# Enclosure 1

# Enclosure 2

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 1 of 14 General Information

Name of Legal Owner: Giant Cement Company
Legal Owner Address: 320-D Midland Parkway, Summerville, SC 29485
Number of Legal Owner Employees:843-851-9898
Facility Name: Giant Cement Company
Facility Address: 654 Judge Street, Harleyville, SC 29448
Mailing Address (if different from facility address): P.O. Box 218, Harleyville, SC 29448
Facility Contact Name: Edward "Sonny" Dougherty
Facility Contact Title: Manager, Environmental Compliance
Facility Contact Phone Number:803-496-2855
Facility Contact Email Address:Sonny.Dougherty@gcpv.com Number of Company Employees at the Entire Facility: 180

Please enter any other comments regarding general ownership information here:

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 2 of 14 Facility Information

Is the facility a major source for HAP? (see definition below) Major sources are any stationary source or group of stationary sources located within a contiguous area and under common control that emits or has the potential to emit considering controls, in the aggregate, 10 tons per year (TPY) or more of any hazardousairpollutant or 25 TPY or more of any combination of HAP.

Are there one or more off-site waste management or recovery operations at the facility subject to the Off-Site Waste and Recovery Operations (OSWRO) MACT (40 CFR 63, subpart DD)?

Is the facility exempt from complying with the OSWRO MACT?

What type(s) of off-site waste does the facility accept? (please include shipment method, physical form (i.e., solid, liquid, sludge), and a general description)

Approximately how many sources (facilities) does that waste come from?

What is the base year for which information is being provided? (please limit reporting years between 2006 and 2012, and provide the most current year)

For this base year, what was the amount of off-site waste received? (please specify units; e.g., gal/yr)

For this base year, what was the HAP content of the off-site waste received? (please specify units; e.g., tons)

How many hours per year are control devices bypassed to the atmosphere to perform routine maintenance?

Are any OSWRO operations scheduled to be discontinued?

Are any OSWRO operations scheduled to be added or expanded?

What is the permitting classification of your facility?

What are the operating permit IDs for the OSWRO operations at your facility?

Is your operating permit available online?

Please provide the coordinates (in decimal degrees) of your facility property boundary at each corner (node). Alternatively, please provide the minimum distance from any OSWRO emission point to the facility property boundary.

Please enter any other comments regarding the facility here:If yes, please provide date(s) that addition(s) and/or expansion(s) will begin production and explain changes: If yes, please provide dates of closure and explain changes: 2011

See "Confidential Business Information" Summary

9,097 tons in 2011 If yes, please explain:

0

Minimum distance to property boundary (approximate): Containers - 550 feet Tanks - 700 feet Equipment Leaks - 700 feet Transfer Systems - 700 feet Hazardous waste to be used for energy recovery. Hazardous liquids are shipped via tanker trucks and railcars, and may include industrial solvents, paints, and other spent materials with Btu value. Hazardous solids are typically shipped in roll-offs and dump trailers although other types of containers are allowed. Hazardous solids include contaminated personal protective equipment (PPE), rags, resinous materials, etc.

Approximately 73 in 2011.

http://www.giantcement.com/Documents/06060 SCDHEC Title V No. 0900-0002

If yes, please provide a link to or a copy of your most recent operating permit. If no, please provide a copy of your most recent operating

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 3 of 14 If no, please explain.

If no, please explain.

If "Other", please explain: Emission factors from site-specific testing at a similar facility, using EPA -453/8-93-828 "Protocol for Equipment Leak Emission Estimates."

If "Other", please explain: 

### Site-specific testing report attached.

If neither apply, please explain:

If yes, please describe the control technique(s):



### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP:

Pumps 15 Compressors 0 Agitators 4 Pressure relief devices 0 Sampling connection systems 120 Open-ended valves or lines 0 Connectors 631 Instrumentation systems 9

Number of valves: 262 (included in the equipment leaks calculations referenced in Enclosure 2a). Equipment Leaks

Have you verified and/or corrected the equipment leak emissions for your OSWRO processes in Enclosure 2A?

Have you completed all control information fields for your OSWRO equipment leaks in Enclosure 2A?

What emissions calculation approach was used to estimate the equipment leak emissions?

Please enter any other comments regarding equipment leaks here: What is the number of each type of component for the equipment in OSWRO HAP service (equipment that contacts off-site material having a total HAP concentration≥ 10% by weight for 300 hours/year or more)? With which subpart do you comply for equipment leaks? Please provide documentation demonstrating the basis for the equipment leak emissions estimates.What type of documentation are you providing?

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard?

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

If no, please explain. 

### These are included with and considered part of "Equipment Leaks."

If no, please explain. 

### These are included with and considered part of "Equipment Leaks."

If "Other", please explain:

Hazardous liquids - Hard piping that is permanently or semipermanently sealed. Hazardous solids - Covers used for hazardous solids conveyor.

If "Other", please explain: 

### Hazardous liquids - See "Equipment Leaks" tab. Hazardous solids - N/A

If yes, please describe the control technique(s):



### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP:

Please enter any other comments regarding transfer systems here: Transfer Systems

Have you entered the OSWRO transfer system emissions in Enclosure 2A?

Have you completed all control information fields for your OSWRO transfer systems in Enclosure 2A?

What emissions calculation approach was used to estimate the transfer system emissions?

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard? Please provide documentation demonstrating the basis for the transfer system emissions estimates.Are you providing emissions factors or source test data?

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

If no, please explain.

### The Giant facility does not operate any oil-water or organicwater separators.

If no, please explain.

If "Other", please explain:

If "Other", please explain:

If yes, please describe the control technique(s):



### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP:

The Giant facility does not operate any oil-water or organicwater separators, and therefore, this tab is not applicable.Please enter any other comments regarding organic or oilwater separators here: Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard? Please provide documentation demonstrating the basis for the oil-water and organic-water separators emissions estimates.Are you providing emissions factors or source test data? Oil-water and organic-water separators

Have you entered the OSWRO oil-water and organic-water separators emissions in Enclosure 2A?

Have you completed all control information fields for your OSWRO oil-water and organic-water separators in Enclosure 2A?

What emissions calculation approach was used to estimate the oil-water and organic-water separators emissions?

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

If no, please explain.

If no, please explain.

If "Other", please explain:



### Please listeachOSWRO container requiring Level 1 or Level 2 control:

Container ID Container capacityContainer emissions control level implemented
Drums <55 gallons Level 1 Tanker Truck <6,000 gallons Level 1/2
Railcar <27,000 gallons Level 1/2 Rolloff/Dump Trailer<40 cubic yards Level 1



### Please enter any other comments regarding containers here:The facility does not process individual, off-site drums. On-site generated waste containerized in drums, at times, may contain off-site material. (add information for more containers as necessary) Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard?

Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP: If yes, please describe the control technique(s): 

### Containers

Have you entered the OSWRO containers emissions in Enclosure 2A?

Have you completed all control information fields for your OSWRO containers in Enclosure 2A?

What emissions calculation approach was used to estimate the containers emissions? Containers meet the requirements for level 1 or level 2. No off-site shipments received in containers requiring monitoring for "no detectable emissions" per Method 21.

See note above.

Please provide documentation demonstrating the basis for the containers emissions estimates.Are you providing emissions factors or source test data?

See note above - N/A. If "Other", please explain: 

### See note above - N/A.

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

If no, please explain. 

### The Giant facility does not operate any surface impoundments.

If no, please explain.

If "Other", please explain:

If "Other", please explain:



### The Giant facility does not operate any surface impoundments, and therefore, this tab is not applicable. Please enter any other comments regarding surface impoundments here: If yes, please describe the control technique(s):



### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP: Surface Impoundments

Have you entered the OSWRO surface impoundments emissions in Enclosure 2A?

Have you completed all control information fields for your OSWRO surface impoundments in Enclosure 2A?

What emissions calculation approach was used to estimate the surface impoundments emissions?

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard? Please provide documentation demonstrating the basis for the surface impoundments emissions estimates.Are you providing emissions factors or source test data?

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 8 of 14 If no, please explain.

If no, please explain.

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard?

The Giant facility does not operate any process vents, and therefore, this tab is not applicable. Please enter any other comments regarding process vents here: If "Other", please explain:

If yes, please describe the control technique(s):



### Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP: If "Other", please explain: Process Vent Emissions Information

Have you verified and/or corrected the process vent emissions for your OSWRO processes in Enclosure 2A?

Have you completed all control information fields for your OSWRO process vent streams in Enclosure 2A?

What emissions calculation approach was used to estimate the process vent emissions?

Please provide documentation demonstrating the basis for the process vent emissions estimates.Are you providing emissions factors or source test data? The Giant facility does not operate any process vents.

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 9 of 14 Tanks Emissions Information

Please listeachOSWRO tank requiring Level 1 or Level 2 control:

Tank IDTank capacity (gallons)Tank content MTVP1

### Tank content AVP2

### Tank height (feet)Tank diameter (feet) Tank average annual throughputTank emissions control equipment

K-666 50,000 50 13.5 Kiln (primary)/ Carbon Units (backup)

K-801 80,000 40.01 18.25 Kiln (primary)/ Carbon Units (backup)

K-802 80,000 40.01 18.25 Kiln (primary)/ Carbon Units (backup)

K-803 80,000 40.01 18.25 Kiln (primary)/ Carbon Units (backup)

1

### Maximum True HAP Vapor Pressure

2

### Average HAP Vapor Pressure For each tank with an internal floating roof, please list the slotted ladder information:

Tank IDNumber of ladders with slotted legsGasketed deck cover over slotted ladder(s)?Ladder sleeve over slotted ladder(s)?Pole wipers in place for slotted ladder legs? N/A



### For each tank with a fixed roof, please list the tank fitting information:

Tank IDNumber of access hatches Number of gauge hatches Number of conservation ventsNumber of valves/instrumentsNumber of
emergency pressure relief
vents
K-666 11 2 1 6 3
K-801 12 2 1 6 2
K-802 12 2 1 6 2
K-803 12 2 1 6 2

1

### Maximum True HAP Vapor Pressure

For each tank with a floating roof (internal or external), please list the tank information:

Tank IDAnnual number of days roof rests on landing legsLength of landing legs N/A

### (add information for more tanks as necessary) Have you entered the tanks emissions for your OSWRO processes in Enclosure 2A?

Have you completed all control information fields for your OSWRO storage vessels in Enclosure 2A?

What emissions calculation approach was used to estimate the tank emissions? If no, please explain.

If no, please explain.



### (add information for more tanks as necessary)

(add information for more tanks as necessary) Please provide the additional capital and annual costs of this practice above that required by the OSWRO NESHAP: Please provide documentation demonstrating the basis for the tanks emissions estimates.Are you providing emissions factors, source test data or other data?

See "Confidential Business Information" Summary

Are you implementing work practices or other HAP control techniques beyond those required by the MACT standard?

See "Confidential Business Information"

Summary If "Other", please explain:

If "Other", please explain:

If yes, please describe the control technique(s):

See "Confidential Business Information" Summary 

### Equations from AP-42 used to calculate emissions from tanks, which are based on the same algorithm as the "TANKS"
program.

See "Confidential Business Information" Summary

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 10 of 14 Tanks Emissions Information

Please enter any other comments regarding tanks here: (add information for more tanks as necessary)

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 11 of 14 Off-Site Material Treatment

If you treat off-site waste using biological degradation, please answer the following questions:

Please enter any other comments regarding off-site waste treatment here: N/A 

### Do you perform any testing or other practices to determine whether fouling agents may be in the waste received? N/A 

### What method of off-site waste HAP reduction is used?

Waste HAP-containing materials are combusted for energy recovery in the cement kiln. HAP emissions are controlled by venting the emissions to the cement kiln or carbon canisters.

How do you characterize the components of the waste products you receive that are treated with biological degradation? N/A If "Other" or more than one of the above applies, please explain.

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 12 of 14 Startup and Shutdown Events

If no for any of the above, please explain: Equipment Leaks

Organic and Oil-Water Separators

Process Vents

Tanks Transfer Systems

Containers

Surface Impoundments The United States Court of Appeals for the District of Columbia Circuit vacated portions of two provisions in the EPA’s CAA section 112 regulations governing the emissions of HAP during periods of startup, shutdown and malfunction (SSM). Sierra Club v. EPA, 551 F.3d 1019 (D.C. Cir. 2008). Specifically, the Court vacated the SSM exemption contained in 40 CFR 63.6(f)(1) and 40 CFR 63.6(h)(1), that are part of a regulation, commonly referred to as the “General Provisions Rule,” that the EPA promulgated under section 112 of the CAA. When incorporated into CAA section 112(d) regulations for specific source categories, these two, now vacated, provisions exempted sources from the requirement to comply with the otherwise applicable CAA section 112(d) emission standard during periods of SSM. To be consistent with the Court’s decision, facilities must comply with the applicable standards at all times.

For each emission source type, do the annual emissions estimate in the Enclosure 2A "Emissions (TPY)" field include the annual emissions from startup and shutdown events that you added in the "STARTUP EMISSIONS (TPY)" and "SHUTDOWN EMISSIONS (TPY)" fields? Please enter a separate response for each emissions point type below:

For each emission source type, can you comply with the emissions limitation and/or work practices in the regulation that apply during normal operation during startup and shutdown events? Please enter a separate response for each emissions point type below: Surface Impoundments

Tanks Equipment Leaks

Transfer Systems

Organic and Oil-Water Separators

Containers

Process Vents

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 13 of 14 Startup and Shutdown Events

Tanks - Yes, startup/shutdown emissions are included in Enclosure 2A. Yes, compliance can be met during startups/shutdowns. Equipment Leaks, Transfer Systems, Separators, Containers, Surface Impoundments, and Process Vents - N/A

Please provide the following information about all startup and shutdown events:

Equipment Leaks (i.e., pumps)/Transfer Systems, Tanks
Yes, except for pumps, which operate more intermittently.
Pump/Transfer Systems - when there is no longer a demand for the material to be transferred. Tanks - Assume shutdown occurs when empty, and startup occurs when begin transferring material into tank. Therefore, this occurs during a cleanout or repair of the unit.

No relevant difference.
Through a control device until the unit is "opened" for cleanout or repair. Pumps/Transfer Systems - Up to several times per day. Tanks - Approximately 1/year.
The duration of the startup/shutdown process is negligible.

Pumps/Transfer Systems - Startup begins when the pump/transfer system begins to move material, and ends when the pump/transfer system ceases to move the material. Tanks - shutdown begins when the tank is emptied prior to being "opened" for cleanout or repair. Startup begins when the tank is closed and material is introduced to the tank. Pumps/Transfer Systems - For startup, moving equipment. No special concerns are associated with shutdown. Tanks - For startup, access points closed to prevent spillage/emissions and moving equipment. No special concerns are associated with shutdown.

Same as normal operation

Same as normal operation

Same as normal operation 

### 1.c. How does the startup or shutdown event compare to normal operations (e.g., differences in flowrate, temp., pressure, alternate fuels used, alternate control devices used, etc.)?

6. How do you determine the HAP emissions during the event? 1. What emissions source types experience startup and shutdown events?

7. How are control devices and work practices used to minmize emissions during the startup or shutdown event? 8. What compliance determination method(s) do you use during startup and shutdown events (e.g., monitor with CEMS)? 1.a. Under normal operating conditions, do these emissions sources operate continuously?

1.b. What triggers the equipment to experience a startup or shutdown event (e.g. hot startup, startup after an emergency shutdown, re-start, control device startup)?

2. How often do startup or shutdown events occur? 1.d. How are emissions released to the atmosphere (e.g., through a pressure relief device)?

4. What marks the end of the startup or shutdown event? 3. What is the average and range of event duration?

5. What safety issues are connected with a startup or shutdown event?

### U.S. EPA Information Collection Request for Off-Site Waste and Recovery Operations

Page 14 of 14 Startup and Shutdown Events

N/A

N/A

N/A

N/A 

### 9.c. How much would HAP emissions be reduced compared to an uncontrolled event? (If "emission factor" is used as basis for emissions estimate, please provide the emission factor and sources of the emission
factor.1

### ) 9. During startup and shutdown events, if you cannot comply with the emissions limitation and/or work practices in the regulation that apply during normal operation, what is the minimum emissions level that could be achieved?

1If "source test" is used as basis for emissions estimate, please provide a copy of the
source test. 

### Please enter any other comments regarding startup or shutdown here: 9.a. Please describe how HAP emissions would be minimized.

9.b. How much would it cost to minimize HAP emissions in this manner?

# Enclosure 2aEnclosure 2a

Page 1 Please complete this table for all OSWRO emission units. Please report all emissions related to the off-site waste handled and/or treated.

Facility NameEmission Unit IDProcess IDEmission Release Point IDSCC Code1Emissions Start DateEmissions End DatePollutant CAS Number2Pollutant Name (include

organic and non-organic pollutants)Actual Emissions (TPY)MACTAllowable Emissions

(TPY)3Routine Emissions Max Hourly

(lbs/hr)Startup Emissions (TPY)Startup Emissions

(lbs/hr)Shutdown Emissions (TPY)Shutdown Emissions

(lbs/hr)MACT Source CategoryEmission Release

Point Type4Stack Height

(ft)Exit Gas Temperature (°F) Stack Diameter (ft)Exit Gas Velocity (ft/sec)Exit Gas Flow Rate

(ft3/sec)FugitiveLength (EW) (ft)FugitiveWidth (NS) (ft)Fugitive Angle (degrees)5Longitude (decimal degrees)6Latitude (decimal degrees)6Is Control Measure In

Place?Control Measure7Control Measure Efficiency Comments

EXAMPLE ENTRY:American Welding Paducah Plant25 25 25 5031000101/01/1012/31/10100414Ethyl Benzene 2.45 4.32 6.7 1.24 0.08 0.61 0.2Off-Site Waste and Recovery Operationsvertical 44 16003.0999999053.8699998861758NA NANA -72.078903241.44273758yes flare 98%reduction efficency based on manufacturer guarantees

Giant Cement Co.Storage Tanks: K-666 K-801 K-802 K-803 Storage Tanks: K-666 K-801 K-802 K-803 Primary: Kiln Stack 331-ES-21 Backup: Carbon Stack STACUN/A [a] 1/1/201112/31/2011 Off-Site Waste and Recovery OperationsverticalKiln Stack: 295 feet Carbon Stack: 12 feetKiln Stack: 210-400 F Carbon Stack: Ambient Kiln Stack: 14.2 feet Carbon Stack: 0.67 feetKiln Stack: 50 - 63 Carbon Stack: 0 - 4.3 [c]Kiln Stack: 7,920 - 10,000 Carbon Stack: 0 - 1.5 [c]N/A N/AN/A Kiln Stack: 80.440447 Carbon Stack: 80.441853Kiln Stack: 33.241808 Carbon Stack: 33.242147Yes Primary: Cement Kiln Backup: Carbon AdsorptionPrimary: >99.99% Backup: >95%Primary: Destruction and Removal Efficiency (DRE) testing Backup: Design Analysis

Giant Cement Co.Eqpt. Leak ComponentsEqpt. Leak ComponentsEqpt. Leak ComponentsN/A [a] 1/1/201112/31/2011 Off-Site Waste and Recovery OperationsfugitiveN/AN/A N/A N/A N/A525 [d]1152 80.4421533.241861Yes LDAR Program

[a] These SCC codes do not reflect the SCC codes used at to the Giant facility, and do not appear to be applicable to the Giant facility. The applicable SCC code for the cement manufacturing facility is 30500623. An NAICS code reflective of the OSWRO units is 562211. [b] See the attached file, "Giant Cement Company OSWRO Calculations." [c] The flow rates for the carbon unit are estimates. There is no normal, consistent airflow. The air through the carbon unit is based on pressure as air is released from a storage tank. [d] The majority of the equipment leak components are located in the western half of the defined area.

1For SCC Code, please input one of the following codes: SCC SCC Description 50310001 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Equipment Leaks 50310002 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Containers 50310003 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Tanks 50310004 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Organic and Oil-Water Separators 50310005 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Surface Impoundments 50310006 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Transfer Systems 50310007 Waste Disposal, Solid Waste Disposal-Industrial, Non-TSDF Treatment, Storage, Disposal Processes, Process Vents

2See List of HAPs in separate worksheet for a table of CAS numbers and HAPs

3MACT- allowable emissions are the maximum emission levels allowed while in compliance with the MACT standards

4Emission point type choices include: fugitive, vertical, horizontal, goose neck, vertical with rain cap, or downward-facing vent

5Fugitive Angle: Specifies the rotation of the source from north (in the clockwise direction). The location coordinates should reflect the southwest corner of the area source as shown in this graphic:

6Location of stack or southwest corner of a fugitive emissions release point

7For control measures, please include all control measures used for that emission point, including but not limited to:

Activated Carbon Adsorption list specific type in Control Measure Comments column

Combustor list specific type in Control Measure Comments column Electrostatic Precipitator Fabric Filter/Baghouse Flare Pressurized Tank Fixed Roof Tank Fixed Roof Tank Vented to Control Device External Floating Roof Tank Fixed Roof Tank with Internal Floating Roof Vapor Balancing Floating Membrane Cover Cover Vented to Control Device High-Efficiency Particulate Air Filter (HEPA)

Leak Detection and Repair Program

Condenser See separate file [b] (annual average if the parameter varies) Vertical Emissions Release Point Parameters Fugitive Emissions Release Point Parameters

See separate file [b]Enclosure 2a

Page 2 Scrubber list specific type in Control Measure Comments column

Multiple Controls in Series list specific types in Control Measure Comments column

Other Control Device describe in Control Measure Comments column

Pollution Prevention Technique describe in Control Measure Comments column

Process Modification describe in Control Measure Comments column

# DRAFT

Pollutant Name CAS No. Acetaldehyde 75070 Acetamide 60355 Acetonitrile 75058 Acetophenone 98862 2-Acetylaminofluorene 53963 Acrolein 107028 Acrylamide 79061 Acrylic acid 79107 Acrylonitrile 107131 Allyl chloride 107051 4-Aminobiphenyl 92671 Aniline 62533 o-Anisidine 90040 Asbestos 1332214 Benzene (including benzene from gasoline) 71432 Benzidine 92875 Benzotrichloride 98077 Benzyl chloride 100447 Biphenyl 92524 Bis(2-ethylhexyl)phthalate (DEHP) 117817 Bis(chloromethyl)ether 542881 Bromoform 75252 1,3-Butadiene 106990 Calcium cyanamide 156627 Captan 133062 Carbaryl 63252 Carbon disulfide 75150 Carbon tetrachloride 56235 Carbonyl sulfide 463581 Catechol 120809 Chloramben 133904 Chlordane 57749 Chlorine 7782505 Chloroacetic acid 79118 2-Chloroacetophenone 532274 Chlorobenzene 108907 Chlorobenzilate 510156 Chloroform 67663 Chloromethyl methyl ether 107302 Chloroprene 126998 Cresols/Cresylic acid (isomers and mixture) 1319773 o-Cresol 95487 m-Cresol 108394 p-Cresol 106445 Cumene 98828 2,4-D, salts and esters 94757 DDE 3547044 Diazomethane 334883 Dibenzofurans 132649 1,2-Dibromo-3-chloropropane 96128 Dibutylphthalate 84742 1,4-Dichlorobenzene(p) 106467 3,3-Dichlorobenzidene 91941 Dichloroethyl ether (Bis(2-chloroethyl)ether) 111444 1,3-Dichloropropene 542756 Dichlorvos 62737 Diethanolamine 111422 N,N-Diethyl aniline (N,N-Dimethylaniline) 121697 List of Hazardous Air Pollutants (HAP)Pollutant Name CAS No. List of Hazardous Air Pollutants (HAP)

Diethyl sulfate 64675 3,3-Dimethoxybenzidine 119904 Dimethyl aminoazobenzene 60117 3,3'-Dimethyl benzidine 119937 Dimethyl carbamoyl chloride 79447 Dimethyl formamide 68122 1,1-Dimethyl hydrazine 57147 Dimethyl phthalate 131113 Dimethyl sulfate 77781 4,6-Dinitro-o-cresol, and salts 534521 2,4-Dinitrophenol 51285 2,4-Dinitrotoluene 121142 1,4-Dioxane (1,4-Diethyleneoxide) 123911 1,2-Diphenylhydrazine 122667 Epichlorohydrin (l-Chloro-2,3-epoxypropane) 106898 1,2-Epoxybutane 106887 Ethyl acrylate 140885 Ethyl benzene 100414 Ethyl carbamate (Urethane) 51796 Ethyl chloride (Chloroethane) 75003 Ethylene dibromide (Dibromoethane) 106934 Ethylene dichloride (1,2-Dichloroethane) 107062 Ethylene glycol 107211 Ethylene imine (Aziridine) 151564 Ethylene oxide 75218 Ethylene thiourea 96457 Ethylidene dichloride (1,1-Dichloroethane) 75343 Formaldehyde 50000 Heptachlor 76448 Hexachlorobenzene 118741 Hexachlorobutadiene 87683 Hexachlorocyclopentadiene 77474 Hexachloroethane 67721 Hexamethylene-1,6-diisocyanate 822060 Hexamethylphosphoramide 680319 Hexane 110543 Hydrazine 302012 Hydrochloric acid 7647010 Hydrogen fluoride (Hydrofluoric acid) 7664393 Hydrogen sulfide 7783064 Hydroquinone 123319 Isophorone 78591 Lindane (all isomers) 58899 Maleic anhydride 108316 Methanol 67561 Methoxychlor 72435 Methyl bromide (Bromomethane) 74839 Methyl chloride (Chloromethane) 74873 Methyl chloroform (1,1,1-Trichloroethane) 71556 Methyl hydrazine 60344 Methyl iodide (Iodomethane) 74884 Methyl isobutyl ketone (Hexone) 108101 Methyl isocyanate 624839 Methyl methacrylate 80626 Methyl tert butyl ether 1634044 4,4-Methylene bis(2-chloroaniline) 101144 Methylene chloride (Dichloromethane) 75092 Methylene diphenyl diisocyanate (MDI) 101688 4,4'¬-Methylenedianiline 101779 Naphthalene 91203Pollutant Name CAS No. List of Hazardous Air Pollutants (HAP)

Nitrobenzene 98953 4-Nitrobiphenyl 92933 4-Nitrophenol 100027 2-Nitropropane 79469 N-Nitroso-N-methylurea 684935 N-Nitrosodimethylamine 62759 N-Nitrosomorpholine 59892 Parathion 56382 Pentachloronitrobenzene (Quintobenzene) 82688 Pentachlorophenol 87865 Phenol 108952 p-Phenylenediamine 106503 Phosgene 75445 Phosphine 7803512 Phosphorus 7723140 Phthalic anhydride 85449 Polychlorinated biphenyls (Aroclors) 1336363 1,3-Propane sultone 1120714 beta-Propiolactone 57578 Propionaldehyde 123386 Propoxur (Baygon) 114261 Propylene dichloride (1,2-Dichloropropane) 78875 Propylene oxide 75569 1,2-Propylenimine (2-Methyl aziridine) 75558 Quinoline 91225 Quinone 106514 Styrene 100425 Styrene oxide 96093 2,3,7,8-Tetrachlorodibenzo-p-dioxin 1746016 1,1,2,2-Tetrachloroethane 79345 Tetrachloroethylene (Perchloroethylene) 127184 Titanium tetrachloride 7550450 Toluene 108883 2,4-Toluene diamine 95807 2,4-Toluene diisocyanate 584849 o-Toluidine 95534 Toxaphene (chlorinated camphene) 8001352 1,2,4-Trichlorobenzene 120821 1,1,2-Trichloroethane 79005 Trichloroethylene 79016 2,4,5-Trichlorophenol 95954 2,4,6-Trichlorophenol 88062 Triethylamine 121448 Trifluralin 1582098 2,2,4-Trimethylpentane 540841 Vinyl acetate 108054 Vinyl bromide 593602 Vinyl chloride 75014 Vinylidene chloride (1,1-Dichloroethylene) 75354 Xylenes (isomers and mixture) 1330207 o-Xylenes 95476 m-Xylenes 108383 p-Xylenes 106423 Antimony Compounds 0 Arsenic Compounds (inorganic including arsine) 0 Beryllium Compounds 0 Cadmium Compounds 0 Chromium Compounds 0 Cobalt Compounds 0 Coke Oven Emissions 0Pollutant Name CAS No. List of Hazardous Air Pollutants (HAP)

Cyanide Compounds 0 Glycol ethers 0 Lead Compounds 0 Manganese Compounds 0 Mercury Compounds 0 Fine mineral fibers 0 Nickel Compounds 0 Polycylic Organic Matter 0 Radionuclides (including radon) 0 Selenium Compounds 0

# Other ICR Response Info.Giant Cement Company OSWRO Section 114 Request Organic HAP Emissions Calculations

Total VOC Emissions Source GroupingsUncontrolled Emissions lb/yrAssumed Control Efficiency (%)Controlled Emissions lb/yrAnnual No. of TurnoversEmissions/ Turnover (lb/turnover)Max No. of Turnovers/ HrMax lb/hr[1] 50K Tank Working 866.91 0.95 43.35 44.22 0.98 0.54 0.53 80K Tank Working 1387.050.95 69.35 44.22 1.57 0.23 0.35 Total Tank Working 5028.070.95 251.40 0.88 50K Tank Breathing 158.70 0.95 7.94 0.00091 80K Tank Breathing 257.25 0.95 12.86 0.00147 Tank Breathing 930.45 0.95 46.52 0.00237 Tank Total 5958.520.95 297.93 0.88 Equipment Leaks 5984.41 N/A N/A 0.68

Actual Emissions (TPY)MACTAllowable Emissions

(TPY)3Routine Emissions Max Hourly

(lbs/hr)Startup Emissions (TPY) Startup Emissions

(lbs/hr) Acetaldehyde 75070 0 N/A 0 0 0 Acetamide 60355 0 N/A 0 0 0 Acetonitrile 750580.03190240.0048 N/A 0.0282 0.0000 0.0282 Acetophenone 988620.00038940.0001 N/A 0.00030.0000 0.0003 2-Acetylaminofluorene 53963 0 N/A 0 0 0 Acrolein 107028 0 N/A 0 0 0 Acrylamide 79061 0 N/A 0 0 0 Acrylic acid 79107 0 N/A 0 0 0 Pollutant Name CAS No.Vapor Weight Fraction (Fraction) [1]Maximum lb/hr working losss emissions defined as working losses associated with the loading of one railcar at 27,000 gallons/hr into one 50K tank and three trucks into the 80K tanks Total Tank Losses: Equipment Leak Emissions:

Tank Emissions[1] Total Working Losses: Total 50K Breathing Losses: Total 80K Breathing Losses: Total Breathing Losses:Acrylonitrile 1071310.03175650.0047 N/A 0.0281 0.0000 0.0281 Allyl chloride 107051 0 N/A 0 0 0 4-Aminobiphenyl 92671 0 N/A 0 0 0 Aniline 62533 0 N/A 0 0 0 o-Anisidine 90040 0 N/A 0 0 0 Asbestos 1332214 0 N/A 0 0 0 Benzene (including benzene from gasoline)714320.00084150.0001 N/A 0.00070.0000 0.0007 Benzidine 92875 0 N/A 0 0 0 Benzotrichloride 98077 0 N/A 0 0 0 Benzyl chloride 100447 0 N/A 0 0 0 Biphenyl 92524 0 N/A 0 0 0 Bis(2-ethylhexyl)phthalate (DEHP) 117817 0 N/A 0 0 0 Bis(chloromethyl)ether 542881 0 N/A 0 0 0 Bromoform 75252 0 N/A 0 0 0 1,3-Butadiene 106990 0 N/A 0 0 0 Calcium cyanamide 156627 0 N/A 0 0 0 Captan 133062 0 N/A 0 0 0 Carbaryl 63252 0 N/A 0 0 0 Carbon disulfide 75150 0 N/A 0 0 0 Carbon tetrachloride 56235 0 N/A 0 0 0 Carbonyl sulfide 463581 0 N/A 0 0 0 Catechol 120809 0 N/A 0 0 0 Chloramben 133904 0 N/A 0 0 0 Chlordane 57749 0 N/A 0 0 0 Chlorine 7782505 0 N/A 0 0 0 Chloroacetic acid 79118 0 N/A 0 0 0 2-Chloroacetophenone 532274 0 N/A 0 0 0 Chlorobenzene 108907 0 N/A 0 0 0 Chlorobenzilate 510156 0 N/A 0 0 0 Chloroform 67663 0 N/A 0 0 0 Chloromethyl methyl ether 107302 0 N/A 0 0 0 Chloroprene 126998 0 N/A 0 0 0 Cresols/Cresylic acid (isomers and mixture)1319773 0 N/A 0 0 0 o-Cresol 95487 0 N/A 0 0 0 m-Cresol 108394 0 N/A 0 0 0 p-Cresol 106445 0 N/A 0 0 0 Cumene 988280.00032050.0000 N/A 0.00030.0000 0.00032,4-D, salts and esters 94757 0 N/A 0 0 0 DDE 3547044 0 N/A 0 0 0 Diazomethane 334883 0 N/A 0 0 0 Dibenzofurans 132649 0 N/A 0 0 0 1,2-Dibromo-3-chloropropane 96128 0 N/A 0 0 0 Dibutylphthalate 84742 0 N/A 0 0 0 1,4-Dichlorobenzene(p) 106467 0 N/A 0 0 0 3,3-Dichlorobenzidene 91941 0 N/A 0 0 0 Dichloroethyl ether (Bis(2-chloroethyl)ether)111444 0 N/A 0 0 0 1,3-Dichloropropene 542756 0 N/A 0 0 0 Dichlorvos 62737 0 N/A 0 0 0 Diethanolamine 111422 0 N/A 0 0 0 N,N-Diethyl aniline (N,N-Dimethylaniline) 121697 0 N/A 0 0 0 Diethyl sulfate 64675 0 N/A 0 0 0 3,3-Dimethoxybenzidine 119904 0 N/A 0 0 0 Dimethyl aminoazobenzene 60117 0 N/A 0 0 0 3,3'-Dimethyl benzidine 119937 0 N/A 0 0 0 Dimethyl carbamoyl chloride 79447 0 N/A 0 0 0 Dimethyl formamide 681220.00030070.0000 N/A 0.00030.0000 0.0003 1,1-Dimethyl hydrazine 57147 0 N/A 0 0 0 Dimethyl phthalate 131113 0 N/A 0 0 0 Dimethyl sulfate 77781 0 N/A 0 0 0 4,6-Dinitro-o-cresol, and salts 534521 0 N/A 0 0 0 2,4-Dinitrophenol 51285 0 N/A 0 0 0 2,4-Dinitrotoluene 121142 0 N/A 0 0 0 1,4-Dioxane (1,4-Diethyleneoxide) 1239110.00006580.0000 N/A 0.0001 0.0000 0.0001 1,2-Diphenylhydrazine 122667 0 N/A 0 0 0 Epichlorohydrin (l-Chloro-2,3-epoxypropane)106898 0 N/A 0 0 0 1,2-Epoxybutane 106887 0 N/A 0 0 0 Ethyl acrylate 140885 0 N/A 0 0 0 Ethyl benzene 1004140.00216740.0003 N/A 0.00190.0000 0.0019 Ethyl carbamate (Urethane) 51796 0 N/A 0 0 0 Ethyl chloride (Chloroethane) 75003 0 N/A 0 0 0 Ethylene dibromide (Dibromoethane) 106934 0 N/A 0 0 0 Ethylene dichloride (1,2-Dichloroethane) 107062 0 N/A 0 0 0 Ethylene glycol 1072110.00004240.0000 N/A 0.00000.0000 0.0000 Ethylene imine (Aziridine) 151564 0 N/A 0 0 0Ethylene oxide 75218 0 N/A 0 0 0 Ethylene thiourea 96457 0 N/A 0 0 0 Ethylidene dichloride (1,1-Dichloroethane) 75343 0 N/A 0 0 0 Formaldehyde 500000.00071160.0001 N/A 0.00060.0000 0.0006 Heptachlor 76448 0 N/A 0 0 0 Hexachlorobenzene 118741 0 N/A 0 0 0 Hexachlorobutadiene 87683 0 N/A 0 0 0 Hexachlorocyclopentadiene 77474 0 N/A 0 0 0 Hexachloroethane 67721 0 N/A 0 0 0 Hexamethylene-1,6-diisocyanate 822060 0 N/A 0 0 0 Hexamethylphosphoramide 680319 0 N/A 0 0 0 Hexane 1105430.05597850.0083 N/A 0.04950.0000 0.0495 Hydrazine 302012 0 N/A 0 0 0 Hydrochloric acid 7647010 0 N/A 0 0 0 Hydrogen fluoride (Hydrofluoric acid) 7664393 0 N/A 0 0 0 Hydrogen sulfide 7783064 0 N/A 0 0 0 Hydroquinone 123319 0 N/A 0 0 0 Isophorone 78591 0 N/A 0 0 0 Lindane (all isomers) 58899 0 N/A 0 0 0 Maleic anhydride 108316 0 N/A 0 0 0 Methanol 675610.07965580.0119 N/A 0.07050.0000 0.0705 Methoxychlor 72435 0 N/A 0 0 0 Methyl bromide (Bromomethane) 74839 0 N/A 0 0 0 Methyl chloride (Chloromethane) 74873 0 N/A 0 0 0 Methyl chloroform (1,1,1-Trichloroethane) 71556 0 N/A 0 0 0 Methyl hydrazine 60344 0 N/A 0 0 0 Methyl iodide (Iodomethane) 74884 0 N/A 0 0 0 Methyl isobutyl ketone (Hexone) 1081010.00663380.0010 N/A 0.00590.0000 0.0059 Methyl isocyanate 624839 0 N/A 0 0 0 Methyl methacrylate 80626 0 N/A 0 0 0 Methyl tert butyl ether 16340440.03772820.0056 N/A 0.03340.0000 0.0334 4,4-Methylene bis(2-chloroaniline) 101144 0 N/A 0 0 0 Methylene chloride (Dichloromethane) 750920.11498850.0171 N/A 0.10170.0001 0.1017 Methylene diphenyl diisocyanate (MDI) 101688 0 N/A 0 0 0 4,4'¬-Methylenedianiline 101779 0 N/A 0 0 0 Naphthalene 912030.00001140.0000 N/A 0.00000.0000 0.0000 Nitrobenzene 98953 0 N/A 0 0 04-Nitrobiphenyl 92933 0 N/A 0 0 0 4-Nitrophenol 100027 0 N/A 0 0 0 2-Nitropropane 79469 0 N/A 0 0 0 N-Nitroso-N-methylurea 684935 0 N/A 0 0 0 N-Nitrosodimethylamine 62759 0 N/A 0 0 0 N-Nitrosomorpholine 59892 0 N/A 0 0 0 Parathion 56382 0 N/A 0 0 0 Pentachloronitrobenzene (Quintobenzene) 82688 0 N/A 0 0 0 Pentachlorophenol 87865 0 N/A 0 0 0 Phenol 1089520.00008780.0000 N/A 0.0001 0.0000 0.0001 p-Phenylenediamine 106503 0 N/A 0 0 0 Phosgene 75445 0 N/A 0 0 0 Phosphine 7803512 0 N/A 0 0 0 Phosphorus 7723140 0 N/A 0 0 0 Phthalic anhydride 85449 0 N/A 0 0 0 Polychlorinated biphenyls (Aroclors) 1336363 0 N/A 0 0 0 1,3-Propane sultone 1120714 0 N/A 0 0 0 beta-Propiolactone 57578 0 N/A 0 0 0 Propionaldehyde 123386 0 N/A 0 0 0 Propoxur (Baygon) 114261 0 N/A 0 0 0 Propylene dichloride (1,2-Dichloropropane)78875 0 N/A 0 0 0 Propylene oxide 75569 0 N/A 0 0 0 1,2-Propylenimine (2-Methyl aziridine) 75558 0 N/A 0 0 0 Quinoline 91225 0 N/A 0 0 0 Quinone 106514 0 N/A 0 0 0 Styrene 1004250.00328390.0005 N/A 0.00290.0000 0.0029 Styrene oxide 96093 0 N/A 0 0 0 2,3,7,8-Tetrachlorodibenzo-p-dioxin 1746016 0 N/A 0 0 0 1,1,2,2-Tetrachloroethane 79345 0 N/A 0 0 0 Tetrachloroethylene (Perchloroethylene) 1271840.00087830.0001 N/A 0.00080.0000 0.0008 Titanium tetrachloride 7550450 0 N/A 0 0 0 Toluene 1088830.05725640.0085 N/A 0.05060.0000 0.0506 2,4-Toluene diamine 95807 0 N/A 0 0 0 2,4-Toluene diisocyanate 584849 0 N/A 0 0 0 o-Toluidine 95534 0 N/A 0 0 0 Toxaphene (chlorinated camphene) 8001352 0 N/A 0 0 0 1,2,4-Trichlorobenzene 120821 0 N/A 0 0 01,1,2-Trichloroethane 79005 0 N/A 0 0 0 Trichloroethylene 790160.00041720.0001 N/A 0.00040.0000 0.0004 2,4,5-Trichlorophenol 95954 0 N/A 0 0 0 2,4,6-Trichlorophenol 88062 0 N/A 0 0 0 Triethylamine 1214480.00091850.0001 N/A 0.00080.0000 0.0008 Trifluralin 1582098 0 N/A 0 0 0 2,2,4-Trimethylpentane 540841 0 N/A 0 0 0 Vinyl acetate 108054 0 N/A 0 0 0 Vinyl bromide 593602 0 N/A 0 0 0 Vinyl chloride 75014 0 N/A 0 0 0 Vinylidene chloride (1,1-Dichloroethylene) 75354 0 N/A 0 0 0 Xylenes (isomers and mixture) 13302070.00779750.0012 N/A 0.00690.0000 0.0069 o-Xylenes 954760.00146180.0002 N/A 0.00130.0000 0.0013 m-Xylenes 1083830.00287770.0004 N/A 0.00250.0000 0.0025 p-Xylenes 1064230.00292810.0004 N/A 0.00260.0000 0.0026 TOTALS 0.44140160.0658 0.3905 0.0002 0.3905

[1]Tanks do not have a typical "start-up." Therefore, we have assumed start-up is commencing the re-filling of a tank after a shut-down. These shutdowns are considered to occur once per year and the start-up is conservatively assumed to take one hour. Therefore, the tank start-up emissions represent the maximum one-hour emissions scenario.Shutdown Emissions (TPY)Shutdown Emissions

(lbs/hr) Actual Emissions (TPY)MACTAllowable Emissions

(TPY)3Routine Emissions Max Hourly (lbs/hr)Startup Emissions (TPY)Startup Emissions

(lbs/hr)Shutdown Emissions (TPY)Shutdown Emissions

(lbs/hr) N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0.0955 N/A0.0218 N/A N/A N/A N/A N/A N/A 0.0012 N/A0.0003 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A Equipment Leak EmissionsN/A N/A 0.0950 N/A0.0217 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0.0025 N/A0.0006 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0.0010 N/A0.0002 N/A N/A N/A N/AN/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0.0009 N/A0.0002 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0.0002 N/A0.0000 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0.0065 N/A0.0015 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0.0001 N/A0.0000 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/AN/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0.0021 N/A0.0005 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A N/A N/A 0 N/A 0 N/A N/A N/A N/A 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