type: 64.002

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - TRAIN 1 - MESH PRODUCTION FUGITIVES

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: 28CNTA LDARCost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: TRAIN 2- MESH PRODUCTION FUGITIVES + Process Type: 64.002

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - TRAIN 2- MESH PRODUCTION FUGITIVES

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: 28 CNTA Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES OF LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: DIMETHYL DISULFIDE AREA PROCESS FUGITIVES + Process Type: 64.002

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - DIMETHYL DISULFIDE AREA PROCESS FUGITIVES

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: DIMETHYL SULFIDE AREA PROCESS FUGITIVES + Process Type: 64.002

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - DIMETHYL SULFIDE AREA PROCESS FUGITIVES

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES OF LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: H2S PLANT PROCESS FUGITIVES + Process Type: 64.002

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - H2S PLANT PROCESS FUGITIVES

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: 28CNTA LDAR Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: FLARE AREA FUGITIVES + Process Type: 19.310

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - FLARE AREA FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED+ Process Name: INCINERATOR PROCESS FUGITIVES + Process Type: 64.999

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - INCINERATOR PROCESS FUGITIVES

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: 28CNTA LDAR Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28VHP LDAR Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: MMP PROCESS AREA FUGITIVES + Process Type: 64.002

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - MMP PROCESS AREA FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: MMP RAILCAR LOADING AREA PROCESS FUGITIVES + Process Type: 64.005

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - MMP RAILCAR LOADING AREA PROCESS FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) )+ Control Method Code: P + Control Method Description: SEE POLLUTANT NOTES Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: MMP STORAGE AREA PROCESS FUGITIVES + Process Type: 64.004

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - MMP STORAGE AREA PROCESS FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: SEE POLLUTANT NOTES. FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: PRODUCT RECOVERY TOWER FUGITIVES + Process Type: 64.999

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - PRODUCT RECOVERY TOWER FUGITIVES

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: 28CNTA LDAR Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK+ Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: RAILCAR LOADING/UNLOADING FUGITIVES + Process Type: 64.005

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - RAILCAR LOADING/UNLOADING FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: SEE POLLUTANT NOTES. FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: SEE POLLUTANT NOTES. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: RUNDOWN TANK FUGITIVES + Process Type: 64.999

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - RUNDOWN TANK FUGITIVES

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: A + Control Method Description: MMP DAY STORAGE TANKS WILL VENT TO THE MMP BULK STORAGE TANK WHICH WILL VENT TO SULF0X-TO. Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method MMP DAY STORAGE TANKS WILL VENT TO THE MMP BULK+ Control Method Description: MMP DAY STORAGE TANKS WILL VENT TO THE MMP BULK STORAGE TANK WHICH WILL VENT TO SULF0X-TO. FOLLOW PRACTICES OF LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: MMP DAY STORAGE TANKS WILL VENT TO THE MMP BULK STORAGE TANK WHICH WILL VENT TO SULF0X-TO. FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: STORAGE TANKS FUGITIVES + Process Type: 64.004

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - STORAGE TANKS FUGITIVES

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: MMP DAY STORAGE TANKS WILL VENT TO THE MMP BULK STORAGE TANK WHICH WILL VENT TO SULF0X-TO. FOLLOW PRACTICES OF LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: MMP DAY STORAGE TANKS WILL VENT TO THE MMP BULK STORAGE TANK WHICH WILL VENT TO SULF0X-TO. FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: SULFOX CHILLER SYSTEM FUGITIVES + Process Type: 64.999Pollutant Information: ATOFINA CHEMICALS INCORPORATED - SULFOX CHILLER SYSTEM FUGITIVES

+ Pollutant Name Hydrochlorofluorocarbons (HCFC) Pollutant Group(s): ( Greenhouse Gasses (GHG) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: SOUR WATER STRIPPERS FUGITIVES + Process Type: 64.006

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - SOUR WATER STRIPPERS FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. EMISSIONS FROM ANY VOC WATER SEPARATION EQUIPMENT SHALL BE VENTED TO A PERMITTED CONTROL DEVICE OR RECYCLED TO THE PROCESS. Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: 28CNTA LDAR Cost Effectiveness:

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: THERMAL OXIDIZER PROCESS FUGITIVES+ Process Type: 64.003

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - THERMAL OXIDIZER PROCESS FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Process Information: ATOFINA CHEMICALS INCORPORATED

+ Process Name: TANK TRUCK LOADING/UNLOADING FUGITIVES + Process Type: 64.005

Pollutant Information: ATOFINA CHEMICALS INCORPORATED - TANK TRUCK LOADING/UNLOADING FUGITIVES

+ Pollutant Name Sulfur, Total Reduced (TRS) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: SEE POLLUTANT NOTES. FOLLOW PRACTICES OF LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: SEE POLLUTANT NOTES. FOLLOW PRACTICES OF GOOD ENGINEERING, LEAK DETECTION, ISOLATION, AND REPAIR. Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC

RBLC ID: NE-0046 + Corporate/Company Name: AVENTINE RENEWABLE ENERGY - AURORA WEST, LLC + Facility Name: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC Facility County: HAMILTONFacility State: NE Facility ZIP Code: 68818 + SIC Code: 2869 NAICS Code: 325193 Permit Issuance Date: 09/27/2007 ACT

Process Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC

+ Process Name: GRAIN RECEIVING, HANDLING, STORAGE, AND HAMMERMILLING + Process Type: 70.290

Pollutant Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC - GRAIN RECEIVING, HANDLING, STORAGE, AND HAMMERMILLING

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE OR VENT FILTER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE OR VENT FILTER Cost Effectiveness:

Process Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC

+ Process Name: DDGS STORAGE AND LOADOUT + Process Type: 70.007

Pollutant Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC - DDGS STORAGE AND LOADOUT

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

Process Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC

+ Process Name: FERMENTATION OPERATIONS + Process Type: 70.190

Pollutant Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC - FERMENTATION OPERATIONS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CO2 SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CO2 SCRUBBER Cost Effectiveness:

Process Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC

+ Process Name: PRE-FERMENTATION, DISTILLATION, AND DGS DRYING OPERATIONS + Process Type: 70.190

Pollutant Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC - PRE-FERMENTATION, DISTILLATION, AND DGS DRYING OPERATIONS

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: REGENERATIVE THERMAL OXIDIZER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A+ Control Method Description: REGENERATIVE THERMAL OXIDIZER Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS ON RTO Cost Effectiveness:

+ Pollutant Name Sulfur Oxides (SOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: NATURAL GAS AS FUEL IN RTO Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: A + Control Method Description: REGENERATIVE THERMAL OXIDIZER Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: REGENERATIVE THERMAL OXIDIZER Cost Effectiveness:

Process Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC

+ Process Name: ORGANIC LIQUID PROCESS AND STORAGE TANKS + Process Type: 64.004

Pollutant Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC - ORGANIC LIQUID PROCESS AND STORAGE TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: INTERNAL FLOATING ROOF FOR ALL BUT CORROSION INHIBITOR TANK Cost Effectiveness:Process Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC

+ Process Name: ETHANOL LOADOUT + Process Type: 70.230

Pollutant Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC - ETHANOL LOADOUT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: FLARE Cost Effectiveness:

Process Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC

+ Process Name: GAS-FIRED BOILERS + Process Type: 11.310

Pollutant Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC - GAS-FIRED BOILERS

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS WILL BE INSTALLED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:Process Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC

+ Process Name: COOLING TOWER + Process Type: 11.310

Pollutant Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC - COOLING TOWER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: MIST ELIMINATOR Cost Effectiveness:

Process Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC

+ Process Name: HAUL ROADS + Process Type: 90.004

Pollutant Information: AVENTINE RENEWABLE ENERGY - AURORA WEST LLC - HAUL ROADS

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: AVOCA, INC.

RBLC ID: NC-0111 + Corporate/Company Name: AVOCA, INC. + Facility Name: AVOCA, INC. Facility County: BERTIE Facility State: NC Facility ZIP Code: 27957 + SIC Code: 2087NAICS Code: 311930 Permit Issuance Date: 07/29/2004 ACT

Process Information: AVOCA, INC.

+ Process Name: ROTOCEL OPERATION PROCESS VENTS + Process Type: 64.003

Pollutant Information: AVOCA, INC. - ROTOCEL OPERATION PROCESS VENTS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CHILLED WATER-COOLED CONDENSER AND PACKED TOWER SCRUBBER Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: ROTOCEL OPERATION SOLVENT RECYCLE TANKS + Process Type: 64.004

Pollutant Information: AVOCA, INC. - ROTOCEL OPERATION SOLVENT RECYCLE TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CHILLED WATER-COOLED CONDENSER AND PACKED TOWER SCRUBBER Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: ROTOCEL OPERATION SOLVENT RECYCLE TANKS + Process Type: 64.004

Pollutant Information: AVOCA, INC. - ROTOCEL OPERATION SOLVENT RECYCLE TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CHILLED WATER-COOLED CONDENSER Cost Effectiveness:Process Information: AVOCA, INC.

+ Process Name: ROTOCEL OPERATION EQUIPMENT LEAKS + Process Type: 64.002

Pollutant Information: AVOCA, INC. - ROTOCEL OPERATION EQUIPMENT LEAKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LEAK DETECTION AND REPAIR (LDAR) Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: ROTOCEL OPERATION WASTEWATER TANKS AND OTHER SIMILAR VESSELS + Process Type: 64.006

Pollutant Information: AVOCA, INC. - ROTOCEL OPERATION WASTEWATER TANKS AND OTHER SIMILAR VESSELS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: FIXED ROOFS Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: RECOVERY OPERATION ARCON TANK PROCESS VENT + Process Type: 64.003

Pollutant Information: AVOCA, INC. - RECOVERY OPERATION ARCON TANK PROCESS VENT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CHILLED WATER-COOLED CONDENSER AND PACKED TOWER SCRUBBER Cost Effectiveness:Process Information: AVOCA, INC.

+ Process Name: RECOVERY OPERATION ARCON TANK PROCESS VENT + Process Type: 64.003

Pollutant Information: AVOCA, INC. - RECOVERY OPERATION ARCON TANK PROCESS VENT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CHILLED WATER-COOLED CONDENSER Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: RECOVERY OPERATION STRIPPER / STRIPPER RECEIVER PROCESS VENT + Process Type: 64.003

Pollutant Information: AVOCA, INC. - RECOVERY OPERATION STRIPPER / STRIPPER RECEIVER PROCESS VENT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CHILLED WATER-COOLED CONDENSER AND PACKED TOWER SCRUBBER Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: RECOVERY OPERATION STRIPPER / STRIPPER RECEIVER PROCESS VENT + Process Type: 64.003

Pollutant Information: AVOCA, INC. - RECOVERY OPERATION STRIPPER / STRIPPER RECEIVER PROCESS VENT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description:Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: RECOVERY OPERATION PROCESS/STORAGE TANKS + Process Type: 64.004

Pollutant Information: AVOCA, INC. - RECOVERY OPERATION PROCESS/STORAGE TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: FIXED ROOFS Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: RECOVERY OPERATION EQUIPMENT LEAKS + Process Type: 64.002

Pollutant Information: AVOCA, INC. - RECOVERY OPERATION EQUIPMENT LEAKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LEAK DETECTION AND REPAIR (LDAR) Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: RECOVERY OPERATION WASTEWATER TANKS AND OTHER SIMILAR VESSELS + Process Type: 64.006

Pollutant Information: AVOCA, INC. - RECOVERY OPERATION WASTEWATER TANKS AND OTHER SIMILAR VESSELS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: FIXED ROOFS AND BIOLOGICAL TREATMENTCost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: BOTANICAL EXTRACTION PROCESS VENTS + Process Type: 64.003

Pollutant Information: AVOCA, INC. - BOTANICAL EXTRACTION PROCESS VENTS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CHILLED WATER-COOLED CONDENSER AND LIQUID NITROGEN-COOLED CONDENSER Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: BOTANICAL EXTRACTION EQUIPMENT LEAKS + Process Type: 64.002

Pollutant Information: AVOCA, INC. - BOTANICAL EXTRACTION EQUIPMENT LEAKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LEAK DETECTION AND REPAIR (LDAR) Cost Effectiveness:

Process Information: AVOCA, INC.

+ Process Name: BOTANICAL EXTRACTION WASTEWATER TANKS AND OTHER SIMILAR VESSELS + Process Type: 64.006

Pollutant Information: AVOCA, INC. - BOTANICAL EXTRACTION WASTEWATER TANKS AND OTHER SIMILAR VESSELS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: FIXED ROOFS Cost Effectiveness:Process Information: AVOCA, INC.

+ Process Name: THREE NO. 2 FUEL-OIL FIRED BOILERS + Process Type: 13.200

Pollutant Information: AVOCA, INC. - THREE NO. 2 FUEL-OIL FIRED BOILERS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: COMBUSTION CONTROL Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: BASF CORPORATION

RBLC ID: MI-0304 + Corporate/Company Name: BASF CORPORATION + Facility Name: BASF CORPORATION Facility County: WAYNE Facility State: MI Facility ZIP Code: 48150 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 10/23/2001 ACT

Process Information: BASF CORPORATION

+ Process Name: REACTORS, ISOCYANATES + Process Type: 64.001

Pollutant Information: BASF CORPORATION - REACTORS, ISOCYANATES

+ Pollutant Name Methylene diphenyl diisocyanate Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method CONTROL BY COMMON CARBON CANISTER. SEE POLLUTANT+ Control Method Description: CONTROL BY COMMON CARBON CANISTER. SEE POLLUTANT NOTES. Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: BULK LOADING, TDI & MDI + Process Type: 63.999

Pollutant Information: BASF CORPORATION - BULK LOADING, TDI & MDI

+ Pollutant Name Methylene diphenyl diisocyanate Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CARBON CANISTER, WITH MONITORING Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: DRUMMING + Process Type: 63.999

Pollutant Information: BASF CORPORATION - DRUMMING

+ Pollutant Name Methylene diphenyl diisocyanate Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: THROUGHPUT LIMIT 50000 T/YR, MDI. Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: TANKS + Process Type: 64.004

Pollutant Information: BASF CORPORATION - TANKS

+ Pollutant Name Methylene diphenyl diisocyanate Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: A+ Control Method Description: CARBON CANISTER WITH MONITORING Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: BLENDING TANKS, RESIN + Process Type: 64.005

Pollutant Information: BASF CORPORATION - BLENDING TANKS, RESIN

+ Pollutant Name Hydrochlorofluorocarbons (HCFC) Pollutant Group(s): ( Greenhouse Gasses (GHG) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: P + Control Method Description: 4000 T/YR THROUGHPUT LIMIT. ALSO 1000 T/YR LIMIT ON HCFC-22. Cost Effectiveness:

+ Pollutant Name Triethylamine Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 3179 LB/MONTH THROUGHPUT LIMIT Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: BASF CORPORATION

RBLC ID: TX-0277 + Corporate/Company Name: BASF CORPORATION + Facility Name: BASF CORPORATION Facility County: BRAZORIA Facility State: TX Facility ZIP Code: 77541 + SIC Code: 2869 NAICS Code: 325110 Permit Issuance Date: 12/12/2001 ACTProcess Information: BASF CORPORATION

+ Process Name: ACRYLIC ACID INCINERATOR (POINT NO. IN-701) + Process Type: 64.999

Pollutant Information: BASF CORPORATION - ACRYLIC ACID INCINERATOR (POINT NO. IN-701)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: THE INCINERATOR IS DESIGNED TO COMBUST VOC WITH A 99.99 PERCENT DRE. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: EQUIPPED WITH LOW NOX BURNER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: THE INCINERATOR IS DESIGNED TO COMBUST NONHAZARDOUS VOC WITH A 99.99 PERCENT DRE. PM10 EMISSIONS ARE NO MORE THAN 0.02 GR/DSCF ON AN ANNUAL BASIS. Cost Effectiveness:

+ Pollutant Name Sulfur Trioxide Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: NATURAL GAS AS SUPPLEMENTAL FUEL CAN CONTAIN NO MORE THAN 0.5 GR/100 DSCF HYDROGEN SULFIDE AND NO MORE THAN 20 GR/100 DSCF SULFER. Cost Effectiveness:+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: NATURAL GAS AS SUPPLEMENTAL FUEL CAN CONTAIN NO MORE THAN 0.5 GR/100 DSCF HYDROGEN SULFIDE AND NO MORE THAN 20 GR/100 DSCF OF SULFER. Cost Effectiveness:

+ Pollutant Name Acrylic Acid Pollutant Group(s): ( Acid Gasses/Mist , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: THE INCINERATOR IS DESIGNED TO COMBUST NONHAZARDOUS VOC WITH A 99.99 PERCENT DRE. Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: INCINERATOR (POINT NO. IN-5500) + Process Type: 64.999

Pollutant Information: BASF CORPORATION - INCINERATOR (POINT NO. IN-5500)

+ Pollutant Name Sulfur Oxides (SOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: NATURAL GAS AS SUPPLEMENTAL FUEL CAN CONTAIN NO MORE THAN 0.5 GR/100 DSCF HYDROGEN SULFIDE AND NO MORE THAN 20 GR/100 DSCF SULFER. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: THE INCINERATOR IS DESGINED TO COMBUST NONHAZARDOUS VOC WITH A 99.9 PERCENT DRE. Cost Effectiveness:

+ Pollutant Name Acrylic Acid Pollutant Group(s): ( Acid Gasses/Mist , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: EQUIPPED WITH A LOW NOX BURNER, THAT LIMITS NOX TO 0.1 LB/MMBTU ON AN ANNUAL BASIS. DESIGNED TO COMBUST NATURAL GAS, ACRYLIC ACID RESIDUE STREAM AND ACID WATER WHILE MINIMIZING NOX FORMATION. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: THE INCINERATOR IS DESIGNED TO COMBUST NONHAZARDOUS VOC WITH A 99.9 PERCENT DRE. PM10 EMISSIONS ARE NO MORE THAN 0.02 GR/DSCF ON AN ANNUAL BASIS. Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: CONTINUOUS FLARE (POINT NO. 4-2-4) + Process Type: 19.310

Pollutant Information: BASF CORPORATION - CONTINUOUS FLARE (POINT NO. 4-2-4)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Acrylic Acid Pollutant Group(s): ( Acid Gasses/Mist , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: STABILIZER SILO (POINT NO. 4-1-2) + Process Type: 64.999

Pollutant Information: BASF CORPORATION - STABILIZER SILO (POINT NO. 4-1-2)

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: (SEE POLLUTANT NOTES)- BAGHOUSE CAPABLE OF ACHIEVING 99.9 PERCENT CONTROL OF PM10. Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: STABILIZER SILO (POINT NO. 4-2-2)+ Process Type: 64.999

Pollutant Information: BASF CORPORATION - STABILIZER SILO (POINT NO. 4-2-2)

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: (SEE POLLUTANT NOTES)- BAGHOUSE IS CAPABLE OF ACHIEVING A 99.9 PERCENT CONTROL OF PM10. Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: COOLING TOWER (POINT NO. 4-2-6) + Process Type: 99.009

Pollutant Information: BASF CORPORATION - COOLING TOWER (POINT NO. 4-2-6)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: BARGE LOADING (POINT NO. 4-2-7) + Process Type: 64.005

Pollutant Information: BASF CORPORATION - BARGE LOADING (POINT NO. 4-2-7)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Acrylic Acid Pollutant Group(s): ( Acid Gasses/Mist , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description:Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: AAE-2 EQUIPMENT FUGITIVES + Process Type: 64.002

Pollutant Information: BASF CORPORATION - AAE-2 EQUIPMENT FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Acrylic Acid Pollutant Group(s): ( Acid Gasses/Mist , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: BASF CORPORATION

+ Process Name: AAE-3 EQUIPMENT FUGITIVES (POINT NO. 4-2-3) + Process Type: 64.002

Pollutant Information: BASF CORPORATION - AAE-3 EQUIPMENT FUGITIVES (POINT NO. 4-2-3)

+ Pollutant Name Acrylic Acid Pollutant Group(s): ( Acid Gasses/Mist , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:Previous Page

NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: BAYPORT ENERGY CENTER

RBLC ID: TX-0453 + Corporate/Company Name: BAYPORT ENERGY CENTER LP + Facility Name: BAYPORT ENERGY CENTER Facility County: HARRIS Facility State: TX Facility ZIP Code: + SIC Code: 4939 NAICS Code: 221122 Permit Issuance Date: 10/20/2003 ACT

Process Information: BAYPORT ENERGY CENTER

+ Process Name: COMBUSTION TURBINE WITH 225 MMBTU/H DUCT BURNERS (2) + Process Type: 15.250

Pollutant Information: BAYPORT ENERGY CENTER - COMBUSTION TURBINE WITH 225 MMBTU/H DUCT BURNERS (2)

+ Pollutant Name Sulfuric Acid (mist, vapors, etc) Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: THE FUEL GAS WILL CONTAIN LESS THAN 0.5 GRAIN SULFUR PER 100 DRY STANDARD CUBIC FEET (ON AN ANNUAL BASIS). Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: THE GAS TURBINES WILL BE EQUIPPED WITH DRY LOW NOX COMBUSTORS, AND THE DUCT BURNERS WILL CONTAIN LOW NOX BURNERS. NOX EMISSIONS WILL BE LIMITED AT THE STACK TO 3.5 PPMVD ON A THREE-HOUR BASIS AND 1.9 PPMVD ON AN ANNUAL BASIS Cost Effectiveness:

+ Pollutant Name Carbon MonoxidePollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: BACT WILL CONSIST OF PROPER COMBUSTION TECHNIQUES. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: BACT WILL CONSIST OF PROPER COMBUSTION TECHNIQUES. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: BACT WILL CONSIST OF PROPER COMBUSTION TECHNIQUES. Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: THE FUEL GAS WILL CONTAIN LESS THAN 0.5 GRAIN SULFUR PER 100 DRY STANDARD CUBIC FEET (ON AN ANNUAL BASIS). Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: AMMONIA SLIP FROM THE SCR UNIT WILL BE LIMITED TO 7 PPMVD. Cost Effectiveness:

Process Information: BAYPORT ENERGY CENTER

+ Process Name: LUBE OIL VENT (2) + Process Type: 64.003

Pollutant Information: BAYPORT ENERGY CENTER - LUBE OIL VENT (2)

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:Process Information: BAYPORT ENERGY CENTER

+ Process Name: FUGITIVES + Process Type: 64.002

Pollutant Information: BAYPORT ENERGY CENTER - FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: BP TEXAS CITY CHEMICAL PLANT B

RBLC ID: TX-0422 + Corporate/Company Name: BP AMOCO CHEMICAL CO. + Facility Name: BP TEXAS CITY CHEMICAL PLANT B Facility County: GALVESTON Facility State: TX Facility ZIP Code: 77590 + SIC Code: 2869 NAICS Code: 325192 Permit Issuance Date: 12/05/2002 ACT

Process Information: BP TEXAS CITY CHEMICAL PLANT B

+ Process Name: FUGITIVES + Process Type: 64.002Pollutant Information: BP TEXAS CITY CHEMICAL PLANT B - FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LEAK INSPECTION AND MONITORING, REPAIR AND MAINTENANCE Cost Effectiveness:

Process Information: BP TEXAS CITY CHEMICAL PLANT B

+ Process Name: TANKS, INTERNAL FLOATING ROOF & FIXED ROOF + Process Type: 64.005

Pollutant Information: BP TEXAS CITY CHEMICAL PLANT B - TANKS, INTERNAL FLOATING ROOF & FIXED ROOF

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: INTERNAL FLOATING ROOF INSTALLED IN ALL TANKS, CLOSURE DEVICES, TANK EXTERIORS PAINTED WHITE OR ALUMINUM, OPERATION WITHOUT VISIBLE LEAKS AND SPILLS. Cost Effectiveness:

Process Information: BP TEXAS CITY CHEMICAL PLANT B

+ Process Name: HEATER, STARTUP, MALEIC ANHYDRIDE REACTOR + Process Type: 19.600

Pollutant Information: BP TEXAS CITY CHEMICAL PLANT B - HEATER, STARTUP, MALEIC ANHYDRIDE REACTOR

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B+ Control Method Description: LOW NOX BURNERS AND SCR Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: PIPELINE QUALITY NATURAL GAS < 2.0 GR S PER 1000 DSCF Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: HEATER BURNS OFF GAS AS CONTROL Cost Effectiveness:

Process Information: BP TEXAS CITY CHEMICAL PLANT B

+ Process Name: FLARE, BDO UNIT + Process Type: 19.310

Pollutant Information: BP TEXAS CITY CHEMICAL PLANT B - FLARE, BDO UNIT

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: BP TEXAS CITY CHEMICAL PLANT B

+ Process Name: MATERIAL LOADING, THF, TRUCK AND RAIL + Process Type: 64.005

Pollutant Information: BP TEXAS CITY CHEMICAL PLANT B - MATERIAL LOADING, THF, TRUCK AND RAIL

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: SCRUBBER, 95% COLLECTION EFFICIENCY Cost Effectiveness:

Process Information: BP TEXAS CITY CHEMICAL PLANT B

+ Process Name: BOILER, SCRUBBER OFF-GAS + Process Type: 13.390

Pollutant Information: BP TEXAS CITY CHEMICAL PLANT B - BOILER, SCRUBBER OFF-GAS

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: LOW NOX BURNERS AND SCR Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: BOILER CONTROLS SCRUBBER OFF-GAS, 99.9% DESTRUCTION. Cost Effectiveness:

+ Pollutant Name Sulfur Oxides (SOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: CARGILL, INC.

RBLC ID: NE-0037 + Corporate/Company Name: CARGILL, INC. + Facility Name: CARGILL, INC. Facility County: WASHINGTON COUNTY Facility State: NE Facility ZIP Code: 680080300 + SIC Code: 2046 NAICS Code: Permit Issuance Date: 09/08/2006 ACT

Process Information: CARGILL, INC.

+ Process Name: CIRCULATING FLUIDIZED BED BOILER + Process Type: 12.110

Pollutant Information: CARGILL, INC. - CIRCULATING FLUIDIZED BED BOILER

+ Pollutant Name Particulate Matter (PM), Organic Condensables Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: COMBUSTION CONTROLS Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: LIMESTONE INJECTION & FABRIC FILTER Cost Effectiveness:

+ Pollutant Name Hydrogen Fluoride Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: LIMESTONE INJECTION & FABRIC FILTER Cost Effectiveness:

+ Pollutant Name Mercury Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Heavy Metals , InOrganic Compounds ) + Control Method Code: P + Control Method Description: SORBENT INJECTION Cost Effectiveness:

+ Pollutant Name Hydrochloric Acid Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) , InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LIME INJECTION Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: LIMESTONE INJECTION Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method+ Control Method Description: COMBUSTION CONTROL PLUS SNCR Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: COMBUSTION CONTROLS Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FABRIC FILTER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable (FPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: FABRIC FILTER Cost Effectiveness:

Process Information: CARGILL, INC.

+ Process Name: STEEPHOUSE + Process Type: 64.003

Pollutant Information: CARGILL, INC. - STEEPHOUSE

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2)Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THERMAL OXIDIZER Cost Effectiveness:

Process Information: CARGILL, INC.

+ Process Name: MILLHOUSE AND FEEDHOUSE + Process Type: 70.310

Pollutant Information: CARGILL, INC. - MILLHOUSE AND FEEDHOUSE

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Hazardous Air Pollutants (HAP) Pollutant Group(s): ( Hazardous Air Pollutants (HAP) ) + Control Method Code: A + Control Method Description: Cost Effectiveness:

Process Information: CARGILL, INC.

+ Process Name: GLUTEN FLASH DRYER + Process Type: 70.210Pollutant Information: CARGILL, INC. - GLUTEN FLASH DRYER

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: COMBUSTION CONTROLS Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: COMBUSTION CONTROL Cost Effectiveness:

+ Pollutant Name Hazardous Air Pollutants (HAP) Pollutant Group(s): ( Hazardous Air Pollutants (HAP) ) + Control Method Code: A + Control Method Description: Cost Effectiveness:

Process Information: CARGILL, INC.+ Process Name: GERM STEAM TUBE DRYERS + Process Type: 70.210

Pollutant Information: CARGILL, INC. - GERM STEAM TUBE DRYERS

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WASTE GAS EVAPORATOR Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: A + Control Method Description: WASTE GAS EVAPORATOR Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THERMAL OXIDIZER Cost Effectiveness:

Process Information: CARGILL, INC.

+ Process Name: FIBER STEAM TUBE DRYER + Process Type: 70.210

Pollutant Information: CARGILL, INC. - FIBER STEAM TUBE DRYER

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WASTE GAS EVAPORATOR Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: A + Control Method Description: WASTE GAS EVAPORATOR Cost Effectiveness:+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THERMAL OXIDIZER Cost Effectiveness:

Process Information: CARGILL, INC.

+ Process Name: FERMENTATION + Process Type: 64.003

Pollutant Information: CARGILL, INC. - FERMENTATION

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Hazardous Air Pollutants (HAP) Pollutant Group(s): ( Hazardous Air Pollutants (HAP) ) + Control Method Code: A + Control Method Description: Cost Effectiveness:

Process Information: CARGILL, INC.

+ Process Name: DISTILLATION COLUMN + Process Type: 64.003

Pollutant Information: CARGILL, INC. - DISTILLATION COLUMN

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Hazardous Air Pollutants (HAP) Pollutant Group(s): ( Hazardous Air Pollutants (HAP) ) + Control Method Code: A+ Control Method Description: Cost Effectiveness:

Process Information: CARGILL, INC.

+ Process Name: STILLAGE EVAPORATOR + Process Type: 64.003

Pollutant Information: CARGILL, INC. - STILLAGE EVAPORATOR

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Hazardous Air Pollutants (HAP) Pollutant Group(s): ( Hazardous Air Pollutants (HAP) ) + Control Method Code: A + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: CHAMBERS PLANT

RBLC ID: TX-0338 + Corporate/Company Name: DOME PETROCHEMICAL LC + Facility Name: CHAMBERS PLANT Facility County: CHAMBERS Facility State: TX Facility ZIP Code: 77027 + SIC Code: 2869 NAICS Code: 325110 Permit Issuance Date: 05/23/2001 ACT

Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 401, 8401+ Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 401, 8401

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 429, 8429 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 429, 8429

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: (3) STORAGE TANKS 430-432, 8430-8432 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - (3) STORAGE TANKS 430-432, 8430-8432

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: (2) STORAGE TANKS 433&434, 8433&8434 + Process Type: 42.009Pollutant Information: CHAMBERS PLANT - (2) STORAGE TANKS 433&434, 8433&8434

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: (2) STORAGE TANKS 435&436, 8435&8436 + Process Type: 64.004

Pollutant Information: CHAMBERS PLANT - (2) STORAGE TANKS 435&436, 8435&8436

+ Pollutant Name Methyl Tertiary Butyl Ether Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 443, 8443 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 443, 8443

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 448, 8448 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 448, 8448+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 449, 8449 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 449, 8449

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 450, 8450 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 450, 8450

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 454, 8454 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 454, 8454

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N+ Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: (2) STORAGE TANKS 455& 456, 8455&8456 + Process Type: 64.004

Pollutant Information: CHAMBERS PLANT - (2) STORAGE TANKS 455& 456, 8455&8456

+ Pollutant Name Methyl Tertiary Butyl Ether Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 457, 8457 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 457, 8457

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 458, 8458 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 458, 8458

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 459, 8459 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 459, 8459

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: (3) STORAGE TANKS 460&461, 465; 8460&8461, 8465 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - (3) STORAGE TANKS 460&461, 465; 8460&8461, 8465

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: (3) STORAGE TANKS 464, 466&467, 8464, 8466&8467 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - (3) STORAGE TANKS 464, 466&467, 8464, 8466&8467

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:Process Information: CHAMBERS PLANT

+ Process Name: (2) STORAGE TANKS 478&479, 8478&8479 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - (2) STORAGE TANKS 478&479, 8478&8479

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: STORAGE TANK 480, 8480 + Process Type: 42.009

Pollutant Information: CHAMBERS PLANT - STORAGE TANK 480, 8480

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: FUGITIVES, 8601-8625 + Process Type: 64.002

Pollutant Information: CHAMBERS PLANT - FUGITIVES, 8601-8625

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LEAK DETECTION AND REPAIR PROGRAM. Cost Effectiveness:

Process Information: CHAMBERS PLANT+ Process Name: (3) LEF PROCESS HEATERS, 8701-8703 + Process Type: 19.600

Pollutant Information: CHAMBERS PLANT - (3) LEF PROCESS HEATERS, 8701-8703

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: NS PROCESS HEATER, 8705 + Process Type: 19.600Pollutant Information: CHAMBERS PLANT - NS PROCESS HEATER, 8705

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: HF PROCESS HEATER, 8706 + Process Type: 19.600

Pollutant Information: CHAMBERS PLANT - HF PROCESS HEATER, 8706

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: (3) HEU PROCESS HEATERS, 8707-8709 + Process Type: 19.600

Pollutant Information: CHAMBERS PLANT - (3) HEU PROCESS HEATERS, 8707-8709

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: (2) BOILERS 1 & 2, 8729 & 8730 + Process Type: 19.600

Pollutant Information: CHAMBERS PLANT - (2) BOILERS 1 & 2, 8729 & 8730

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: WATER STRIPPER HEATER, 8731 + Process Type: 19.600

Pollutant Information: CHAMBERS PLANT - WATER STRIPPER HEATER, 8731

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: C/CF PROCESS HEATER, 8733 + Process Type: 19.600

Pollutant Information: CHAMBERS PLANT - C/CF PROCESS HEATER, 8733

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHAMBERS PLANT

+ Process Name: VAPOR COMBUSTION UNIT, 8734 + Process Type: 64.999

Pollutant Information: CHAMBERS PLANT - VAPOR COMBUSTION UNIT, 8734

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: THE VAPOR COMBUSTION UNIT IS A VOC CONTROL DEVICE Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:Process Information: CHAMBERS PLANT

+ Process Name: BOILER 3, 8736 + Process Type: 19.600

Pollutant Information: CHAMBERS PLANT - BOILER 3, 8736

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID.NOTE: Draft determinations are marked with a " * " beside the RBLC ID.

Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: CHOCOLATE BAYOU PLANT

RBLC ID: TX-0347 + Corporate/Company Name: BP AMOCO CHEMICAL COMPANY + Facility Name: CHOCOLATE BAYOU PLANT Facility County: BRAZORIA Facility State: TX Facility ZIP Code: 775121488 + SIC Code: 2869 NAICS Code: 325110 Permit Issuance Date: 10/16/2001 ACT

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: NO.1 OLEFINS COOLING TOWER, AT-1210 + Process Type: 99.009

Pollutant Information: CHOCOLATE BAYOU PLANT - NO.1 OLEFINS COOLING TOWER, AT-1210

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: WEEKLY VOC AND BX MONITORING OF THE CIRCULATION WATER. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: NO. 2 OLEFINS COOLING TOWER, DAT-3201 + Process Type: 99.009Pollutant Information: CHOCOLATE BAYOU PLANT - NO. 2 OLEFINS COOLING TOWER, DAT-3201

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: WEEKLY MONITORING OF VOC AND BZ IN THE CIRCULATION WATER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: NO. 1 OLEFINS UNIT FUGITIVES, FUG-V10F + Process Type: 64.002

Pollutant Information: CHOCOLATE BAYOU PLANT - NO. 1 OLEFINS UNIT FUGITIVES, FUG-V10F

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28VHP LEAK DETECTION AND REPAIR PROGRAM Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: NO. 2 OLEFINS UNIT FUGITIVES, FUG-V20F + Process Type: 64.002

Pollutant Information: CHOCOLATE BAYOU PLANT - NO. 2 OLEFINS UNIT FUGITIVES, FUG-V20F

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28VHP LDAR PROGRAMCost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: NO. 1&2 OLEFINS ANALYZER VENT FUGITIVES + Process Type: 64.002

Pollutant Information: CHOCOLATE BAYOU PLANT - NO. 1&2 OLEFINS ANALYZER VENT FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28VHP LDAR PROGRAM Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: SECOND STAGE HYDROTREATER FUGITIVES, FUGVSSH + Process Type: 64.002

Pollutant Information: CHOCOLATE BAYOU PLANT - SECOND STAGE HYDROTREATER FUGITIVES, FUGVSSH

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28VHP LDAR PROGRAM Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: TANK FARM FUGITIVES, FUG-FTF + Process Type: 64.002

Pollutant Information: CHOCOLATE BAYOU PLANT - TANK FARM FUGITIVES, FUG-FTF

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28VHP LDAR PROGRAM Cost Effectiveness:Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: MARINE DOCK FUGITIVES, FUG-VBD + Process Type: 64.002

Pollutant Information: CHOCOLATE BAYOU PLANT - MARINE DOCK FUGITIVES, FUG-VBD

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28VHP LDAR PROGRAM Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: METERING STATION FUGITIVES, FUG-VCM + Process Type: 64.002

Pollutant Information: CHOCOLATE BAYOU PLANT - METERING STATION FUGITIVES, FUG-VCM

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28 VHP LDAR PROGRAM Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: RAIL LOADING FUGITIVES, FUG-RAIL + Process Type: 64.005

Pollutant Information: CHOCOLATE BAYOU PLANT - RAIL LOADING FUGITIVES, FUG-RAIL

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28 VHP LDAR PROGRAM Cost Effectiveness:Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: NO. 1 OLEFINS TRUCK LOADING, FUELTRK1 + Process Type: 64.005

Pollutant Information: CHOCOLATE BAYOU PLANT - NO. 1 OLEFINS TRUCK LOADING, FUELTRK1

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: NO. 2 OLEFINS TRUCK LOADING, FUELTRK2 + Process Type: 64.005

Pollutant Information: CHOCOLATE BAYOU PLANT - NO. 2 OLEFINS TRUCK LOADING, FUELTRK2

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: BLEACH TANK, AF-1215 + Process Type: 64.999

Pollutant Information: CHOCOLATE BAYOU PLANT - BLEACH TANK, AF-1215

+ Pollutant Name Sodium Hypochlorite Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: BLEACH TANK, AF-3215 + Process Type: 64.999

Pollutant Information: CHOCOLATE BAYOU PLANT - BLEACH TANK, AF-3215

+ Pollutant Name Chlorine / Chlorine Compounds Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: SLOP TANK, AF-3701 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - SLOP TANK, AF-3701

+ Pollutant Name Acetonitrile Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: (2) ACETONITRILE TANKS, AF-1103&-1104 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - (2) ACETONITRILE TANKS, AF-1103&-1104

+ Pollutant Name Acetonitrile Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: RERUNS BOTTOMS TANK, AF-1105 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - RERUNS BOTTOMS TANK, AF-1105

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Benzene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Toluene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: RERUNS BOTTOMS TANK, AF-1106 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - RERUNS BOTTOMS TANK, AF-1106

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Benzene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Toluene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: FUEL OIL TANK, AF-1905 + Process Type: 42.009

Pollutant Information: CHOCOLATE BAYOU PLANT - FUEL OIL TANK, AF-1905

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: ACETONITRILE TANK, AF-3103 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - ACETONITRILE TANK, AF-3103

+ Pollutant Name Acetonitrile Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: FUEL OIL TANK, AF-3905 + Process Type: 42.009

Pollutant Information: CHOCOLATE BAYOU PLANT - FUEL OIL TANK, AF-3905

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: FUEL OIL TANK, DDF-1001 + Process Type: 42.009

Pollutant Information: CHOCOLATE BAYOU PLANT - FUEL OIL TANK, DDF-1001

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: METHANOL TANK, DDF-1301 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - METHANOL TANK, DDF-1301

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: METHANOL TANK, DDF-202 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - METHANOL TANK, DDF-202

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: SODIUM NITRITE SOLUTION TANK, DDF-701 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - SODIUM NITRITE SOLUTION TANK, DDF-701

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: SODIUM NITRITE SOLUTION TANK, DDF-705 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - SODIUM NITRITE SOLUTION TANK, DDF-705

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: FUEL OIL TANK, DF-1001 + Process Type: 42.009

Pollutant Information: CHOCOLATE BAYOU PLANT - FUEL OIL TANK, DF-1001

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: ALCOHOL TANK, DF-1301 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - ALCOHOL TANK, DF-1301

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: LUBE OIL STORAGE, DF-502 + Process Type: 42.009

Pollutant Information: CHOCOLATE BAYOU PLANT - LUBE OIL STORAGE, DF-502

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT+ Process Name: SODIUM NITRITE SOLUTION TANK, DF-701 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - SODIUM NITRITE SOLUTION TANK, DF-701

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: SODIUM NITRITE SOLUTION TANK, DF-702 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - SODIUM NITRITE SOLUTION TANK, DF-702

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Acetonitrile Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: SODIUM NITRITE SOLUTION TANK, DF-705 + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - SODIUM NITRITE SOLUTION TANK, DF-705

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Acetonitrile Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: LUBE OIL STORAGE + Process Type: 42.009

Pollutant Information: CHOCOLATE BAYOU PLANT - LUBE OIL STORAGE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: DECOKE STACK, DF-101 + Process Type: 64.003

Pollutant Information: CHOCOLATE BAYOU PLANT - DECOKE STACK, DF-101

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE SEPARATOR Cost Effectiveness:+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: DECOKE STACK, DF-104 + Process Type: 64.003

Pollutant Information: CHOCOLATE BAYOU PLANT - DECOKE STACK, DF-104

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE SEPARATOR Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: DECOKE STACK, DDF-101 + Process Type: 64.003

Pollutant Information: CHOCOLATE BAYOU PLANT - DECOKE STACK, DDF-101

+ Pollutant Name Carbon Dioxide Pollutant Group(s): ( Acid Gasses/Mist , Greenhouse Gasses (GHG) , InOrganic Compounds )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE SEPARATOR Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: DECOKE STACK, DDF-104 + Process Type: 64.003

Pollutant Information: CHOCOLATE BAYOU PLANT - DECOKE STACK, DDF-104

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE SEPARATOR Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: (2) DECOKE STACKS, DF-105 & DDF-105 + Process Type: 64.003

Pollutant Information: CHOCOLATE BAYOU PLANT - (2) DECOKE STACKS, DF-105 & DDF-105

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE SEPARATORCost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: DOCK FLARE, AM-1500 + Process Type: 19.310

Pollutant Information: CHOCOLATE BAYOU PLANT - DOCK FLARE, AM-1500

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name 1, 3-Butadiene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE FLARE IS A CONTROL DEVICE FOR BUTADIENE Cost Effectiveness:

+ Pollutant Name Propylene Pollutant Group(s): ( Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: A + Control Method Description: THE FLARE IS A CONTROL FOR PROPYLENE Cost Effectiveness:

+ Pollutant Name Carbon MonoxidePollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: (2) HYDROTREATER REGENERATOR STACKS,DD-606&DDD-606 + Process Type: 64.003

Pollutant Information: CHOCOLATE BAYOU PLANT - (2) HYDROTREATER REGENERATOR STACKS,DD-606&DDD-606

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: NO. 1 OLEFINS FLARE, DM-1101 + Process Type: 19.310

Pollutant Information: CHOCOLATE BAYOU PLANT - NO. 1 OLEFINS FLARE, DM-1101

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: THE FLARE IS A VOC CONTROL Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: NO. 2 OLEFINS FLARE, DDM-3101 + Process Type: 19.310

Pollutant Information: CHOCOLATE BAYOU PLANT - NO. 2 OLEFINS FLARE, DDM-3101

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: THE FLARE IS A VOC CONTROL Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: LIME SILO FILTER VENT, DDZ-902 + Process Type: 64.003

Pollutant Information: CHOCOLATE BAYOU PLANT - LIME SILO FILTER VENT, DDZ-902

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: THE FILTER CONTROLS PM10 EMISSIONS Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: LIME SILO FILTER VENT + Process Type: 64.003

Pollutant Information: CHOCOLATE BAYOU PLANT - LIME SILO FILTER VENT

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: THE FILTER CONTROLS PM10 EMISSIONS Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: SEAL OIL VENTS, OF1SOVENT + Process Type: 64.002

Pollutant Information: CHOCOLATE BAYOU PLANT - SEAL OIL VENTS, OF1SOVENT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N+ Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: RAILROAD LOADING FUGITIVES, RAILLOAD + Process Type: 64.005

Pollutant Information: CHOCOLATE BAYOU PLANT - RAILROAD LOADING FUGITIVES, RAILLOAD

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: REGENERATION FURNACE, DB-201 + Process Type: 19.600

Pollutant Information: CHOCOLATE BAYOU PLANT - REGENERATION FURNACE, DB-201

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: REGENERATION HEATER, DB-601 + Process Type: 19.600

Pollutant Information: CHOCOLATE BAYOU PLANT - REGENERATION HEATER, DB-601

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: REGENERATION HEATER, DDB-201 + Process Type: 19.600

Pollutant Information: CHOCOLATE BAYOU PLANT - REGENERATION HEATER, DDB-201

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Dioxide Pollutant Group(s): ( Acid Gasses/Mist , Greenhouse Gasses (GHG) , InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: REGENERATION HEATER, DDB-601 + Process Type: 19.600

Pollutant Information: CHOCOLATE BAYOU PLANT - REGENERATION HEATER, DDB-601

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: 2ND STAGE HYDROTREATER FEED HEATER, J-1 + Process Type: 19.600

Pollutant Information: CHOCOLATE BAYOU PLANT - 2ND STAGE HYDROTREATER FEED HEATER, J-1

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: FURNACE EMISSION CAPS FOR 30 EMISSION POINTS + Process Type: 19.600

Pollutant Information: CHOCOLATE BAYOU PLANT - FURNACE EMISSION CAPS FOR 30 EMISSION POINTS

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate MatterPollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: SCR, LOW NOX BURNERS Cost Effectiveness:

Process Information: CHOCOLATE BAYOU PLANT

+ Process Name: TANK EMISSION CAPS FOR 9 EMISSION POINTS + Process Type: 64.004

Pollutant Information: CHOCOLATE BAYOU PLANT - TANK EMISSION CAPS FOR 9 EMISSION POINTS

+ Pollutant Name Ethyl Benzene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Benzene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Toluene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Hexane Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Styrene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name o-Xylene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: CITY PUBLIC SERVICE LEON CREEK PLANT

RBLC ID: TX-0457 + Corporate/Company Name: CITY PUBLIC SERVICE + Facility Name: CITY PUBLIC SERVICE LEON CREEK PLANT Facility County: BEXAR Facility State: TX Facility ZIP Code: + SIC Code: 351 NAICS Code: 333311 Permit Issuance Date: 06/26/2003 ACT

Process Information: CITY PUBLIC SERVICE LEON CREEK PLANT

+ Process Name: GE LM6000 COMBUSTION TURBINE (4) + Process Type: 15.110Pollutant Information: CITY PUBLIC SERVICE LEON CREEK PLANT - GE LM6000 COMBUSTION TURBINE (4)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: NOX EMISSIONS WILL BE LIMITED TO 5 PPMVD BY ADDING SELECTIVE CATALYTIC REDUCTION (SCR) TECHNOLOGY TO THE EXHAUST STACK. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: A + Control Method Description: OXIDATION CATALYST Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: OXIDATION CATALYST Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: CONTROLLED BY PROPER COMBUSTION OF NATURAL GAS Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:+ Pollutant Name Ammonium (NH4) Compounds Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: CONTROLLED BY PROPER COMBUSTION OF NATURAL GAS Cost Effectiveness:

+ Pollutant Name Sulfuric Acid (mist, vapors, etc) Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: CONTROLLED BY PROPER COMBUSTION OF NATURAL GAS Cost Effectiveness:

Process Information: CITY PUBLIC SERVICE LEON CREEK PLANT

+ Process Name: EMERGENCY GENERATOR (5) + Process Type: 19.900

Pollutant Information: CITY PUBLIC SERVICE LEON CREEK PLANT - EMERGENCY GENERATOR (5)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N+ Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: CITY PUBLIC SERVICE LEON CREEK PLANT

+ Process Name: PLANT FUGITIVES (4) + Process Type: 64.002

Pollutant Information: CITY PUBLIC SERVICE LEON CREEK PLANT - PLANT FUGITIVES (4)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: CITY PUBLIC SERVICE LEON CREEK PLANT

+ Process Name: DIESEL TANK 1 (4) AND (2) + Process Type: 42.010Pollutant Information: CITY PUBLIC SERVICE LEON CREEK PLANT - DIESEL TANK 1 (4) AND (2)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: E. I. DU PONT FORT HILL

RBLC ID: 

### * OH-0340 + Corporate/Company Name: E. I. DU PONT + Facility Name: E. I. DU PONT FORT HILL Facility County: HAMILTON Facility State: OH Facility ZIP Code: 45052 + SIC Code: 2819 NAICS Code: 325188 Permit Issuance Date: 08/06/2010 ACT

Process Information: E. I. DU PONT FORT HILL

+ Process Name: Sulfuric Acid Process + Process Type: 64.000

Pollutant Information: E. I. DU PONT FORT HILL - Sulfuric Acid Process

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: A + Control Method Description: Hydrogen peroxide assisted scrubber Cost Effectiveness:

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method+ Control Method Description: Hydrogen Peroxide Assisted Scrubber for PM as sufuric acid mist Cost Effectiveness:

+ Pollutant Name Sulfuric Acid (mist, vapors, etc) Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: Hydrogen peroxide assisted scrubber Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: EL PASO NATURAL GAS CORNUDAS COMPRESSOR STATION

RBLC ID: TX-0454 + Corporate/Company Name: EL PASO NATURAL GAS COMPANY + Facility Name: EL PASO NATURAL GAS CORNUDAS COMPRESSOR STATION Facility County: HUDSPETH Facility State: TX Facility ZIP Code: + SIC Code: 4922 NAICS Code: 486210 Permit Issuance Date: 10/31/2003 ACT

Process Information: EL PASO NATURAL GAS CORNUDAS COMPRESSOR STATION

+ Process Name: TURBINES (2) + Process Type: 16.110

Pollutant Information: EL PASO NATURAL GAS CORNUDAS COMPRESSOR STATION - TURBINES (2)

+ Pollutant Name Nitrogen Oxides (NOx)Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: LOW NOX BURNERS Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: EL PASO NATURAL GAS CORNUDAS COMPRESSOR STATION

+ Process Name: FUGITIVES (4) + Process Type: 64.002

Pollutant Information: EL PASO NATURAL GAS CORNUDAS COMPRESSOR STATION - FUGITIVES (4)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method+ Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: EVONIK DEGUSSA CORPORATION

RBLC ID: AL-0249 + Corporate/Company Name: EVONIK DEGUSSA CORPORATION + Facility Name: EVONIK DEGUSSA CORPORATION Facility County: MOBILE Facility State: AL Facility ZIP Code: + SIC Code: 2869 NAICS Code: 11 Permit Issuance Date: 01/07/2010 ACT

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: METHIONINE PRODUCTION UNIT - THERMAL OXIDIZER + Process Type: 64.999

Pollutant Information: EVONIK DEGUSSA CORPORATION - METHIONINE PRODUCTION UNIT - THERMAL OXIDIZER

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: THERMAL OXIDIZER - SNCR Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: METHIONINE PRODUCTION UNIT - CEILCOTE SCRUBBER A + Process Type: 64.999

Pollutant Information: EVONIK DEGUSSA CORPORATION - METHIONINE PRODUCTION UNIT - CEILCOTE SCRUBBER A

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBERCost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: METHIONINE PRODUCTION UNIT - CEILCOTE SCRUBBER B + Process Type: 64.999

Pollutant Information: EVONIK DEGUSSA CORPORATION - METHIONINE PRODUCTION UNIT - CEILCOTE SCRUBBER B

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: METHIONINE PRODUCTION UNIT - CEILCOTE SCRUBBER C + Process Type: 64.999

Pollutant Information: EVONIK DEGUSSA CORPORATION - METHIONINE PRODUCTION UNIT - CEILCOTE SCRUBBER C

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: METHIONINE PRODUCTION UNIT - CEILCOTE SCRUBBER D + Process Type: 64.999

Pollutant Information: EVONIK DEGUSSA CORPORATION - METHIONINE PRODUCTION UNIT - CEILCOTE SCRUBBER D

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s):+ Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: METHIONINE PRODUCTION UNIT - CEILCOTE SCRUBBER E + Process Type: 64.999

Pollutant Information: EVONIK DEGUSSA CORPORATION - METHIONINE PRODUCTION UNIT - CEILCOTE SCRUBBER E

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: PACKED BED SCRUBBER Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: EXISTING HCN PRODUCTION UNIT - WASTE HEAT BOILER + Process Type: 12.300

Pollutant Information: EVONIK DEGUSSA CORPORATION - EXISTING HCN PRODUCTION UNIT - WASTE HEAT BOILER

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: SNCR Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: HCN PRODUCTION UNIT - FLARE A1 + Process Type: 19.310

Pollutant Information: EVONIK DEGUSSA CORPORATION - HCN PRODUCTION UNIT - FLARE A1

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICESCost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: HCN PRODUCTION UNIT - FLARE A2 + Process Type: 19.310

Pollutant Information: EVONIK DEGUSSA CORPORATION - HCN PRODUCTION UNIT - FLARE A2

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE)Pollutant Group(s): + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: HCN PRODUCTION UNIT - TANK FARM FLARE - A5 + Process Type: 19.310

Pollutant Information: EVONIK DEGUSSA CORPORATION - HCN PRODUCTION UNIT - TANK FARM FLARE - A5

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method+ Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: AMSUL PRODUCTION UNIT - DUST SCRUBBER - A10 + Process Type: 64.999

Pollutant Information: EVONIK DEGUSSA CORPORATION - AMSUL PRODUCTION UNIT - DUST SCRUBBER - A10

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: ACROLEIN PRODUCTION UNIT - THERMAL OXIDIZER + Process Type: 64.999Pollutant Information: EVONIK DEGUSSA CORPORATION - ACROLEIN PRODUCTION UNIT - THERMAL OXIDIZER

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: LOW NOX BURNERS Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: ANDRUSSOW HCN PRODUCTION UNIT - THERMAL OXIDIZER / WASTE HEAT BOILER + Process Type: 12.300Pollutant Information: EVONIK DEGUSSA CORPORATION - ANDRUSSOW HCN PRODUCTION UNIT - THERMAL OXIDIZER / WASTE HEAT BOILER

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: SNCR Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: ANDRUSSOW HCN PRODUCTION UNIT - FLARE HCNA - 2 + Process Type: 19.310Pollutant Information: EVONIK DEGUSSA CORPORATION - ANDRUSSOW HCN PRODUCTION UNIT - FLARE HCNA - 2

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: EVONIK DEGUSSA CORPORATION

+ Process Name: ANDRUSSOW AMSUL PRODUCTION UNIT DUST SCRUBBER + Process Type: 64.999Pollutant Information: EVONIK DEGUSSA CORPORATION - ANDRUSSOW AMSUL PRODUCTION UNIT DUST SCRUBBER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 2.5 μ (FPM2.5) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: FORMOSA PLASTICS - BATON ROUGE PLANT

RBLC ID: LA-0230 + Corporate/Company Name: FORMOSA PLASTICS CORP + Facility Name: FORMOSA PLASTICS - BATON ROUGE PLANT Facility County: EAST BATON ROUGE Facility State: LA Facility ZIP Code: 708210271 + SIC Code: 2821 NAICS Code: 325211NAICS Code: 325211 Permit Issuance Date: 02/18/2009 ACT

Process Information: FORMOSA PLASTICS - BATON ROUGE PLANT

+ Process Name: VCM UNIT FURNACE D + Process Type: 64.003

Pollutant Information: FORMOSA PLASTICS - BATON ROUGE PLANT - VCM UNIT FURNACE D

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND GASEOUS FUEL BURNING Cost Effectiveness:

Process Information: FORMOSA PLASTICS - BATON ROUGE PLANT

+ Process Name: INCINERATORS A, B, C + Process Type: 21.200

Pollutant Information: FORMOSA PLASTICS - BATON ROUGE PLANT - INCINERATORS A, B, C

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND NATURAL GAS FIRED Cost Effectiveness:

Process Information: FORMOSA PLASTICS - BATON ROUGE PLANT

+ Process Name: VCM UNIT COOLING TOWER + Process Type: 64.006

Pollutant Information: FORMOSA PLASTICS - BATON ROUGE PLANT - VCM UNIT COOLING TOWER

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method+ Control Method Description: GOOD DESIGN, MAINTENANCE AND DRIFT ELIMINATORS Cost Effectiveness:

Process Information: FORMOSA PLASTICS - BATON ROUGE PLANT

+ Process Name: PVC DRYERS + Process Type: 63.036

Pollutant Information: FORMOSA PLASTICS - BATON ROUGE PLANT - PVC DRYERS

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: MULTICYCLONE/SCRUBBER Cost Effectiveness:

Process Information: FORMOSA PLASTICS - BATON ROUGE PLANT

+ Process Name: PVC SILOS + Process Type: 63.036

Pollutant Information: FORMOSA PLASTICS - BATON ROUGE PLANT - PVC SILOS

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAG OR CARTRIDGE FILTER Cost Effectiveness:

Process Information: FORMOSA PLASTICS - BATON ROUGE PLANT

+ Process Name: FUGITIVES + Process Type: 63.036

Pollutant Information: FORMOSA PLASTICS - BATON ROUGE PLANT - FUGITIVES

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD HOUSEKEEPING, WET SUPPRESSION, AND WATER WASH DOWN Cost Effectiveness:Process Information: FORMOSA PLASTICS - BATON ROUGE PLANT

+ Process Name: WASTE PVC DRYER 206 + Process Type: 63.036

Pollutant Information: FORMOSA PLASTICS - BATON ROUGE PLANT - WASTE PVC DRYER 206

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: MULTICYCLONE/SCRUBBER Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: FORMOSA PLASTICS TEXAS

RBLC ID: TX-0309 + Corporate/Company Name: FORMOSA PLASTICS CORPORATION + Facility Name: FORMOSA PLASTICS TEXAS Facility County: CALHOUN Facility State: TX Facility ZIP Code: 77978 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 02/10/2000 ACT

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: COOLING TOWER, 70382E6 + Process Type: 99.009

Pollutant Information: FORMOSA PLASTICS TEXAS - COOLING TOWER, 70382E6

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: (2) FLUSH TANK CARBON ADSORBERS, 70F125-1&-2 + Process Type: 64.999

Pollutant Information: FORMOSA PLASTICS TEXAS - (2) FLUSH TANK CARBON ADSORBERS, 70F125-1&-2

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE CARBON ADSORBER IS A CONTROL FOR VOC Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: (2) STARTUP HEATERS, 70H101-1&-2 + Process Type: 13.900

Pollutant Information: FORMOSA PLASTICS TEXAS - (2) STARTUP HEATERS, 70H101-1&-2

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: PROCESS FLUSH VENT, 70K214 + Process Type: 64.003

Pollutant Information: FORMOSA PLASTICS TEXAS - PROCESS FLUSH VENT, 70K214

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:

+ Pollutant Name Hydrogen Cyanide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:

+ Pollutant Name Acrylonitrile Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: PURIFICATION FLUSH TANK, 70K314 + Process Type: 64.999

Pollutant Information: FORMOSA PLASTICS TEXAS - PURIFICATION FLUSH TANK, 70K314

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: QUENCHER TANK, 70K504 + Process Type: 64.999

Pollutant Information: FORMOSA PLASTICS TEXAS - QUENCHER TANK, 70K504

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: MEHQ TANK, 70K512 + Process Type: 64.004

Pollutant Information: FORMOSA PLASTICS TEXAS - MEHQ TANK, 70K512

+ Pollutant Name Acrylonitrile Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS+ Process Name: AUXILIARY FLUSH TANK + Process Type: 64.006

Pollutant Information: FORMOSA PLASTICS TEXAS - AUXILIARY FLUSH TANK

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: RECYCLE WATER TANK, 70K515 + Process Type: 64.006

Pollutant Information: FORMOSA PLASTICS TEXAS - RECYCLE WATER TANK, 70K515

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:

+ Pollutant Name Hydrogen Cyanide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:

+ Pollutant Name Acrylonitrile Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: A + Control Method Description: SCRUBBER Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: CIRCULATING WATER TANK, 70T204 + Process Type: 64.006Pollutant Information: FORMOSA PLASTICS TEXAS - CIRCULATING WATER TANK, 70T204

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: TEMPERED WATER TANK, 70T215 + Process Type: 64.006

Pollutant Information: FORMOSA PLASTICS TEXAS - TEMPERED WATER TANK, 70T215

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: SULFURIC ACID TANK + Process Type: 62.020

Pollutant Information: FORMOSA PLASTICS TEXAS - SULFURIC ACID TANK

+ Pollutant Name Sulfuric Acid (mist, vapors, etc) Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: ACETIC ACID TANK, 7T502-1 + Process Type: 64.004

Pollutant Information: FORMOSA PLASTICS TEXAS - ACETIC ACID TANK, 7T502-1+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: ACETIC ACID TANK, 7T502-2 + Process Type: 64.004

Pollutant Information: FORMOSA PLASTICS TEXAS - ACETIC ACID TANK, 7T502-2

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: HQ TANK, 70T511 + Process Type: 64.004

Pollutant Information: FORMOSA PLASTICS TEXAS - HQ TANK, 70T511

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: GLYCOL SURGE TANK, 70T513 + Process Type: 64.004

Pollutant Information: FORMOSA PLASTICS TEXAS - GLYCOL SURGE TANK, 70T513

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N+ Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: WASTE HEAT BOILER, 70Z401 + Process Type: 13.310

Pollutant Information: FORMOSA PLASTICS TEXAS - WASTE HEAT BOILER, 70Z401

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Acrylonitrile Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE WASTE HEAT BOILER IS A CONTROL FOR VOC Cost Effectiveness:+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Hydrogen Cyanide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: PROCESS FLARE, 70Z522 + Process Type: 19.310

Pollutant Information: FORMOSA PLASTICS TEXAS - PROCESS FLARE, 70Z522

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE FLARE IS A VOC CONTROL DEVICE Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: PROCESS FUGITIVES, 70ANFUG + Process Type: 64.002

Pollutant Information: FORMOSA PLASTICS TEXAS - PROCESS FUGITIVES, 70ANFUG

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28 LAER Cost Effectiveness:

+ Pollutant Name Hydrogen Cyanide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: 28 AVO Cost Effectiveness:

+ Pollutant Name Acrylonitrile Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: P + Control Method Description: 28 LAER Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: FORMOSA PLASTICS TEXAS

RBLC ID: TX-0327 + Corporate/Company Name: FORMOSA PLASTICS CORPORATION + Facility Name: FORMOSA PLASTICS TEXAS Facility County: CALHOUN Facility State: TX Facility ZIP Code: 77978 + SIC Code: 2821 NAICS Code: 325211 Permit Issuance Date: 02/10/2000 ACT

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: CO2 REGENERATOR VENT, EP221 + Process Type: 64.003Pollutant Information: FORMOSA PLASTICS TEXAS - CO2 REGENERATOR VENT, EP221

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: CAUSTIC TANK GT552, EP552 + Process Type: 62.020

Pollutant Information: FORMOSA PLASTICS TEXAS - CAUSTIC TANK GT552, EP552

+ Pollutant Name Sodium Hydroxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: GT615 TANK, EP615 + Process Type: 64.004

Pollutant Information: FORMOSA PLASTICS TEXAS - GT615 TANK, EP615

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: (3) TANKS, GT630A, B & C, EP630A, B & C + Process Type: 64.004Pollutant Information: FORMOSA PLASTICS TEXAS - (3) TANKS, GT630A, B & C, EP630A, B & C

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: (4) TANKS, GT725A&B & GT730A&B; EP725A&B/EP730A&B + Process Type: 64.004

Pollutant Information: FORMOSA PLASTICS TEXAS - (4) TANKS, GT725A&B & GT730A&B; EP725A&B/EP730A&B

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: GT740 TANK, EP740 + Process Type: 64.004

Pollutant Information: FORMOSA PLASTICS TEXAS - GT740 TANK, EP740

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: GT750 TANK, EP750 + Process Type: 64.004Pollutant Information: FORMOSA PLASTICS TEXAS - GT750 TANK, EP750

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: WASTE HEAT BOILER, EP910 + Process Type: 19.600

Pollutant Information: FORMOSA PLASTICS TEXAS - WASTE HEAT BOILER, EP910

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: THE BOILER IS FOR THE CONTROL OF VOC'S. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2)Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: PIPING FUGITIVES, EGFUG1 + Process Type: 64.002

Pollutant Information: FORMOSA PLASTICS TEXAS - PIPING FUGITIVES, EGFUG1

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 28MIDI + M PROGRAMS Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: COOLING TOWER, EG-CT + Process Type: 99.009

Pollutant Information: FORMOSA PLASTICS TEXAS - COOLING TOWER, EG-CT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: FORMOSA PLASTICS TEXAS

+ Process Name: (4) TANKS, GT806-9; EP806-9 + Process Type: 64.004

Pollutant Information: FORMOSA PLASTICS TEXAS - (4) TANKS, GT806-9; EP806-9

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: JACK COUNTY POWER PLANT

RBLC ID: TX-0458 + Corporate/Company Name: DUKE ENERGY LP + Facility Name: JACK COUNTY POWER PLANT Facility County: JACK Facility State: TX Facility ZIP Code: + SIC Code: 4922 NAICS Code: 333611 Permit Issuance Date: 07/22/2003 ACT

Process Information: JACK COUNTY POWER PLANT

+ Process Name: COMBUSTION TURBINE WITH 550 MMBTU/HR DUCT BURNER + Process Type: 15.110

Pollutant Information: JACK COUNTY POWER PLANT - COMBUSTION TURBINE WITH 550 MMBTU/HR DUCT BURNER

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: SCR Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION TECHNIQUES Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION TECHNIQUES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: BURN LOW SULFUR NATURAL GAS Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: JACK COUNTY POWER PLANT

+ Process Name: COOLING TOWER VENTS (4) + Process Type: 64.003

Pollutant Information: JACK COUNTY POWER PLANT - COOLING TOWER VENTS (4)

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:Process Information: JACK COUNTY POWER PLANT

+ Process Name: AUXILIARY BOILER + Process Type: 13.310

Pollutant Information: JACK COUNTY POWER PLANT - AUXILIARY BOILER

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: JACK COUNTY POWER PLANT+ Process Name: FIRE WATER PUMP ENGINE + Process Type: 19.900

Pollutant Information: JACK COUNTY POWER PLANT - FIRE WATER PUMP ENGINE

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: JACK COUNTY POWER PLANT

+ Process Name: CHILLER VENTS + Process Type: 64.003Pollutant Information: JACK COUNTY POWER PLANT - CHILLER VENTS

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: JACK COUNTY POWER PLANT

+ Process Name: EMERGENCY GENERATOR (6) + Process Type: 19.900

Pollutant Information: JACK COUNTY POWER PLANT - EMERGENCY GENERATOR (6)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10)Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: JACK COUNTY POWER PLANT

+ Process Name: DIESEL TANK + Process Type: 42.009

Pollutant Information: JACK COUNTY POWER PLANT - DIESEL TANK

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: JACK COUNTY POWER PLANT

+ Process Name: ACID TANK + Process Type: 42.009

Pollutant Information: JACK COUNTY POWER PLANT - ACID TANK

+ Pollutant Name Sulfuric Acid (mist, vapors, etc) Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: JACK COUNTY POWER PLANT

+ Process Name: AMMONIA TANK + Process Type: 42.009Pollutant Information: JACK COUNTY POWER PLANT - AMMONIA TANK

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: KENAI REFINERY

RBLC ID: AK-0053 + Corporate/Company Name: TESORO ALASKA COMPANY + Facility Name: KENAI REFINERY Facility County: Facility State: AK Facility ZIP Code: 99611 + SIC Code: 2911 NAICS Code: 324110 Permit Issuance Date: 03/21/2000 ACT

Process Information: KENAI REFINERY

+ Process Name: INJECTION TURBINE CF-C33012-TB + Process Type: 15.110

Pollutant Information: KENAI REFINERY - INJECTION TURBINE CF-C33012-TB

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: BURN FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NO GREATER THAN 200 PPM OR DISTILLATE FUEL OIL WITH A FUEL SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES. COMPLY WITH VE EMISSION LIMITS AS A SURROGATE FOR PM LIMITS. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN HEAD END COMBUSTION TECHNOLOGY Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR TURBINE, CF-G-70001 + Process Type: 15.110

Pollutant Information: KENAI REFINERY - GENERATOR TURBINE, CF-G-70001

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: BURN FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NO GREATER THAN 200 PPM OR DISTILLATE FUEL OIL WITH A FUEL SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method ACCORDING TO BACT-PSD- USE LEAN HEAD END+ Control Method Description: ACCORDING TO BACT-PSD- USE LEAN HEAD END COMBUSTION TECHNOLOGY. ACCORDING TO NSPS- DO NOT OPERATE TURBINE ON FUEL OIL, EXCEPT AS PROVIDED FOR UNDER EMERGENCY FUEL PROVISIONS LISTED IN 40 CFR 60.332(K) Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES. COMPLY WITH VE LIMITS AS A SURROGATE FOR PM EMISSION LIMITS. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR TURBINE, CF-G-70002 + Process Type: 16.110

Pollutant Information: KENAI REFINERY - GENERATOR TURBINE, CF-G-70002

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method BURN FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NO+ Control Method Description: BURN FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NO GREATER THAN 200 PPM OR DISTILLATE FUEL OIL WITH A FUEL SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: DRY LOW NOX COMBUSTION TECHNOLOGY. Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES. COMPLY WITH VE EMISSION LIMITS AS A SURROGATE FOR PM EMISSION LIMITS. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES AND MAINTENANCE Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: CRUDE HEATER, CF-H-31003A + Process Type: 13.310

Pollutant Information: KENAI REFINERY - CRUDE HEATER, CF-H-31003A

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES. COMPLY WITH VE EMISSION LIMITS AS A SURROGATE FOR PM LIMITS. Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: CRUDE HEATER, CF-H-31003B + Process Type: 13.310

Pollutant Information: KENAI REFINERY - CRUDE HEATER, CF-H-31003B

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES. COMPLY WITH VE EMISSION LIMITS AS A SURROGATE FOR PM EMISSION LIMITS. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds )+ Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: UTILITY HEATER MEDIUM, CF-H-64004 + Process Type: 13.900

Pollutant Information: KENAI REFINERY - UTILITY HEATER MEDIUM, CF-H-64004

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES, COMPLY WITH LIMIT OF VE AS SURROGATE FOR PM LIMIT. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: UTILITY HEATER MEDIUM, CF-H-64005 + Process Type: 13.900

Pollutant Information: KENAI REFINERY - UTILITY HEATER MEDIUM, CF-H-64005

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNER Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES. COMPLY WITH VE EMISSION LIMITS AS A SURROGATE FOR PM LIMITS. Cost Effectiveness:+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: EMERGENCY GENERATOR, CF-G-70003 + Process Type: 17.110

Pollutant Information: KENAI REFINERY - EMERGENCY GENERATOR, CF-G-70003

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES AND MAINTENANCE. Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P+ Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: AFTER-COOLING COMBINED WITH HIGH PRESSURE FUEL INJECTION PUMPS AND CYLINDER DESIGN TO ENSURE CLEAN BURN IN THE CYLINDER. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: EMERGENCY GENERATOR, CF-G-70004 + Process Type: 17.110

Pollutant Information: KENAI REFINERY - EMERGENCY GENERATOR, CF-G-70004

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: AFTER-COOLING COMBINED WITH HIGH PRESSURE FUEL INJECTION PUMPS AND CYLINDER DESIGN TO ENSURE CLEAN BURN IN THE CYLINDER. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD OPERATIONAL PRACTICES AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P+ Control Method Description: GOOD OPERATIONAL PRACTICES AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: WASTE INCINERATOR, CF-U-59001A + Process Type: 50.008

Pollutant Information: KENAI REFINERY - WASTE INCINERATOR, CF-U-59001A

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER OPERATION AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER OPERATION AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: REDUCED-SULFUR FUEL Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER OPERATION AND MAINTENANCE Cost Effectiveness:+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: WASTE INCINERATOR, CF-U-590001B + Process Type: 50.008

Pollutant Information: KENAI REFINERY - WASTE INCINERATOR, CF-U-590001B

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER OPERATION AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER OPERATION AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER OPERATION AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: REDUCED-SULFUR FUELS Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N+ Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: HP FLARE, CF-X-35002 + Process Type: 19.330

Pollutant Information: KENAI REFINERY - HP FLARE, CF-X-35002

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER OPERATION AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER OPERATION AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: SMOKELESS DESIGN WITH AIR ASSIST CONFIGURATION Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:Process Information: KENAI REFINERY

+ Process Name: LP FLARE, CF-X-35012 + Process Type: 19.330

Pollutant Information: KENAI REFINERY - LP FLARE, CF-X-35012

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER OPERATION AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER OPERATION AND MAINTENANCE Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: SMOKELESS DESIGN WITH AIR ASSIST CONFIGURATION Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:Process Information: KENAI REFINERY

+ Process Name: GENERATOR DR1 + Process Type: 17.190

Pollutant Information: KENAI REFINERY - GENERATOR DR1

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR DR2 + Process Type: 17.190

Pollutant Information: KENAI REFINERY - GENERATOR DR2

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s):+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR DR3 + Process Type: 17.190

Pollutant Information: KENAI REFINERY - GENERATOR DR3

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR DR4 + Process Type: 17.190Pollutant Information: KENAI REFINERY - GENERATOR DR4

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, DR5 + Process Type: 17.190

Pollutant Information: KENAI REFINERY - GENERATOR, DR5

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2)Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, DR6 + Process Type: 17.190

Pollutant Information: KENAI REFINERY - GENERATOR, DR6

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: RIG MOVE ENGINE NO. 1 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - RIG MOVE ENGINE NO. 1

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: RIG MOVE ENGINE NO. 2 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - RIG MOVE ENGINE NO. 2

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:Process Information: KENAI REFINERY

+ Process Name: RIG MOVE ENGINE NO. 3 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - RIG MOVE ENGINE NO. 3

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: CEMENT PUMP, CP1 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - CEMENT PUMP, CP1

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: CEMENT PUMP, CP2 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - CEMENT PUMP, CP2

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: LISTER BOILER, DR11 + Process Type: 13.900Pollutant Information: KENAI REFINERY - LISTER BOILER, DR11

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: LISTER BOILER, DR12 + Process Type: 13.900

Pollutant Information: KENAI REFINERY - LISTER BOILER, DR12

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A H2S CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A S CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: HEATER, DR13 + Process Type: 13.900

Pollutant Information: KENAI REFINERY - HEATER, DR13

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: HEATER, DR14 + Process Type: 13.900

Pollutant Information: KENAI REFINERY - HEATER, DR14

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s):+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: MUD PLANT HEATER, DR15 + Process Type: 13.900

Pollutant Information: KENAI REFINERY - MUD PLANT HEATER, DR15

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: HEATER, MP1 + Process Type: 13.900

Pollutant Information: KENAI REFINERY - HEATER, MP1

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, BP1 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATOR, BP1

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM)Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, BP2 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATOR, BP2

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: ELECTRIC LINE UNIT ENGINE+ Process Type: 17.190

Pollutant Information: KENAI REFINERY - ELECTRIC LINE UNIT ENGINE

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: SICK LINE UNIT ENGINES + Process Type: 17.190

Pollutant Information: KENAI REFINERY - SICK LINE UNIT ENGINES

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: COIL TUBING UNIT LARGE ENGINES + Process Type: 17.190

Pollutant Information: KENAI REFINERY - COIL TUBING UNIT LARGE ENGINES

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: COIL TUBING UNIT SMALL ENGINES + Process Type: 17.290

Pollutant Information: KENAI REFINERY - COIL TUBING UNIT SMALL ENGINES

+ Pollutant Name Visible Emissions (VE)Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: COIL TUBING UNIT HEATERS + Process Type: 13.900

Pollutant Information: KENAI REFINERY - COIL TUBING UNIT HEATERS

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT+ Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM AND USE DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: WELL FRACTIONATION UNIT SMALL ENGINES + Process Type: 17.190

Pollutant Information: KENAI REFINERY - WELL FRACTIONATION UNIT SMALL ENGINES

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: WELL FRACTIONATION UNIT LARGE ENGINES + Process Type: 17.190

Pollutant Information: KENAI REFINERY - WELL FRACTIONATION UNIT LARGE ENGINES

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NOT TO EXCEED 200 PPM, AND USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: WELL FRACTIONATION UNIT TURBINES + Process Type: 16.900

Pollutant Information: KENAI REFINERY - WELL FRACTIONATION UNIT TURBINES

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: BURN FUEL GAS WITH A HYDROGEN SULFIDE CONTENT NO GREATER THAN 200 PPM OR DISTILLATE FUEL OIL WITH A FUEL SULFUR CONTENT NOT TO EXCEED 0.15%. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, D1 + Process Type: 17.190

Pollutant Information: KENAI REFINERY - GENERATOR, D1

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.15% Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, D2 + Process Type: 17.190

Pollutant Information: KENAI REFINERY - GENERATOR, D2

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, N1 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATOR, N1

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20% Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:Process Information: KENAI REFINERY

+ Process Name: GENERATOR, N2 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATOR, N2

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20% Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, 1 + Process Type: 17.190

Pollutant Information: KENAI REFINERY - GENERATOR, 1

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20%. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, 2 + Process Type: 17.190

Pollutant Information: KENAI REFINERY - GENERATOR, 2

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20%. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: INCINERATOR, 3 + Process Type: 50.008

Pollutant Information: KENAI REFINERY - INCINERATOR, 3+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20% Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, 4 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATOR, 4

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20%.Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, 5 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATOR, 5

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20%. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, 7 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATOR, 7

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20%. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, 8 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATOR, 8

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20%. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, 9 + Process Type: 17.290Pollutant Information: KENAI REFINERY - GENERATOR, 9

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20%. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATORS, 10-23 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATORS, 10-23

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20% Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s):+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, 24 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATOR, 24

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20%. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: GENERATOR, 25 + Process Type: 17.290

Pollutant Information: KENAI REFINERY - GENERATOR, 25

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE ONLY DISTILLATE FUEL OIL WITH A SULFUR CONTENT NOT TO EXCEED 0.20%. Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: METHANOL STORAGE TANKS + Process Type: 64.004

Pollutant Information: KENAI REFINERY - METHANOL STORAGE TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: KENAI REFINERY

+ Process Name: FUEL OIL STORAGE TANKS + Process Type: 42.005

Pollutant Information: KENAI REFINERY - FUEL OIL STORAGE TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: MILNE POINT PRODUCTION FACILITY

RBLC ID: AK-0047 + Corporate/Company Name: BP EXPLORATION (ALASKA) INC. + Facility Name: MILNE POINT PRODUCTION FACILITY Facility County: Facility State: AK Facility ZIP Code: 99519 + SIC Code: 1311 NAICS Code: 211111 Permit Issuance Date: 07/13/2001 ACT

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: TURBINES (2), PU-0701 AND PU-0801 + Process Type: 16.110

Pollutant Information: MILNE POINT PRODUCTION FACILITY - TURBINES (2), PU-0701 AND PU-0801

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FUEL SULFUR CONTENT LIMIT; BURN NATURAL GAS WITH NO GREATER THAN 100 PPM H2S IN ANY OF THE FUEL BURNING EQUIPMENT. Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: SOURCE HAS OPTION OF USING DIRECT WATER INJECTION OR THE FOLLOWING OPERATING LIMITS: 21,371 KW (GENERATOR OUTPUT) EACH WHEN USING NATURAL GAS OR 7,771 KW (GENERATOR OUTPUT) EACH WHEN USING FUEL OILCost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NO ADDITIONAL CONTROLS IS BACT. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: BURN NATURAL GAS WITH NO GREATER THAN 100 PPM H2S. BURN FUEL OIL WITH NO GREATER THAN 0.30 % SULFUR BY WEIGHT. Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: HEATERS (2), H-5302A AND H-5302B + Process Type: 13.310

Pollutant Information: MILNE POINT PRODUCTION FACILITY - HEATERS (2), H-5302A AND H-5302B

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LIMIT EXTENDED FROM PREVIOUS PERMIT TO AVOID PSD REVIEW. Cost Effectiveness:+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: BURN NATURAL GAS WITH NO GREATER THAN 100 PPM H2S. BURN FUEL OIL WITH NO GREATER THAN 0.30 % SULFUR BY WEIGHT. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: LIMIT EXTENDED FROM PREVIOUS PERMIT TO AVOID PSD REVIEW. FOLLOW PREVENTATIVE MAINTENANCE PROCEDURES. Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: HEATERS (2), H-4510A AND H-4510B + Process Type: 13.310

Pollutant Information: MILNE POINT PRODUCTION FACILITY - HEATERS (2), H-4510A AND H-4510B

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: LIMIT EXTENDED FROM PREVIOUS PERMIT TO AVOID PSD REVIEW. Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2)Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: USE FUEL OIL WITH NO GREATER THAN 0.3% SULFUR BY WEIGHT AND NATURAL GAS WITH NO GREATER THAN 100 PPMVD. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: LIMIT EXTENDED FROM PREVIOUS PERMIT TO AVOID PSD REVIEW. FOLLOW PREVENTATIVE MAINTENANCE PROCEDURES. Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: HEATERS (2), H-5701A AND H-5701B + Process Type: 13.310

Pollutant Information: MILNE POINT PRODUCTION FACILITY - HEATERS (2), H-5701A AND H-5701B

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: BACT LIMIT EXTENDED FROM PREVIOUS PERMIT TO AVOID PSD REVIEW. Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) )+ Control Method Code: P + Control Method Description: BURN NATURAL GAS WITH NO GREATER THAN 100 PPM H2S. BURN FUEL OIL WITH NO GREATER THAN 0.30 % SULFUR BY WEIGHT. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PREVENTATIVE MAINTENANCE PROCEDURES Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: ENGINES (2), PU-0110A AND PU-0110B + Process Type: 17.210

Pollutant Information: MILNE POINT PRODUCTION FACILITY - ENGINES (2), PU-0110A AND PU-0110B

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description:Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: BURN FUEL OIL WITH NO GREATER THAN 0.30 % SULFUR BY WEIGHT. Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: HEATERS (2), H-2001A AND H-2001B + Process Type: 13.310

Pollutant Information: MILNE POINT PRODUCTION FACILITY - HEATERS (2), H-2001A AND H-2001B

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FUEL SULFUR CONTENT LIMIT; BURN NATURAL GAS WITH NO GREATER THAN 100 PPM H2S IN ANY OF THE FUEL BURNING EQUIPMENT. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: BACT LIMIT EXTENDED FROM PREVIOUS PERMIT TO AVOID PSD REVIEW. DO NOT OPERATE HEATERS ON FUEL OIL AT ANY TIME. REPLACE BOTH HEATERS WITH LOW NOX BURNERS NO LATER THAN 180 D AFTER PERMIT ISSUANCE. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: BACT LIMIT EXTENDED FROM PREVIOUS PERMIT TO AVOID PSD REVIEW. FOLLOW PREVENTATIVE MAINTENANCE PROCEDURES. Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: ENGINES (3), PU-0101A, PU-0101B, PU-0101C+ Process Type: 17.110

Pollutant Information: MILNE POINT PRODUCTION FACILITY - ENGINES (3), PU-0101A, PU-0101B, PU-0101C

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FUEL SULFUR CONTENT LIMIT; BURN NATURAL GAS WITH NO GREATER THAN 100 PPM H2S IN ANY OF THE FUEL BURNING EQUIPMENT. Cost Effectiveness:

+ Pollutant Name Sulfur / Sulfates Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: P + Control Method Description: BURN FUEL OIL WITH NO GREATER THAN 0.30% SULFUR BY WEIGHT Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: ENGINE (1), PU-4703 + Process Type: 17.210

Pollutant Information: MILNE POINT PRODUCTION FACILITY - ENGINE (1), PU-4703

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FUEL SULFUR CONTENT LIMIT; BURN NATURAL GAS WITH NO GREATER THAN 100 PPM H2S IN ANY OF THE FUEL BURNING EQUIPMENT. Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: ENGINE (1), PU-2004 + Process Type: 17.110

Pollutant Information: MILNE POINT PRODUCTION FACILITY - ENGINE (1), PU-2004

+ Pollutant Name Sulfur / Sulfates Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: P+ Control Method Description: BURN FUEL OIL WITH NO GREATER THAN 0.30% SULFUR BY WEIGHT Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FUEL SULFUR CONTENT LIMIT; BURN NATURAL GAS WITH NO GREATER THAN 100 PPM H2S IN ANY OF THE FUEL BURNING EQUIPMENT. Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: FLARE + Process Type: 19.330

Pollutant Information: MILNE POINT PRODUCTION FACILITY - FLARE

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: BURN FUEL OIL WITH NO GREATER THAN 0.3% SULFUR BY WEIGHT AND NATURAL GAS WITH NO GREATER THAN 100 PPMVD H2S. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: TANK, T-6101A + Process Type: 42.005Pollutant Information: MILNE POINT PRODUCTION FACILITY - TANK, T-6101A

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: COMPLIANCE WITH THE RECORDKEEPING PROVISIONS OF 40 CFR SUBPART KB. Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: TANK, T-2002 + Process Type: 64.004

Pollutant Information: MILNE POINT PRODUCTION FACILITY - TANK, T-2002

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: COMPLIANCE WITH THE RECORDKEEPING PROVISIONS OF 40 CFR SUBPART KB. Cost Effectiveness:

Process Information: MILNE POINT PRODUCTION FACILITY

+ Process Name: VENTS + Process Type: 50.002

Pollutant Information: MILNE POINT PRODUCTION FACILITY - VENTS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GAS BLANKETING AND BACK PRESSURE RELIEF VALVE FOR OIL RESERVE TANKS. WITHIN 60 D OF ISSUANCE, DO NOT VENT GAS TO ATMOSPHERE FROM PRODUCED WATER SURGE TANK. ISOLATE PRESSURE CONTROL VALVE. Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform)Facility Information: MONT BELVIEU COMPLEX

RBLC ID: TX-0333 + Corporate/Company Name: TAME ENVIRO-FUEL PARTNERS - ENTERPRISE PRODUCTS CO + Facility Name: MONT BELVIEU COMPLEX Facility County: CHAMBERS Facility State: TX Facility ZIP Code: 77210 + SIC Code: 2869 NAICS Code: 320000 Permit Issuance Date: 12/05/2000 ACT

Process Information: MONT BELVIEU COMPLEX

+ Process Name: SOLAR TURBINE & DUCT BURNER, 70 + Process Type: 19.700

Pollutant Information: MONT BELVIEU COMPLEX - SOLAR TURBINE & DUCT BURNER, 70

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER (OPTIMAL) OPERATION Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: SELECTIVE CATALYTIC REDUCTION Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: A + Control Method Description: CATALYTIC OXIDATION Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: MONT BELVIEU COMPLEX

+ Process Name: DUCT BURNERS + Process Type: 12.310

Pollutant Information: MONT BELVIEU COMPLEX - DUCT BURNERS

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: CATALYTIC OXIDATION Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: SELECTIVE CATALYTIC REDUCTION Cost Effectiveness:Process Information: MONT BELVIEU COMPLEX

+ Process Name: CONTINUOUS CATALYST REGENERATOR, 71 + Process Type: 64.999

Pollutant Information: MONT BELVIEU COMPLEX - CONTINUOUS CATALYST REGENERATOR, 71

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER (OPTIMAL) OPERATION Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: A + Control Method Description: CAUSTIC SCRUBBER Cost Effectiveness:

+ Pollutant Name Chlorine / Chlorine Compounds Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) ) + Control Method Code: A + Control Method Description: CAUSTIC SCRUBBER Cost Effectiveness:

+ Pollutant Name Hydrochloric Acid Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) , InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: A+ Control Method Description: CAUSTIC SCRUBBER Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: MONT BELVIEU COMPLEX

+ Process Name: REACTOR HEATER, 72 + Process Type: 19.600

Pollutant Information: MONT BELVIEU COMPLEX - REACTOR HEATER, 72

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER (OPTIMAL) OPERATION Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW-NOX BURNERS, FIRING NAT GAS Cost Effectiveness:+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FIRING NAT GAS Cost Effectiveness:

Process Information: MONT BELVIEU COMPLEX

+ Process Name: 3 DIP TURBINES & 3 DUCT BURNERS, 74 + Process Type: 19.700

Pollutant Information: MONT BELVIEU COMPLEX - 3 DIP TURBINES & 3 DUCT BURNERS, 74

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FIRING NAT GAS WITH S CONCENTRATION OF NO MORE THAN 15 PPMW. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER (OPTIMAL) OPERATION Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: SELECTIVE CATALYTIC REDUCTION Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds )+ Control Method Code: A + Control Method Description: CATALYTIC OXIDATION Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: MONT BELVIEU COMPLEX

+ Process Name: FLARE, 76 + Process Type: 19.310

Pollutant Information: MONT BELVIEU COMPLEX - FLARE, 76

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: MONT BELVIEU COMPLEX

+ Process Name: COOLING TOWER, C70 + Process Type: 99.009

Pollutant Information: MONT BELVIEU COMPLEX - COOLING TOWER, C70

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: MONT BELVIEU COMPLEX

+ Process Name: (2) WASTEWATER SUMPS, 73 & 75 + Process Type: 64.006

Pollutant Information: MONT BELVIEU COMPLEX - (2) WASTEWATER SUMPS, 73 & 75

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: MONT BELVIEU COMPLEX

+ Process Name: (1) WASTE OIL TANK & (2) LUBE OIL TANKS, 78,80,80A + Process Type: 64.004

Pollutant Information: MONT BELVIEU COMPLEX - (1) WASTE OIL TANK & (2) LUBE OIL TANKS, 78,80,80A

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: MONT BELVIEU COMPLEX

+ Process Name: FIREWATER PUMP, 81 + Process Type: 19.800

Pollutant Information: MONT BELVIEU COMPLEX - FIREWATER PUMP, 81

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

Process Information: MONT BELVIEU COMPLEX

+ Process Name: PROCESS FUGITIVES, F70 + Process Type: 64.003

Pollutant Information: MONT BELVIEU COMPLEX - PROCESS FUGITIVES, F70

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: NAFTA REGION OLEFINS COMPLEX

RBLC ID: TX-0353 + Corporate/Company Name: BASF CORPORATION + Facility Name: NAFTA REGION OLEFINS COMPLEX Facility County: JEFFERSON Facility State: TX Facility ZIP Code: 77643 + SIC Code: 2869 NAICS Code: 325110 Permit Issuance Date: 09/05/2001 ACT

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: (2) PRODUCT INHIBITOR TANK & ANTIFORM VESSEL VENTS + Process Type: 64.003

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - (2) PRODUCT INHIBITOR TANK & ANTIFORM VESSEL VENTS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B+ Control Method Description: INTERNAL FLOATING ROOF WITH SPECIFIED CLOSURES OR EQUIV. UNINSULATED TANK EXTERIOR SURFACES EXPOSED TO THE SUN SHALL BE WHITE OR ALUMINUM. SPECIFIC PROCEDURES FOR INSPECTION, REPAIR, AND LOADING. Cost Effectiveness:

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: LOW PRESSURE FLARE, P-6 + Process Type: 19.310

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - LOW PRESSURE FLARE, P-6

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATEDCost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: HIGH PRESSURE FLARE, P-7 + Process Type: 19.310

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - HIGH PRESSURE FLARE, P-7

+ Pollutant Name o-Xylene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: STORMWATER TANK, TK-9804 + Process Type: 64.006

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - STORMWATER TANK, TK-9804

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES OF INSPECTION, MITIGATION, AND REPAIR AS SPECIFIED IN PERMIT. Cost Effectiveness:

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: 98% SULFURIC ACID TANK, TK-9810 + Process Type: 64.004

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - 98% SULFURIC ACID TANK, TK-9810

+ Pollutant Name Sulfuric Acid (mist, vapors, etc) Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: N+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Trioxide Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: COOLING TOWER, CT + Process Type: 99.009

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - COOLING TOWER, CT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES SPECIFIED IN PERMIT FOR TESTING AND REPAIR. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: FUGITIVES INALK UNIT, ALKFUG + Process Type: 64.999

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - FUGITIVES INALK UNIT, ALKFUG

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: FUGITIVES BUTADIENE UNIT, BDEFUG + Process Type: 64.999

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - FUGITIVES BUTADIENE UNIT, BDEFUG

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: TANK TRUCK LOADING, P-10 + Process Type: 64.005

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - TANK TRUCK LOADING, P-10

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: FOLLOW PROCEDURES FOR INSPECTION, MITIGATION, AND REPAIR AS SPECIFIED IN PERMIT. Cost Effectiveness:

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: DRUM LOADING, P-11 + Process Type: 64.005

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - DRUM LOADING, P-11

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FOLLOW SPECIFIC LOADING PROCEDURES FOR REPORTING, INSPECTION, AND REPAIR. Cost Effectiveness:Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: BOILER, BLR + Process Type: 19.600

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - BOILER, BLR

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: DRY LOW NOX BURNERS & SELECTIVE CATALYTIC REDUCTION Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FUEL SULFUR CONTENT LIMIT: THE NATURAL GAS STREAM SHALL CONTAIN LESS THAN 5 GR TOTAL SULFUR/100 DSCF. Cost Effectiveness:

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: FUGITIVES - NH3 STORAGE, NH3FUGST + Process Type: 64.999

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - FUGITIVES - NH3 STORAGE, NH3FUGST

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR INSPECTION, ACCIDENT PREVENTION, AND MITIGATION. Cost Effectiveness:

Process Information: NAFTA REGION OLEFINS COMPLEX

+ Process Name: FUGITIVES - INJECTION SKID, NH3FUGSKID + Process Type: 64.999

Pollutant Information: NAFTA REGION OLEFINS COMPLEX - FUGITIVES - INJECTION SKID, NH3FUGSKID

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PREVENTION AND MITIGATION PROCEDURES FOR ACCIDENTAL RELEASE OF EMISSIONS. FOLLOW INSPECTION PROCEDURES. Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: NATUREWORKS, LLC

RBLC ID: NE-0042 + Corporate/Company Name: + Facility Name: NATUREWORKS, LLC Facility County: WASHINGON Facility State: NE Facility ZIP Code: 68008 + SIC Code: 01 NAICS Code: 111998 Permit Issuance Date: 09/29/2006 ACT

Process Information: NATUREWORKS, LLC

+ Process Name: FERMENTATION + Process Type: 64.999

Pollutant Information: NATUREWORKS, LLC - FERMENTATION

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: ROUTE VOCS IN SOLUTION TO THE FINISHING PROCESS RTO. Cost Effectiveness:

Process Information: NATUREWORKS, LLC

+ Process Name: LACTIC ACID PRODUCTION + Process Type: 64.999

Pollutant Information: NATUREWORKS, LLC - LACTIC ACID PRODUCTION

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: REGENERATIVE THERMAL OXIDIZER Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: NORCO CHEMICAL PLANT, M-UNIT

RBLC ID: LA-0199 + Corporate/Company Name: SHELL CHEMICAL LP + Facility Name: NORCO CHEMICAL PLANT, M-UNIT Facility County: ST. CHARLES Facility State: LA Facility ZIP Code: 70079 + SIC Code: 2869 NAICS Code: 325199 Permit Issuance Date: 03/21/2003 ACT

Process Information: NORCO CHEMICAL PLANT, M-UNIT

+ Process Name: DEHYDROGENATION FURNACES (4) + Process Type: 13.310

Pollutant Information: NORCO CHEMICAL PLANT, M-UNIT - DEHYDROGENATION FURNACES (4)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES AND ENGINEERING DESIGN Cost Effectiveness:

Process Information: NORCO CHEMICAL PLANT, M-UNIT

+ Process Name: DISTILLATION POLYMER RUNDOWN TANK (T-M942) + Process Type: 64.004

Pollutant Information: NORCO CHEMICAL PLANT, M-UNIT - DISTILLATION POLYMER RUNDOWN TANK (T-M942)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: INTERNAL FLOATING ROOF AND SUBMERGED FILL PIPE Cost Effectiveness:Process Information: NORCO CHEMICAL PLANT, M-UNIT

+ Process Name: FINISHED SBA RUNDOWN TANKS (T-M943, T-M944) + Process Type: 64.004

Pollutant Information: NORCO CHEMICAL PLANT, M-UNIT - FINISHED SBA RUNDOWN TANKS (T-M943, T-M944)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: SUBMERGED FILL PIPE Cost Effectiveness:

Process Information: NORCO CHEMICAL PLANT, M-UNIT

+ Process Name: CRUDE SBA TANK (T-M955) + Process Type: 64.004

Pollutant Information: NORCO CHEMICAL PLANT, M-UNIT - CRUDE SBA TANK (T-M955)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: INTERNAL FLOATING ROOF AND SUBMERGED FILL PIPE Cost Effectiveness:

Process Information: NORCO CHEMICAL PLANT, M-UNIT

+ Process Name: DISTILLATION POLYMER RUNDOWN TANK (T-M946) + Process Type: 64.004

Pollutant Information: NORCO CHEMICAL PLANT, M-UNIT - DISTILLATION POLYMER RUNDOWN TANK (T-M946)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: INTERNAL FLOATING ROOF AND SUBMERGED FILL PIPE Cost Effectiveness:Process Information: NORCO CHEMICAL PLANT, M-UNIT

+ Process Name: SBA FEED TANK (T-M955) + Process Type: 64.004

Pollutant Information: NORCO CHEMICAL PLANT, M-UNIT - SBA FEED TANK (T-M955)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: INTERNAL FLOATING ROOF AND SUBMERGED FILL PIPE Cost Effectiveness:

Process Information: NORCO CHEMICAL PLANT, M-UNIT

+ Process Name: SBA WATER CUTS TANK (T-S941) + Process Type: 64.004

Pollutant Information: NORCO CHEMICAL PLANT, M-UNIT - SBA WATER CUTS TANK (T-S941)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: INTERNAL FLOATING ROOF AND SUBMERGED FILL PIPE Cost Effectiveness:

Process Information: NORCO CHEMICAL PLANT, M-UNIT

+ Process Name: HEXANE STORAGE TANK (T-S954) + Process Type: 64.004

Pollutant Information: NORCO CHEMICAL PLANT, M-UNIT - HEXANE STORAGE TANK (T-S954)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: INTERNAL FLOATING ROOF AND SUBMERGED FILL PIPE Cost Effectiveness:Process Information: NORCO CHEMICAL PLANT, M-UNIT

+ Process Name: MEK BARGE TANK (T-B901) + Process Type: 64.004

Pollutant Information: NORCO CHEMICAL PLANT, M-UNIT - MEK BARGE TANK (T-B901)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: INTERNAL FLOATING ROOF AND SUBMERGED FILL PIPE Cost Effectiveness:

Process Information: NORCO CHEMICAL PLANT, M-UNIT

+ Process Name: W.S. GROUND FLARE + Process Type: 19.310

Pollutant Information: NORCO CHEMICAL PLANT, M-UNIT - W.S. GROUND FLARE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: POWER COUNTY ADVANCED ENERGY CENTER

RBLC ID: ID-0017 + Corporate/Company Name: SOUTHEAST IDAHO ENERGY, LLC + Facility Name: POWER COUNTY ADVANCED ENERGY CENTER Facility County: POWER Facility State: ID Facility ZIP Code: 83211 + SIC Code: 2873 NAICS Code: 113210 Permit Issuance Date: 02/10/2009 ACTProcess Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: ZLDS COOLING TOWER, SRC30 + Process Type: 99.009

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - ZLDS COOLING TOWER, SRC30

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: DRIFT/MIST ELIMINATORS Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: DRIFT/MIST ELIMINATORS Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: COAL/PETCOKE RAILCAR UNLOADING & STORAGE, SRC01-SRC07 + Process Type: 90.011

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - COAL/PETCOKE RAILCAR UNLOADING & STORAGE, SRC01-SRC07

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: ENCLOSED RAILCAR UNLOADING AT NEGATIVE PRESSURE. COVERED CONVEYORS AND ENCLOSED TRANSFER POINTS. STORAGE IN EUROSILO OR EQUIVALENT. HIGH EFFICIENCY BAGHOUSES (RAILCAR UNLOADING, CONVEYORS, STORAGE SILO VENTS). Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: B + Control Method ENCLOSED RAILCAR UNLOADING AT NEGATIVE PRESSURE.+ Control Method Description: ENCLOSED RAILCAR UNLOADING AT NEGATIVE PRESSURE. COVERED CONVEYORS AND ENCLOSED TRANSFER POINTS. STORAGE IN EUROSILO OR EQUIVALENT. HIGH EFFICIENCY BAGHOUSES (RAILCAR UNLOADING, CONVEYORS, STORAGE SILO VENTS). Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: COAL/PETCOKE RECLAIM TO ROD MILL, SRC08-SRC12 + Process Type: 90.011

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - COAL/PETCOKE RECLAIM TO ROD MILL, SRC08-SRC12

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: COVERED CONVEYORS WITH ENCLOSED TRANSFER POINTS. HIGH EFFICIENCY BAGHOUSES. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: COVERED CONVEYORS WITH ENCLOSED TRANSFER POINTS. HIGH EFFICIENCY BAGHOUSES. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: FLUXANT TRUCK LDOUT & CONVEYING, FUG + Process Type: 90.019

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - FLUXANT TRUCK LDOUT & CONVEYING, FUG

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: COVERED CONVEYORS AND ENCLOSED TRANSFER POINTS. FUGITIVE DUST BMPS. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: COVERED CONVEYORS AND ENCLOSED TRANSFER POINTS. FUGITIVE DUST BMPS. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: FLUXANT STORAGE, SRCXX + Process Type: 90.019

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - FLUXANT STORAGE, SRCXX

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: HIGH EFFICIENCY BAGHOUSE(S) ON STORAGE SILO VENT(S) Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: HIGH EFFICIENCY BAGHOUSE(S) ON STORAGE SILO VENT(S) Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: SLAG HAND, FUG + Process Type: 99.190

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - SLAG HAND, FUG

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: STORAGE IN 3-SIDED BUNKER. FUGITIVE DUST BMPS. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method+ Control Method Description: STORAGE IN 3-SIDED BUNKER. FUGITIVE DUST BMPS. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: LEAKS - SYNGAS PIPING OR VALVES, CO FUG + Process Type: 64.002

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - LEAKS - SYNGAS PIPING OR VALVES, CO FUG

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: FUGITIVE CO BMPS. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: ASU REGEN HEATER, 0.1 MMBTU/H, SRC13 + Process Type: 19.600

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - ASU REGEN HEATER, 0.1 MMBTU/H, SRC13

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method+ Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: GASIFIER HEATERS (2), 25 MMBTU/H, SRC14 & SRC15 + Process Type: 19.600

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - GASIFIER HEATERS (2), 25 MMBTU/H, SRC14 & SRC15

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. Cost Effectiveness:Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: GASIFIER FLARE, SRC16 + Process Type: 19.310

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - GASIFIER FLARE, SRC16

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: SMOKELESS FLARE. AIR OR STEAM-ASSIST ONLY IF UNASSISTED FLARE PRODUCES SMOKE. GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: SMOKELESS FLARE. AIR OR STEAM-ASSIST ONLY IF UNASSISTED FLARE PRODUCES SMOKE. GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FLARE DESIGNED TO MINIMIZE CO EMISSIONS. GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: SELEXOL AGR CO2 VENT, SRC17 + Process Type: 64.003Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - SELEXOL AGR CO2 VENT, SRC17

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: A + Control Method Description: THERMAL OXIDIZER (CAT-OX) Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES FOR THERMAL OXIDIZER (CAT-OX) USED TO CONTROL CO EMISSIONS. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: UREA GRANULATION VENT, SRC19 + Process Type: 61.012

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - UREA GRANULATION VENT, SRC19

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: WET SCRUBBER IS INTEGRAL PART OF GRANULATION PROCESS, IS PROCESS EQUIPMENT. DESIGNED FOR MIN 98% CAPTURE AND RECYCLING OF PM/PM10. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: WET SCRUBBER IS INTEGRAL PART OF GRANULATION PROCESS, IS PROCESS EQUIPMENT. DESIGNED FOR MIN 98% CAPTURE AND RECYCLING OF PM/PM10. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: NITRIC ACID PLANT TAILGAS, SRC20 + Process Type: 62.014Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - NITRIC ACID PLANT TAILGAS, SRC20

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: SCR, AMMONIA SLIP MAX 10 PPMV (DRY) CONVERTED TO 15% O2. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: PROCESS FLARE, SRC21 + Process Type: 19.310

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - PROCESS FLARE, SRC21

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: SMOKELESS FLARE. AIR OR STEAM-ASSIST ONLY IF UNASSISTED FLARE PRODUCES SMOKE. GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: SMOKELESS FLARE. AIR OR STEAM-ASSIST ONLY IF UNASSISTED FLARE PRODUCES SMOKE. GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds )+ Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: COOLING TOWER, SRC22 + Process Type: 99.009

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - COOLING TOWER, SRC22

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: DRIFT/MIST ELIMINATORS Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: DRIFT/MIST ELIMINATORS Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: 250 MMBTU/H PACKAGE BOILER, SRC24 + Process Type: 12.310

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - 250 MMBTU/H PACKAGE BOILER, SRC24

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method+ Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: LOW-NOX BURNER AND FGR Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: 250 MMBTU/H STEAM SUPERHEATER BOILER, SRC31 + Process Type: 12.300

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - 250 MMBTU/H STEAM SUPERHEATER BOILER, SRC31

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW-NOX BURNER & SCR, AMMONIA SLIP LIMITED TO 10 PPM (DRY) CORRECTED TO 15% O2. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: 2 MW EMERGENCY GENERATOR, SRC25 + Process Type: 17.110

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - 2 MW EMERGENCY GENERATOR, SRC25

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: ULSD FUEL, GOOD COMBUSTION PRACTICES, EPA CERTIFIED PER NSPS IIII Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: ULSD FUEL, GOOD COMBUSTION PRACTICES, EPA CERTIFIED PER NSPS IIII Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. EPA CERTIFIED PER NSPS IIII Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. EPA CERTIFIED PER NSPS IIII Cost Effectiveness:Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: 500 KW EMERGENCY GENERATOR, FIRE PUMP, SRC26 + Process Type: 17.110

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - 500 KW EMERGENCY GENERATOR, FIRE PUMP, SRC26

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: ULSD FUEL, EPA CERTIFICATION PER NSPS IIII Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: ULSD FUEL, EPA CERTIFICATION PER NSPS IIII Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. EPA CERTIFICATION PER NSPS IIII. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. EPA CERTIFICATION PER NSPS IIII. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: AMMONIA STORAGE FLARE, SRC27 + Process Type: 19.310

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - AMMONIA STORAGE FLARE, SRC27

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10)Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: SMOKELESS FLARE. AIR OR STEAM-ASSIST ONLY IF UNASSISTED FLARE PRODUCES SMOKE. GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: SMOKELESS FLARE. AIR OR STEAM-ASSIST ONLY IF UNASSISTED FLARE PRODUCES SMOKE. GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: GOOD COMBUSTION PRACTICES. MEET 40 CFR 60.18. Cost Effectiveness:

Process Information: POWER COUNTY ADVANCED ENERGY CENTER

+ Process Name: AMMONIUM NITRATE NEUTRALIZER VENT, SRC29 + Process Type: 61.012

Pollutant Information: POWER COUNTY ADVANCED ENERGY CENTER - AMMONIUM NITRATE NEUTRALIZER VENT, SRC29

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: WET SCRUBBER IS INTEGRAL TO PROCESS. MUST BE DESIGNED TO CAPTURE AND RECYCLE 90% OF PM/PM10. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: WET SCRUBBER IS INTEGRAL TO PROCESS. MUST BE DESIGNED TO CAPTURE AND RECYCLE 90% OF PM/PM10. Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: QUAKER CHEMICAL CORPORATION

RBLC ID: MI-0270 + Corporate/Company Name: + Facility Name: QUAKER CHEMICAL CORPORATION Facility County: WAYNE Facility State: MI Facility ZIP Code: 48238 + SIC Code: 2992 NAICS Code: Permit Issuance Date: 12/19/2000 ACT

Process Information: QUAKER CHEMICAL CORPORATION

+ Process Name: CHEMICAL PRODUCTION, TOTAL + Process Type: 64.001

Pollutant Information: QUAKER CHEMICAL CORPORATION - CHEMICAL PRODUCTION, TOTAL

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: 3 STAGE SCRUBBER. 75% CAPTURE, 90% REMOVAL Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: 3 STAGE SCRUBBER. ENGINEERING JUDGEMENT OF 80% CAPTURE, 60% REMOVAL Cost Effectiveness:

+ Pollutant Name Hazardous Air Pollutants (HAP)Pollutant Group(s): ( Hazardous Air Pollutants (HAP) ) + Control Method Code: A + Control Method Description: 3 STAGE SCRUBBER SYSTEM. INCLUDING 97.6% CONTROL OF H2S, 95.9% ACROLEIN . PRIMARY LIMIT IS FOR INDIVIDUAL HAP, ALTERNATE FOR TOTAL HAPS. Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: RICHARDTON PLANT

RBLC ID: ND-0020 + Corporate/Company Name: RED TRAIL ENERGY, LLC + Facility Name: RICHARDTON PLANT Facility County: STARK Facility State: ND Facility ZIP Code: 58652 + SIC Code: 2869 NAICS Code: 325193 Permit Issuance Date: 08/04/2004 ACT

Process Information: RICHARDTON PLANT

+ Process Name: BOILER, COAL-FIRED + Process Type: 12.110

Pollutant Information: RICHARDTON PLANT - BOILER, COAL-FIRED

+ Pollutant Name Sulfur Oxides (SOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: LIMESTONE INJECTION INTO THE BOILER AND A LIME SPRAY DRYER. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: SNCR Cost Effectiveness:+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

Process Information: RICHARDTON PLANT

+ Process Name: DDGS COOLING + Process Type: 70.120

Pollutant Information: RICHARDTON PLANT - DDGS COOLING

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method+ Control Method Description: BAGHOUSE Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

Process Information: RICHARDTON PLANT

+ Process Name: ETHANOL LOADOUT + Process Type: 64.005

Pollutant Information: RICHARDTON PLANT - ETHANOL LOADOUT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: VAPOR COMBUSTION UNIT (ENCLOSED FLARE) Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: RICHARDTON PLANT

+ Process Name: GRAIN RECEIVING + Process Type: 70.230

Pollutant Information: RICHARDTON PLANT - GRAIN RECEIVING+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

Process Information: RICHARDTON PLANT

+ Process Name: HAMMERMILLING + Process Type: 70.290

Pollutant Information: RICHARDTON PLANT - HAMMERMILLING

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

Process Information: RICHARDTON PLANT

+ Process Name: DDGS LOADOUT + Process Type: 70.230

Pollutant Information: RICHARDTON PLANT - DDGS LOADOUT

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method+ Control Method Description: BAGHOUSE Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

Process Information: RICHARDTON PLANT

+ Process Name: FERMENTATION + Process Type: 70.120

Pollutant Information: RICHARDTON PLANT - FERMENTATION

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

Process Information: RICHARDTON PLANT

+ Process Name: COAL HANDLING + Process Type: 90.011

Pollutant Information: RICHARDTON PLANT - COAL HANDLING

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: BAGHOUSE Cost Effectiveness:Process Information: RICHARDTON PLANT

+ Process Name: ETHANOL STORAGE TANKS + Process Type: 42.009

Pollutant Information: RICHARDTON PLANT - ETHANOL STORAGE TANKS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: INTERNAL FLOATING ROOF Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: SABINA PETROCHEMICALS LLC

RBLC ID: TX-0575 + Corporate/Company Name: SABINA PETROCHEMICALS LLC + Facility Name: SABINA PETROCHEMICALS LLC Facility County: JEFFERSON Facility State: TX Facility ZIP Code: + SIC Code: 2869 NAICS Code: 325199 Permit Issuance Date: 08/20/2010 ACT

Process Information: SABINA PETROCHEMICALS LLC

+ Process Name: HIGH AND LOW PRESSURE FLARES + Process Type: 19.310

Pollutant Information: SABINA PETROCHEMICALS LLC - HIGH AND LOW PRESSURE FLARES

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method+ Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: FLARE Cost Effectiveness:

Process Information: SABINA PETROCHEMICALS LLC

+ Process Name: ALKFUG, BDEFUG, AND UTILFUG + Process Type: 64.002

Pollutant Information: SABINA PETROCHEMICALS LLC - ALKFUG, BDEFUG, AND UTILFUG

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: THE FACILITY UTILIZES THE LOWEST ACHEIVABLE EMISSION RATE (LAER) LDAR (LEAK DETECTION AND REPAIR) PROGRAM. Cost Effectiveness:

Process Information: SABINA PETROCHEMICALS LLC

+ Process Name: STORMWATER TANK + Process Type: 64.006

Pollutant Information: SABINA PETROCHEMICALS LLC - STORMWATER TANK

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: EXTERNAL FLOATING ROOF Cost Effectiveness:

Process Information: SABINA PETROCHEMICALS LLC

+ Process Name: BOILER + Process Type: 13.310Pollutant Information: SABINA PETROCHEMICALS LLC - BOILER

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: LOW NOX BURNERS AND SCR Cost Effectiveness:

Process Information: SABINA PETROCHEMICALS LLC

+ Process Name: COOLING TOWER + Process Type: 50.007

Pollutant Information: SABINA PETROCHEMICALS LLC - COOLING TOWER

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: THE COOLING TOWER, EPN CT, HAS A NON-CONTACT DESIGN, UTILIZES MONTHLY MONITORING OF VOC IN WATER PER APPENDIX P OR APPROVED EQUIVALENT AND IDENTIFIED LEAKS ARE REPAIRED AS SOON AS POSSIBLE, BUT BEFORE NEXT SCHEDULED SHUTDOWN. Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: SALT CREEK GAS PLANT

RBLC ID: TX-0465 + Corporate/Company Name: EXXON MOBIL CORPORATION + Facility Name: SALT CREEK GAS PLANT Facility County: KENT Facility State: TX Facility ZIP Code: + SIC Code: 1321 NAICS Code: 221210 Permit Issuance Date: 01/31/2003 ACTProcess Information: SALT CREEK GAS PLANT

+ Process Name: COOPER-BESSEMER ENGINE + Process Type: 17.190

Pollutant Information: SALT CREEK GAS PLANT - COOPER-BESSEMER ENGINE

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT+ Process Name: CLARK ENGINE (2) + Process Type: 17.190

Pollutant Information: SALT CREEK GAS PLANT - CLARK ENGINE (2)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT

+ Process Name: INGERSOLL-RAND ENGINE + Process Type: 17.290Pollutant Information: SALT CREEK GAS PLANT - INGERSOLL-RAND ENGINE

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT

+ Process Name: HOT OIL HEATER + Process Type: 19.600

Pollutant Information: SALT CREEK GAS PLANT - HOT OIL HEATER

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT

+ Process Name: INGERSOLL-RAND ENGINE 1330 HP + Process Type: 17.190

Pollutant Information: SALT CREEK GAS PLANT - INGERSOLL-RAND ENGINE 1330 HP

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method+ Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT

+ Process Name: GLYCOL REBOILER + Process Type: 19.600

Pollutant Information: SALT CREEK GAS PLANT - GLYCOL REBOILER

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT

+ Process Name: GLYCOL VENT + Process Type: 64.003

Pollutant Information: SALT CREEK GAS PLANT - GLYCOL VENT

+ Pollutant Name Benzene Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds , Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method+ Control Method Description: Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT

+ Process Name: COOPER-BESSEMER ENGINE 3105 HP + Process Type: 17.190

Pollutant Information: SALT CREEK GAS PLANT - COOPER-BESSEMER ENGINE 3105 HP

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LEAN COMBUSTION Cost Effectiveness:Process Information: SALT CREEK GAS PLANT

+ Process Name: HOT OIL HEATER + Process Type: 19.600

Pollutant Information: SALT CREEK GAS PLANT - HOT OIL HEATER

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT

+ Process Name: FLARES (2)+ Process Type: 19.310

Pollutant Information: SALT CREEK GAS PLANT - FLARES (2)

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT

+ Process Name: HP TEG FIREBOX + Process Type: 19.600Pollutant Information: SALT CREEK GAS PLANT - HP TEG FIREBOX

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT

+ Process Name: FUGITIVES (4) + Process Type: 64.002

Pollutant Information: SALT CREEK GAS PLANT - FUGITIVES (4)

+ Pollutant Name Volatile Organic Compounds (VOC)Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: SALT CREEK GAS PLANT

+ Process Name: FUGITIVES + Process Type: 64.002

Pollutant Information: SALT CREEK GAS PLANT - FUGITIVES

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: SPI POLYOLS, INC.

RBLC ID: DE-0017 + Corporate/Company Name: SPI POLYOLS, INC. + Facility Name: SPI POLYOLS, INC. Facility County: NEW CASTLE COUNTYFacility State: DE Facility ZIP Code: 197202780 + SIC Code: 2869 NAICS Code: 325199 Permit Issuance Date: 10/26/2001 ACT

Process Information: SPI POLYOLS, INC.

+ Process Name: BATCH TREATMENT OF SPENT NICKLE CATALYST (CATALYST REGENERATION) + Process Type: 64.001

Pollutant Information: SPI POLYOLS, INC. - BATCH TREATMENT OF SPENT NICKLE CATALYST (CATALYST REGENERATION)

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: WATER SCRUBBER ON BATCH EXHAUST; LIMIT ON NITRIC ACID (HNO3) FEED RATE AND METHOD; LIMIT ON PROCESS TEMPERATURE. Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: ST. CHARLES REFINERY

RBLC ID: LA-0213 + Corporate/Company Name: VALERO REFINING - NEW ORLEANS, LLC + Facility Name: ST. CHARLES REFINERY Facility County: ST. CHARLES Facility State: LA Facility ZIP Code: 70079 + SIC Code: 2911 NAICS Code: 324110 Permit Issuance Date: 11/17/2009 ACT

Process Information: ST. CHARLES REFINERY

+ Process Name: BOILER 401-E (2004-10) + Process Type: 11.390Pollutant Information: ST. CHARLES REFINERY - BOILER 401-E (2004-10)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: HEATERS/REBOILERS + Process Type: 13.390

Pollutant Information: ST. CHARLES REFINERY - HEATERS/REBOILERS

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: USE OF PIPELINE QUALITY NATURAL GAS OR REFINERY FUEL GASES WITH AN H2S CONCENTRATION LESS THAN 100 PPMV (ANNUAL AVERAGE). Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: ULTRA LOW NOX BURNERS Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: HEATERS (2008-1 - 2008-9) + Process Type: 12.390

Pollutant Information: ST. CHARLES REFINERY - HEATERS (2008-1 - 2008-9)

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: USE OF PIPELINE QUALITY NATURAL GAS OR PROCESS FUEL GASES WITH AN H2S CONCENTRATION LESS THAN 10 PPMV (ANNUAL AVERAGE). Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: ULTRA LOW NOX BURNERS Cost Effectiveness: 172 ($/ton)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 60 SUBPARTS NNN AND RRR Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 60 SUBPARTS NNN AND RRR Cost Effectiveness:

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 60 SUBPARTS NNN AND RRR Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: MVR THERMAL OXIDIZER NO. 2 (2008-38) + Process Type: 50.008

Pollutant Information: ST. CHARLES REFINERY - MVR THERMAL OXIDIZER NO. 2 (2008-38)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: USE OF PIPELINE QUALITY NATURAL GAS OR PROCESS FUEL GASES WITH AN H2S CONCENTRATION LESS THAN 10 PPMV (ANNUAL AVERAGE). Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method+ Control Method Description: COMPLY WITH 40 CFR 61 SUBPART BB Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: HEATERS (94-21 & 94-29) + Process Type: 13.390

Pollutant Information: ST. CHARLES REFINERY - HEATERS (94-21 & 94-29)

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: USE OF PIPELINE QUALITY NATURAL GAS OR REFINERY FUEL GASES WITH AN H2S CONCENTRATION LESS THAN 100 PPMV (ANNUAL AVERAGE). Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:Process Information: ST. CHARLES REFINERY

+ Process Name: CPF HEATER H-39-03 & H-39-02 (94-28 & 94-30) + Process Type: 13.390

Pollutant Information: ST. CHARLES REFINERY - CPF HEATER H-39-03 & H-39-02 (94-28 & 94-30)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: USE OF PIPELINE QUALITY NATURAL GAS OR REFINERY FUEL GASES WITH AN H2S CONCENTRATION LESS THAN 100 PPMV (ANNUAL AVERAGE). Cost Effectiveness:Process Information: ST. CHARLES REFINERY

+ Process Name: BOILERS (94-43 & 94-45) + Process Type: 11.390

Pollutant Information: ST. CHARLES REFINERY - BOILERS (94-43 & 94-45)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: CLEAN FUELS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: USE OF PIPELINE QUALITY NATURAL GAS OR REFINERY FUEL GASES WITH AN H2S CONCENTRATION LESS THAN 100 PPMV (ANNUAL AVERAGE). Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: FUEL CHOICE, OPERATING TECHNIQUES, AND LOW NOX BURNERS Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD OPERATING PRACTICES Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ST. CHARLES REFINERY+ Process Name: FLARE 1-5 (15-77, 12-81, 2004-5A, 2004-5B & 2005-38) + Process Type: 50.008

Pollutant Information: ST. CHARLES REFINERY - FLARE 1-5 (15-77, 12-81, 2004-5A, 2004-5B & 2005-38)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 63 SUBPART A Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: USE OF PIPELINE QUALITY NATURAL GAS OR REFINERY FUEL GASES WITH AN H2S CONCENTRATION LESS THAN 100 PPMV (ANNUAL AVERAGE) AS FUELS AT FLARE TIP. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 63 SUBPART A Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 63 SUBPART A Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 63 SUBPART A Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method+ Control Method Description: COMPLY WITH 40 CFR 63 SUBPART A Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: COOLING TOWERS (13-81, 2004-6, 2005-42, 2005-43, 2008-35) + Process Type: 99.009

Pollutant Information: ST. CHARLES REFINERY - COOLING TOWERS (13-81, 2004-6, 2005-42, 2005-43, 2008-35)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: DRIFT ELIMINATORS Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: MONITORING PROCESS SIDE OF THE HEAT EXCHANGERS FOR LEAKS 2008-35: VOC MONITORING PROGRAM MEETS 40 CFR 63 SUBPART F Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: SRU THERMAL OXIDIZERS (99-3, 99-4, 2005-39, 2007-4) + Process Type: 50.006

Pollutant Information: ST. CHARLES REFINERY - SRU THERMAL OXIDIZERS (99-3, 99-4, 2005-39, 2007-4)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method PROPER EQUIPMENT DESIGN AND OPERATION, GOOD+ Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: CONTROL DEVICE - COMPLY WITH 40 CFR 60 SUBPART J Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: FCCU REGENERATOR (16-77) + Process Type: 50.003

Pollutant Information: ST. CHARLES REFINERY - FCCU REGENERATOR (16-77)+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Sulfur Oxides (SOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: A + Control Method Description: WET SCRUBBER Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FULL BURN DESIGN Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FULL BURN Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: PETROLEUM PRODUCT LOADING DOCKS (94-9) + Process Type: 50.004Pollutant Information: ST. CHARLES REFINERY - PETROLEUM PRODUCT LOADING DOCKS (94-9)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: COMPLY WITH LAC 33:III.2108 FOR LOADING MATERIALS WITH VAPOR PRESSURE > 1.5 PSIA Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: COKER NOS. 1 & 2 STEAM VENT (2005-58 & 2005-59) + Process Type: 50.999

Pollutant Information: ST. CHARLES REFINERY - COKER NOS. 1 & 2 STEAM VENT (2005-58 & 2005-59)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: COKE HANDLING (5-83) + Process Type: 50.999

Pollutant Information: ST. CHARLES REFINERY - COKE HANDLING (5-83)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: KEEP COKE WET WHILE STORING AND TRANSPORTING Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: FUGITIVE EMISSIONS + Process Type: 50.007Pollutant Information: ST. CHARLES REFINERY - FUGITIVE EMISSIONS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: REFINERY (90-0): LA REFINERY MACT LDAR PROGRAM; ARU (2008-39): MONITORING ACCORDING TO 40 CFR 63 SUBPART H; ARU LOADING (2008-37): MONITORING ACCORDING TO 40 CFR 61 SUBPART V Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PAVING ROADS OR WETTING UNPAVED ROADS AS NECESSARY Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: MVR THERMAL OXIDIZER NO. 1 (94-8) + Process Type: 50.008

Pollutant Information: ST. CHARLES REFINERY - MVR THERMAL OXIDIZER NO. 1 (94-8)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: USE OF GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: USE OF PIPELINE QUALITY NATURAL GAS OR REFINERY FUEL GASES WITH AN H2S CONCENTRATION LESS THAN 100 PPMV (ANNUAL AVERAGE). Cost Effectiveness:+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER EQUIPMENT DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: COMPLY WITH LAC 33:III.2108 AND 40 CFR 63 SUBPART CC Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: WASTEWATER COLLECTION & TREATMENT: ARU + Process Type: 64.006

Pollutant Information: ST. CHARLES REFINERY - WASTEWATER COLLECTION & TREATMENT: ARU

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 63 SUBPARTS F & G Cost Effectiveness:Process Information: ST. CHARLES REFINERY

+ Process Name: TANKS - FOR BENZENE, XYLENE, SULFOLANE, PAREX, INTERMEDIATE + Process Type: 42.009

Pollutant Information: ST. CHARLES REFINERY - TANKS - FOR BENZENE, XYLENE, SULFOLANE, PAREX, INTERMEDIATE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: EQUIPPED WITH INTERNAL FLOATING ROOFS FOLLOWED BY THERMAL OXIDIZERS Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: TANKS - FOR LIGHT MATERIALS, SOUR WATER, NAPHTHA, RAFFINATE + Process Type: 42.006

Pollutant Information: ST. CHARLES REFINERY - TANKS - FOR LIGHT MATERIALS, SOUR WATER, NAPHTHA, RAFFINATE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: EQUIP WITH FLOATING ROOFS (IFR OR EFR) & COMPLY WITH 40 CFR 60 SUBPART KB OR 40 CFR 63 SUBPART CC Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: ARU FLARE (2008-36) + Process Type: 50.008

Pollutant Information: ST. CHARLES REFINERY - ARU FLARE (2008-36)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 60 SUBPART A Cost Effectiveness:+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 60 SUBPART A Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 60 SUBPART A Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 60 SUBPART A Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FUELED BY NATURAL GAS OR PROCESS FUEL GAS WITH H2S Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: BOILERS (2008-10, 2008-11, 2008-40) + Process Type: 11.390

Pollutant Information: ST. CHARLES REFINERY - BOILERS (2008-10, 2008-11, 2008-40)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 60 SUBPARTS NNN AND RRR Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P+ Control Method Description: FUELED BY NATURAL GAS AND/OR REFINERY FUEL GAS WITH H2S Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: ULTRA LOW NOX BURNERS Cost Effectiveness: 43 ($/ton)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 60 SUBPARTS NNN AND RRR Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 60 SUBPARTS NNN AND RRR Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: DHT HEATERS (4-81, 5-81) + Process Type: 13.390

Pollutant Information: ST. CHARLES REFINERY - DHT HEATERS (4-81, 5-81)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FUELED BY NATURAL GAS OR REFINERY FUEL GAS WITH H2S Cost Effectiveness:+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: LOW NOX BURNERS Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PROPER DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: HEATER F-72-703 (7-81) + Process Type: 11.390

Pollutant Information: ST. CHARLES REFINERY - HEATER F-72-703 (7-81)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FUELED BY NATURAL GAS OR REFINERY FUEL GAS WITH H2S Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P+ Control Method Description: LOW NOX BURNERS Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PROPER DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: THERMAL OXIDIZERS (2008-32, 2008-33, 2008-34) + Process Type: 50.008

Pollutant Information: ST. CHARLES REFINERY - THERMAL OXIDIZERS (2008-32, 2008-33, 2008-34)

+ Pollutant Name Particulate matter, total < 10 μ (TPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES, AND GASEOUS FUELS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FUELED BY NATURAL GAS AND PROCESS FUEL GAS WITH H2S Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: PROPER DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: PROPER DESIGN AND OPERATION, GOOD COMBUSTION PRACTICES Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: TANKS - FOR HEAVY MATERIALS + Process Type: 42.005

Pollutant Information: ST. CHARLES REFINERY - TANKS - FOR HEAVY MATERIALS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: EQUIPPED WITH FIXED ROOF AND COMPLY WITH 40 CFR 63 SUBPART CC Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: TANKS - FOR SPENT CAUSTIC + Process Type: 62.020

Pollutant Information: ST. CHARLES REFINERY - TANKS - FOR SPENT CAUSTIC

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: FIXED ROOF AND SUBMERGED FILL LINES (LAC 33:III.2103) Cost Effectiveness:

Process Information: ST. CHARLES REFINERY+ Process Name: LOADINGS - REFINERY + Process Type: 50.004

Pollutant Information: ST. CHARLES REFINERY - LOADINGS - REFINERY

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: TRUCK/RAILCAR LOADING: COMPLY WITH 40 CFR 63 SUBPART CC Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: PROPER DESIGN AND OPERATION Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: LOADINGS - AROMATIC RECOVERY UNIT + Process Type: 64.005

Pollutant Information: ST. CHARLES REFINERY - LOADINGS - AROMATIC RECOVERY UNIT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: RAILCAR LOADING: COMPLY WITH 40 CFR 63 SUBPART G MARINE LOADING: COMPLY WITH 40 CFR 61 SUBPART BB Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: PROCESS VENTS - REFINERY (CCEX) + Process Type: 50.999

Pollutant Information: ST. CHARLES REFINERY - PROCESS VENTS - REFINERY (CCEX)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method ROUTE TO THE FUEL GAS SYSTEMS OR FLARES OR COMPLY+ Control Method Description: ROUTE TO THE FUEL GAS SYSTEMS OR FLARES OR COMPLY WITH 40 CFR 63 SUBPART CC Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: ROUTE TO FUEL GAS SYSTEMS OR FLARES Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: VENT GAS WASH TOWER (99-8) + Process Type: 50.006

Pollutant Information: ST. CHARLES REFINERY - VENT GAS WASH TOWER (99-8)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: WASTEWATER COLLECTION & TREATMENT: REFINERY + Process Type: 50.009

Pollutant Information: ST. CHARLES REFINERY - WASTEWATER COLLECTION & TREATMENT: REFINERY

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: WW (EQT0255): COMPLY WITH LA REFINERY MACT WWTU (EQT0359): COMPLY WITH 40 CFR 61 SUBPART FF CRUIDS (EQT369): COMPLY WITH 40 CFR 63 SUBPARTS F & G Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: CRU: CHLOROSORB VENT AND DUST COLLECTOR + Process Type: 50.003Pollutant Information: ST. CHARLES REFINERY - CRU: CHLOROSORB VENT AND DUST COLLECTOR

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: COMPLY WITH 40 CFR 63 SUBPART UUU Cost Effectiveness:

Process Information: ST. CHARLES REFINERY

+ Process Name: STARTUPS/SHUTDOWNS - SRU + Process Type: 50.006

Pollutant Information: ST. CHARLES REFINERY - STARTUPS/SHUTDOWNS - SRU

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: FOLLOW WRITTEN SOP, MINIMIZE DURATION AND FREQUENCY, PROPERLY DOCUMENT ALL SU/SD Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: SUNOCO, INC

RBLC ID: OH-0284 + Corporate/Company Name: SUNOCO, INC + Facility Name: SUNOCO, INC Facility County: SCIOTO Facility State: OH Facility ZIP Code: 45629 + SIC Code: 2869 NAICS Code: 325110 Permit Issuance Date: 10/07/2004 ACT

Process Information: SUNOCO, INC+ Process Name: CUMENE OXIDATION PROCESS UNIT + Process Type: 64.003

Pollutant Information: SUNOCO, INC - CUMENE OXIDATION PROCESS UNIT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CONDENSER, THERMAL OXIDIZER, AND REGENERATIVE THERMAL OXIDIZER Cost Effectiveness:

Process Information: SUNOCO, INC

+ Process Name: THERMAL OXIDIZER FOR CUMENE OXIDATION AND PHENOL II PROCESS + Process Type: 64.003

Pollutant Information: SUNOCO, INC - THERMAL OXIDIZER FOR CUMENE OXIDATION AND PHENOL II PROCESS

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: THERMAL OXIDIZER IS ONE OF THE CONTROL DEVICES FOR THE CUMENE OXIDATION AND PHENOL II PROCESS Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: THERMAL OXIDIZER IS ONE OF THE CONTROL DEVICES FOR THE CUMENE OXIDATION AND PHENOL II PROCESS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: THERMAL OXIDIZER IS ONE OF THE CONTROL DEVICES FOR THE CUMENE OXIDATION AND PHENOL II PROCESS Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N+ Control Method Description: THERMAL OXIDIZER IS ONE OF THE CONTROL DEVICES FOR THE CUMENE OXIDATION AND PHENOL II PROCESS Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: THERMAL OXIDIZER IS ONE OF THE CONTROL DEVICES FOR THE CUMENE OXIDATION AND PHENOL II PROCESS Cost Effectiveness:

Process Information: SUNOCO, INC

+ Process Name: REGEN THERMAL OXIDIZER FOR CUMENE OXIDATION & PHENOL II PROCESS + Process Type: 64.003

Pollutant Information: SUNOCO, INC - REGEN THERMAL OXIDIZER FOR CUMENE OXIDATION & PHENOL II PROCESS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: REGENERATIVE THERMAL OXIDIZER EMISSIONS Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: REGENERATIVE THERMAL OXIDIZER EMISSIONS Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: REGENERATIVE THERMAL OXIDIZER EMISSIONS Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: REGENERATIVE THERMAL OXIDIZER EMISSIONSCost Effectiveness:

Process Information: SUNOCO, INC

+ Process Name: PHENOL II PROCESS + Process Type: 64.003

Pollutant Information: SUNOCO, INC - PHENOL II PROCESS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CONDENSER, THERMAL OXIDIZER, AND REGENERATIVE THERMAL OXIDIZER Cost Effectiveness:

Process Information: SUNOCO, INC

+ Process Name: PRIMARY CUMENE STRIPPER AND JET CONDENSER SYSTEM + Process Type: 64.003

Pollutant Information: SUNOCO, INC - PRIMARY CUMENE STRIPPER AND JET CONDENSER SYSTEM

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CONDENSER Cost Effectiveness:

Process Information: SUNOCO, INC

+ Process Name: DISTILLATION OF ALPHAMETHYLSTYRENE + Process Type: 64.003

Pollutant Information: SUNOCO, INC - DISTILLATION OF ALPHAMETHYLSTYRENE

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: CONDENSERS Cost Effectiveness:Previous Page

NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

RBLC ID: FL-0322 + Corporate/Company Name: SOUTHEAST RENEWABLE FUELS (SRF), LLC + Facility Name: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY Facility County: HENDRY COUNTY Facility State: FL Facility ZIP Code: 33440 + SIC Code: 2869 NAICS Code: 325193 Permit Issuance Date: 12/23/2010 ACT

Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Biomass Material Handling and Preparation + Process Type: 99.999

Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Biomass Material Handling and Preparation

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: B + Control Method Description: SRF shall utilize reasonable precautions for controlling fugitive PM emissions from this emission unit. These include but are not limited to: •Enclosing material drop points, transfer points, shredders and screens wherever practical; •Contouring storage piles to minimize wind erosion; •Utilizing water sprays on storage piles as needed; •Paving all main plant roads; •Watering of gravel surfaces as needed to control dust; and •Weekly sweeping and watering of paved surfaces as needed to remove dust. The permittee shall also comply with additional precautions listed in Appendix BMP- Best Management Practices of permit PSD-FL-412. Cost Effectiveness:

Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Cogeneration Biomass Boiler + Process Type: 12.120Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Cogeneration Biomass Boiler

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: Controls: Good combustion practices (GCP) leading to the efficient combustion of biomass in the boiler, including an over-fired air (OFA) system, to minimize formation of PM, nitrogen oxides (NOX), Selective Non-Catalytic Reduction (SNCR), Selective Catalytic Reduction (SCR) or a combination of the two with urea or anhydrous ammonia (NH3) injection to destroy NOX. Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: B + Control Method Description: Dry sorbent injection system. A wet scrubber to remove hydrogen sulfide from the biogas prior to combustion in the boiler to minimize SO2 emissions. Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: Good combustion practices, including an over-fired air system. If necessary, the permittee shall design and build the project to facilitate future installation of an ox-cat system to control in conjunction with good combustion practices (GCP), emissions of NOX, CO, VOC and organic HAP emissions to the permitted standards. Cost Effectiveness:

+ Pollutant Name Sulfuric Acid (mist, vapors, etc) Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: A dry sorbent injection system (DSIS) utilizing lime, trona, or sodium bicarbonate to control SO2, sulfuric acid mist (SAM) and acid gas HAP; a wet scrubber to remove hydrogen sulfide (H2S) from the biogas prior to combustion in the boiler to minimize SO2 emissions. Cost Effectiveness:

+ Pollutant Name Hydrochloric Acid Pollutant Group(s): ( Acid Gasses/Mist , Hazardous Air Pollutants (HAP) , InOrganic Compounds , Particulate Matter (PM) ) + Control Method Code: B + Control Method A dry sorbent injection system (DSIS) utilizing lime, trona, or sodium+ Control Method Description: A dry sorbent injection system (DSIS) utilizing lime, trona, or sodium bicarbonate to control SO2, sulfuric acid mist (SAM) and acid gas HAP. Cost Effectiveness:

+ Pollutant Name Hazardous Air Pollutants (HAP) Pollutant Group(s): ( Hazardous Air Pollutants (HAP) ) + Control Method Code: B + Control Method Description: Use of inherently clean fossil fuels fired in low-NOX burners (LNB) for boiler startup, shutdown and flame (bed) stabilization to minimize formation of PM, NOX, sulfur dioxide (SO2) and HAP; a dry sorbent injection system (DSIS) utilizing lime, trona, or sodium bicarbonate to control SO2, sulfuric acid mist (SAM) and acid gas HAP; a wet scrubber to remove hydrogen sulfide (H2S) from the biogas prior to combustion in the boiler to minimize SO2 emissions. Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: A wet sand separator (cyclone) and a electrostatic precipitator (ESP) or fabric filter baghouse to further control PM and VE. Cost Effectiveness:

+ Pollutant Name Hydrogen Fluoride Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: Good combustion practices (GCP) leading to the efficient combustion of biomass in the boiler, including an over-fired air (OFA) system, to minimize formation of PM, nitrogen oxides (NOX), carbon monoxide (CO), volatile organic compounds (VOC) and HAP. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: B + Control Method Description: ESP OR BAGHOUSE Cost Effectiveness:Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Cooling Water Tower + Process Type: 99.009

Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Cooling Water Tower

+ Pollutant Name Total Suspended Particulates Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: Weekly Testing and Recording Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: Cost Effectiveness:

Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Ethanol Production Process + Process Type: 70.120

Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Ethanol Production Process

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: Wet scrubbers Cost Effectiveness:

Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Bioreactors and Biogas Flare + Process Type: 19.390

Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Bioreactors and Biogas Flare+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: Wet scrubber Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: B + Control Method Description: Flare Cost Effectiveness:

Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Storage Tanks + Process Type: 64.004

Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Storage Tanks

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: Emissions of VOC from the Blending and Storage tanks will be controlled by the proper construction of the tanks per 40 CFR 60.110b(a)(2) which requires internal floating roofs in the tanks or the equivalent. Cost Effectiveness:

Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Truck Rack Product and Flare + Process Type: 19.390

Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Truck Rack Product and Flare

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: B + Control Method Flare. One flare system with a continuous pilot and combustion chambers+ Control Method Description: Flare. One flare system with a continuous pilot and combustion chambers to destroy displaced vapors during truck loadout. The flare shall be operated with a flame present at all times. The presence of a flare pilot flame shall be monitored using a thermocouple or any other equivalent device to detect the presence of a flame. Cost Effectiveness:

Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Miscellaneous Storage Silos + Process Type: 99.999

Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Miscellaneous Storage Silos

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: Baghouse. Cost Effectiveness:

+ Pollutant Name Visible Emissions (VE) Pollutant Group(s): + Control Method Code: B + Control Method Description: Baghouse Cost Effectiveness:

Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Emergency Generators, Two 2682 HP EA + Process Type: 17.110

Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Emergency Generators, Two 2682 HP EA

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Emergency Diesel Fire Pump, One 600 HP + Process Type: 17.210

Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Emergency Diesel Fire Pump, One 600 HP

+ Pollutant Name Nitrogen Dioxide (NO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate matter, total (TPM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY

+ Process Name: Fugitive VOC Emission Leaks (facility-wide) + Process Type: 64.002Pollutant Information: SWEET SORGHUM-TO-ETHANOL ADVANCED BIOREFINERY - Fugitive VOC Emission Leaks (facility-wide)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: The permittee shall demonstrate compliance with the requirements of §§60.482–1a through 60.482–10a or §60.480a(e) for all equipment subject to NSPS Subpart VVa within 180 days of initial startup of the SRF. Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: SYNTHESIS GAS UNIT

RBLC ID: TX-0380 + Corporate/Company Name: EXXON CHEMICAL AMERICAS + Facility Name: SYNTHESIS GAS UNIT Facility County: HARRIS Facility State: TX Facility ZIP Code: 77522 + SIC Code: 2869 NAICS Code: 320000 Permit Issuance Date: 06/01/2001 ACT

Process Information: SYNTHESIS GAS UNIT

+ Process Name: (2) AIR PREHEATERS 1106 & 1206, F1106SGU &F1206SGU + Process Type: 19.600

Pollutant Information: SYNTHESIS GAS UNIT - (2) AIR PREHEATERS 1106 & 1206, F1106SGU &F1206SGU

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Particulate matter, filterable < 10 μ (FPM10) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: SYNTHESIS GAS UNIT

+ Process Name: ANALYZER HOUSE VENT + Process Type: 64.003

Pollutant Information: SYNTHESIS GAS UNIT - ANALYZER HOUSE VENT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method+ Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR,AND CONTAINMENT. Cost Effectiveness:

Process Information: SYNTHESIS GAS UNIT

+ Process Name: GREY WATER TANK, TK1004 + Process Type: 64.004

Pollutant Information: SYNTHESIS GAS UNIT - GREY WATER TANK, TK1004

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

Process Information: SYNTHESIS GAS UNIT

+ Process Name: FLUSH OIL TANK, TK1011 + Process Type: 64.004

Pollutant Information: SYNTHESIS GAS UNIT - FLUSH OIL TANK, TK1011

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: COMPLY WITH ALL APPLICABLE STANDARDS OF TITLE 40 CFR PART 60, SUBPART A AND KB. Cost Effectiveness:Process Information: SYNTHESIS GAS UNIT

+ Process Name: POLYSULFIDE TANK, TK1014 + Process Type: 64.004

Pollutant Information: SYNTHESIS GAS UNIT - POLYSULFIDE TANK, TK1014

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

Process Information: SYNTHESIS GAS UNIT

+ Process Name: FILTER FEED TANK, TK1016 + Process Type: 64.004

Pollutant Information: SYNTHESIS GAS UNIT - FILTER FEED TANK, TK1016

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

Process Information: SYNTHESIS GAS UNIT

+ Process Name: FLARE, FS28 + Process Type: 19.310

Pollutant Information: SYNTHESIS GAS UNIT - FLARE, FS28

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P+ Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

+ Pollutant Name Carbonyl Sulfide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:Process Information: SYNTHESIS GAS UNIT

+ Process Name: AMMONIA STRIPPER, T1004SGU + Process Type: 64.006

Pollutant Information: SYNTHESIS GAS UNIT - AMMONIA STRIPPER, T1004SGU

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT PROCEDURES. Cost Effectiveness:

Process Information: SYNTHESIS GAS UNIT

+ Process Name: FIRST FLUSH SUMP, S1031SGU + Process Type: 64.006

Pollutant Information: SYNTHESIS GAS UNIT - FIRST FLUSH SUMP, S1031SGU

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: SYNTHESIS GAS UNIT

+ Process Name: BLACK WATER SUMP, S1040SGU + Process Type: 64.006

Pollutant Information: SYNTHESIS GAS UNIT - BLACK WATER SUMP, S1040SGU

+ Pollutant Name Hydrogen Cyanide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) , Organic Non-HAP Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Sulfuric Acid (mist, vapors, etc) Pollutant Group(s): ( InOrganic Compounds , Particulate Matter (PM) )+ Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbonyl Sulfide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

+ Pollutant Name Hexamethylene Diisocyanate Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , Organic Compounds (all) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

Process Information: SYNTHESIS GAS UNIT

+ Process Name: OIL COLLECTION SUMP + Process Type: 64.006

Pollutant Information: SYNTHESIS GAS UNIT - OIL COLLECTION SUMP

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:Process Information: SYNTHESIS GAS UNIT

+ Process Name: SYNGAS UNIT FUGITIVES, FGSGU + Process Type: 64.002

Pollutant Information: SYNTHESIS GAS UNIT - SYNGAS UNIT FUGITIVES, FGSGU

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES FOR LEAK DETECTION, ISOLATION, REPAIR, AND CONTAINMENT. Cost Effectiveness:

+ Pollutant Name Carbonyl Sulfide Pollutant Group(s): ( Hazardous Air Pollutants (HAP) , InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES OF LEAK DETECTION, ISOLATION, REPAIR AND CONTAINMENT. Cost Effectiveness:

+ Pollutant Name Ammonia (NH3) Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: FOLLOW PROCEDURES OF LEAK DETECTION, ISOLATION, REPAIR AND CONTAINMENT. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

Process Information: SYNTHESIS GAS UNIT

+ Process Name: SYNGAS DISPOSAL + Process Type: 64.999Pollutant Information: SYNTHESIS GAS UNIT - SYNGAS DISPOSAL

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: NONE INDICATED Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: A + Control Method Description: FLARE Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: UCC SEADRIFT OPERATIONS

RBLC ID: TX-0449 + Corporate/Company Name: UNION CARBIDE CORPORATION - A SUBSIDIARY OF DOW CC + Facility Name: UCC SEADRIFT OPERATIONS Facility County: CALHOUN Facility State: TX Facility ZIP Code: + SIC Code: 2869 NAICS Code: 325188 Permit Issuance Date: 04/03/2004 ACT

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: RXN AND ETHYLENE PURIFICATION FUGITIVES (8) + Process Type: 50.007

Pollutant Information: UCC SEADRIFT OPERATIONS - RXN AND ETHYLENE PURIFICATION FUGITIVES (8)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) )+ Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: ANALYZER VENTS + Process Type: 64.003

Pollutant Information: UCC SEADRIFT OPERATIONS - ANALYZER VENTS

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: SMALL FLARE + Process Type: 19.310

Pollutant Information: UCC SEADRIFT OPERATIONS - SMALL FLARE

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: MEET HEATING VALUE AND VELOCITY REQUIREMENT Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: MEET HEATING VALUE AND VELOCITY REQUIREMENT Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: MEETS HEATING VALUE AND VELOCITY REQUIREMENTCost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: CYCLE GAS COMPRESSOR OIL VENT + Process Type: 64.002

Pollutant Information: UCC SEADRIFT OPERATIONS - CYCLE GAS COMPRESSOR OIL VENT

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: CATALYST TRANSFER TANK VENT FILTER (2) + Process Type: 64.002

Pollutant Information: UCC SEADRIFT OPERATIONS - CATALYST TRANSFER TANK VENT FILTER (2)

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: G-3 REACTOR SED BED VENT + Process Type: 64.002

Pollutant Information: UCC SEADRIFT OPERATIONS - G-3 REACTOR SED BED VENT

+ Pollutant Name Particulate Matter (PM), Organic Condensables Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: CATALYST VENT FILTER + Process Type: 64.002

Pollutant Information: UCC SEADRIFT OPERATIONS - CATALYST VENT FILTER

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: LARGE FLARE + Process Type: 19.310

Pollutant Information: UCC SEADRIFT OPERATIONS - LARGE FLARE

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. Cost Effectiveness:Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: LARGE FLARE START-UP, SHUTDOWN, MAINTENANCE + Process Type: 19.310

Pollutant Information: UCC SEADRIFT OPERATIONS - LARGE FLARE START-UP, SHUTDOWN, MAINTENANCE

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD PRACTICES DURING THESE EVENTS Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD PRACTICES DURING THESE EVENTS Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: FLARE BEFOER THE RECYCLE COMPRESSOR PROJECTS IS COMPLETE + Process Type: 19.310

Pollutant Information: UCC SEADRIFT OPERATIONS - FLARE BEFOER THE RECYCLE COMPRESSOR PROJECTS IS COMPLETE

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: FLARE AFTER THE RECYCLE COMPRESSOR PROJECTS IS COMPLETE + Process Type: 19.310

Pollutant Information: UCC SEADRIFT OPERATIONS - FLARE AFTER THE RECYCLE COMPRESSOR PROJECTS IS COMPLETE

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds )+ Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: FLARE NATURAL GAS COMBUSTION (6) + Process Type: 19.310

Pollutant Information: UCC SEADRIFT OPERATIONS - FLARE NATURAL GAS COMBUSTION (6)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: A + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERSCost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: B + Control Method Description: MEETS HEATING VALUES AND VELOCITY REQ. AND BTU ANALYZERS Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: STARTUP, SHUTDOWN, MAINTENANCE BEFORE THE RECYCLE PROJECT IS COMPLETE (5) + Process Type: 19.310

Pollutant Information: UCC SEADRIFT OPERATIONS - STARTUP, SHUTDOWN, MAINTENANCE BEFORE THE RECYCLE PROJECT IS COMPLETE (5)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:+ Pollutant Name Sulfur Dioxide (SO2) Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: STARTUP, SHUTDOWN, MAINTENANCE AFTER THE RECYCLE PROJECT IS COMPLETE (5) + Process Type: 19.310

Pollutant Information: UCC SEADRIFT OPERATIONS - STARTUP, SHUTDOWN, MAINTENANCE AFTER THE RECYCLE PROJECT IS COMPLETE (5)

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:

+ Pollutant Name Hydrogen Sulfide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:

+ Pollutant Name Sulfur Dioxide (SO2)Pollutant Group(s): ( InOrganic Compounds , Oxides of Sulfur (SOx) ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: GOOD PRACTICES Cost Effectiveness:

Process Information: UCC SEADRIFT OPERATIONS

+ Process Name: AREA FUGITIVES (4) + Process Type: 64.002

Pollutant Information: UCC SEADRIFT OPERATIONS - AREA FUGITIVES (4)

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: Cost Effectiveness:

Previous Page NOTE: Draft determinations are marked with a " * " beside the RBLC ID. Required fields are denoted by "+".

Report Date: 10/06/2011            Control Technology Determinations (Freeform) Facility Information: UWGP - FUEL GRADE ETHANOL PLANT

RBLC ID: WI-0204 + Corporate/Company Name: UNITED WISCONSIN GRAIN PRODUCERS + Facility Name: UWGP - FUEL GRADE ETHANOL PLANT Facility County: COLUMBIA Facility State: WI Facility ZIP Code: 53935 + SIC Code: 2869 NAICS Code: 325193 Permit Issuance Date: 08/14/2003 ACTProcess Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: BOILER /OXIDIZER ( DRYER / DISTILLATION), P10 + Process Type: 12.310

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - BOILER /OXIDIZER ( DRYER / DISTILLATION), P10

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: PROCESS IS THE CONTROL FOR OTHER SOURCES LISTED IN PROCESS ENTRY. Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Nitrogen Oxides (NOx) Pollutant Group(s): ( InOrganic Compounds , Oxides of Nitrogen (NOx) , Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: BOILER / BURNER DESIGN Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: BYPASS FLARE, BIOMETHANATOR - P11 + Process Type: 19.320

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - BYPASS FLARE, BIOMETHANATOR - P11+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: OPERATION LIMIT: NO MORE THAN 5040 H/YR Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Carbon Monoxide Pollutant Group(s): ( InOrganic Compounds ) + Control Method Code: P + Control Method Description: OPERATION LIMIT: NO MORE THAN 5040 H/YR Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: GRAIN RECEIVING / TRANSPORT / STORAGE, P20 + Process Type: 70.290

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - GRAIN RECEIVING / TRANSPORT / STORAGE, P20

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: ENCLOSURE; BAGHOUSE (10:1 A/C); FUGITIVE DUST CONTROL Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: CORN MILLING / MILLED CORN TRANSPORT, P30 + Process Type: 70.290

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - CORN MILLING / MILLED CORN TRANSPORT, P30

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) )+ Control Method Code: A + Control Method Description: ENCLOSURE; BAGHOUSE (10:1 A/C) Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: FERMENTATION PROCESS, P40 + Process Type: 70.120

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - FERMENTATION PROCESS, P40

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: WET SCRUBBER (PACKED TOWER); WATER RECYCLED TO PROCESS Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: LOADING RACK WITH FLARE, P50 + Process Type: 19.310

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - LOADING RACK WITH FLARE, P50

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: A + Control Method Description: FLARE / VAPOR COLLECTION Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: LARGE STORAGE TANKS, T61, T62, T63, T64, T65 + Process Type: 42.009

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - LARGE STORAGE TANKS, T61, T62, T63, T64, T65

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) )+ Control Method Code: P + Control Method Description: INTERNAL FLOATING ROOF (NSPS) STORAGE TANKS, GOOD OPERATING PRACTICE Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: STORAGE TANK, 2000 GAL, CORROSION INHIBITOR, T66 + Process Type: 42.009

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - STORAGE TANK, 2000 GAL, CORROSION INHIBITOR, T66

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 2000 GAL. FIXED ROOF TANK, PRESSURE/VACUUM CONSERVATION VENT, SUBMERGED FILL PIPE. (NSPS BUT ONLY RECORDKEEPING) Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: DDGS COOLER / TRANSPORT, P70 + Process Type: 70.120

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - DDGS COOLER / TRANSPORT, P70

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: N + Control Method Description: Cost Effectiveness:

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method Description: CYCLONE WITH INTEGRATED BAGHOUSE (10:1 A/C); EST. 97% + EFF. COLLECTION. Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT+ Process Name: COOLING TOWERS, P80 + Process Type: 99.009

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - COOLING TOWERS, P80

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: 0.005% MAX. DRIFT RATE; 2000 PPM SOLIDS; MAX FLOW OF 22,000 GPM Cost Effectiveness:

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: 0.005% MAX. DRIFT RATE; 124 PPM VOCS; MAX FLOW OF 22,000 GPM Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: FUGITIVE VOC, FROM EQUIPMENT, F01 + Process Type: 64.002

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - FUGITIVE VOC, FROM EQUIPMENT, F01

+ Pollutant Name Volatile Organic Compounds (VOC) Pollutant Group(s): ( Volatile Organic Compounds (VOC) ) + Control Method Code: P + Control Method Description: SOCMI LEAK DETECTION AND REPAIR Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: DDGS LOADOUT, P90 + Process Type: 70.120

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - DDGS LOADOUT, P90

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: A + Control Method+ Control Method Description: ENCLOSURE, BAGHOUSE (10:1 A/C); FUGITIVE DUST CONTROL Cost Effectiveness:

Process Information: UWGP - FUEL GRADE ETHANOL PLANT

+ Process Name: FUGITIVE DUST, F02 + Process Type: 99.999

Pollutant Information: UWGP - FUEL GRADE ETHANOL PLANT - FUGITIVE DUST, F02

+ Pollutant Name Particulate Matter (PM) Pollutant Group(s): ( Particulate Matter (PM) ) + Control Method Code: P + Control Method Description: FUGITIVE DUST CONTROL (PAVING, CLEANING, TRANSPORTATION AND STORAGE). CLEAN AND SWEEP ROADS, WATER AND CHEMICAL CONTROLS FOR DUST, PLASTIC COVERINGS, ENCLOSURES, AND TRUCK SPEED AND WEIGHT LIMITS Cost Effectiveness:

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