## Date: October 1 8 , 2012

Subject: Summary of RBLC and Other Findings to Support Section 111(b) Review o f

Kraft Pulp Mill NSPS

EPA Contract No. EP

- D

- 11

- 0 84 ; Work Assignment No. 1

- 0 8

From: Thomas Holloway

To: Kelley Spence, Nick Swanson, John Bradfield

, B ill Schrock

U.S. Environmental Protection Agency

Research Triangle Park, NC 27711

I. Introduction

Under section 11 1 ( b )( 1 ) (B) of the Clean Air Act (CAA)

, the U.S. Environmental

Protection Agency (EPA) is required to review and, if appropriate, revise existing new source

performance standards (NSPS) at least every 8 years. The NSPS for kraft pulp mills (40 CFR

part 60, subpart BB) were promulgated in 1978 and last reviewed in 1986, and are due for

another review. The NSPS regulates emissions of particulate matt er (PM) from new, modified,

and reconstructed recovery furnaces, smelt dissolving tanks, and lime kilns at kraft pulp mills.

The NSPS also regulates emissions of total reduced sulfur (TRS) compounds from new

, modified and reconstructed digester s , brown sto ck washers, multiple

- effect evaporator s

, condensate stripper s , recovery furnaces, smelt dissolving tanks, and lime kilns at kraft pulp mills.

Total reduced sulfur compounds are defined under 40 CFR 6 0 .281(c) of the kraft pulp mills

NSPS to include the foll owing four compounds: hydrogen sulfide (H 2 

## S), methyl mercaptan,

dimethyl sulfide, and dimethyl disulfide.

The purpose of this memorandum is to present information relevant to the NSPS review

from the following:

• A recent search of the RACT/BACT/LAER Cleari nghouse (RBLC) for information on

air pollution control options in the pulp and paper indust ry ;

• A 20 1 0 d ocument by the European Commission on b est available t echniques in the p ulp

and p aper i ndustry ; and

• A 2006 document by the State and Territorial Air Pol lution Program Administrators and

the Association of Local Air Pollution Control Offi cials (STAPPA/ALAPCO) on the

most effective ways to control emissions of fine particles (PM 2.5 

## ) and PM 2.5 

## precursors

from sources in various industry categories, including the pulp and paper industry

.

II. 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 increase by a large

amount, 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 control equipment. The terms “RACT,”

## 2 “BACT, ” and “LAER” are acronyms for different program requirements under the NSR

program. RACT, or Reasonably Available Control Technology, is required on sources in areas

that are not meeting national ambient air quality standards (i.e., nonattainment areas). B ACT, or

Best Available Control Technology, is required on major new or modified sources in attainment

areas. LAER, or Lowest Achievable Emission Rate, is required on major new or modified

sources in non

- attainment areas. BACT and LAER (and sometimes RACT) are determined on a

case

- by

- case basis, usually by State or local permitting agencies. The EPA established the

RACT/BACT/LAER Clearinghouse, or RBLC, to provide a central database of air pollution

technology information (including past BACT and LAER decisi ons 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 subject to RACT,

BACT, and LAER requirements. Noteworthy pr evention and control technology decisions and

information are included even if they are not related to past RACT, BACT, or LAER decisions.

The RBLC contains over 5,000 air pollution control permit determinations that can help

identify appropriate control options 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 sources, and includes data submitted by several

U.S. te rritories and all 50 s tates on over 200 different air pollutants and 1,000 industrial

processes.

The RBLC provides several options for searching the database to locate applicable

control options

. To identify control options relevant to the review of the k raft pulp mill s NSPS

, search es of the RBLC w ere made using the Process Type field for Process Type Code 30.200

– Kraft Pulp & Paper Process. A n initial search looked at records from 2000 to 2010. A more

recent search looked at records from 2010 to 2012 , bu t found nothing new to add to the initial

search results

. We extracted the relevant data from the RBLC website and grouped the search

results for similar process types under the following RTI process codes :

• For TRS compounds: digester, evaporator, noncon densable gases (NCG) incinerator

, recovery furnace, smelt dissolving tank, and lime kiln

• For PM: recovery furnace, smelt dissolving tank, and lime kiln

The following sections describe the findings of our RBLC search for TRS and PM control

options used at kraft pulp mills.

A. Total Reduced Sulfur (TRS)

The RBLC search identified information for 28 kraft pulp mills that use some type of

emissions control for TRS

, H 2 

## S (a major component of TRS), odor (typically from TRS), volatile

organic compounds (VOC), met hanol, or formaldehyde. The search also identified information

for an additional mill that converted its Nos. 2 and 3 recovery furnaces from direct contact

evaporator (DCE) units to non

- direct contact evaporator (NDCE) units

, which

, by their design

,

are ex pected to have lower TRS emissions

. Mills using control measures for non

- TRS

compounds ( VOC, methanol, or formaldehyde ) were included in the results because , in most

cases, TRS is expected to be reduced by the same control measures that reduce emissions of

## 3 these non

- TRS compounds

. Appendix A summarizes the results of the RBLC search for these 2 8

mills , organized by process code

. Note: Some of these mills have results for multiple compounds

and processes.

According to the RBLC search results, e missions of T RS, H 2 

## S, odor, VOC, and methanol

from digesters and evaporators at 1 2 kraft pulp mills a re controlled by routing them to an

incineration device, such as a lime kiln , boiler, or thermal oxidizer (NCG incinerator)

. Emissions

of TRS from the digesters at 1 of the 12 kraft pulp mills a re further controlled by adjust ing the

p H of the boiler’ s scrubber w ater to 8.0 prior to incinerati n g the TRS in the boiler

.

The RBLC search results noted that TRS and VOC emissions from recovery furnaces at

1 6 kraft pulp mills a re controlled through recovery furnace design and operation

, described

varyingly throughout the RBLC results as proper boiler design, installation of/conversion to an

NDCE recovery furnace, staged combustion, combustion improvements, proper boiler ope ratio n,

good combustion practices, and combustion control. The RBLC results also indicated that 1 of

the 16 mills uses proper boiler design and operation to control H 2 

## S emissions, a major

component of TRS, and another of the 16 mills uses good combustion practi ces to control

formaldehyde, which i s controlled through the same mechanisms as TRS. One of the 16 mills

also reduces the TRS and VOC emissions from its recovery furnace by limiting the recovery

furnace firing rate and pulp production rate. The RBLC result s indicated a 17 th 

## mill limits its

recovery furnace TRS emissions through a combination of good engineering practices,

continuous emissions monitoring, and a wet scrubber. While the RBLC results indicated a n 18 th



## mill limits its TRS emissions by upgrading the black liquor oxidation (BLO) system associated

with its DCE recovery furnaces , a review of the mill’s response to EPA’s 2011 information

collection request (ICR) indicates that the DCE recovery furnaces at this mill were converted to

the NDCE design in 2000 and 2001, at which time the BLO system would have been removed

.

Two mills’ recovery furnaces have TRS limits below the NSPS limit of 5 ppm at

8 percent oxygen ( O 2 

## ) for straight recovery furnaces. One mill’s recovery furnace, which ensures

reduced T RS emissions through the use of proper boiler design and operation, has a TRS

emission limit of 3 parts per million (ppm) at 8 percent O 2



## . An other mill’s recovery furnace,

which ensures reduced TRS emissions through the use of an NDCE recovery furnace

, goo d

combustion practice s, and limits on its recover y furnace firing rate (4.4 million pounds of black

liquor solids per day [ MM lb BLS/d]) and pulp p roduction ( 1410 air

- dried tons of bleached pulp

per day [ ADTBP/d ])

, has a TRS emission limit of 4 ppm at 8 pe rcent O 2



## .

The results of the RBLC search show ed lime kilns at 8 kraft pulp mills with some kind of

control measure to reduce TRS and VOC emissions. Four of these mills reduc e their TRS and

VOC emissions using wet scrubbers , with 1 of these 4 mills us ing fresh water in the scrubber and

another using optimal mud washing

. The remaining 4 mills use a variety of control measures to

reduce TRS and VOC emissions, including kiln design and operation, good combustion

practices, opti m ized mud washing

, or best manag ement practices for pulp washing

. One mill ’ s

lime kiln, which controls TRS with a wet scrubber using fresh water, has a TRS emission limit of

6.5 ppm, which is below the NSPS limit of 8 ppm at 10 percent O 2 

## for lime kilns

.

## 4 According to the RBLC search res ults, 2 kraft pulp mills rely on recovery furnace design

and operation to ensure reduced TRS and/or VOC emissions from the SDT downs tream of the

recovery furnace. A 3 rd 

## mill rel ies on its SDT wet scrubber to reduce TRS emissions from the

SDT , and a 4 th 

## mil l relies on a combination of a low

- sulfide water scrubber for the SDT and

limits to the recovery furnace firing rate and pulp production rate to reduce TRS emissions from

the SDT

. The SDTs at t he 3 rd 

## and 4 th 

## mills have TRS emission limits of 0.032 and 0.03 pound

per ton of black liquor solids (lb/ton BLS), respectively, which are slightly below the NSPS limit

of 0.033 lb/ton BLS for SDTs

.

B. Particulate Matter (PM)

The RBLC search identified information for 21 kraft pulp mills that use some type of

emissions con trol for filterable PM (15 mills) , filterable PM 10 

## (8 mills)

, condensable PM (1 mill)

, or lead compounds (1 mill)

. Note: As with TRS, some of the mills have results for multiple

pollutants and processes. Filterable PM includes those particles captured on the front half of the

sampling filter , with PM 10 

## comprising those particles 10 micrometers ( μm) or less in size.

Condensable PM includes those particles in the vapor phase at stack conditi ons which form a

solid/liquid after discharge from the stack and comprise those particles 2.5 μm or less in size

(PM 2.5 

## )

.

The mills listed for filterable PM 10 

## , condensable PM, and lead compounds were included

in the results because filterable PM is expected to be reduced by the same control measures that

reduce emissions of these other pollutants . Appendix B summarizes the results of the RBLC

search for these 21 mil ls, organized by process code.

The results of the RBLC search show that r ecovery furnace PM emissions at 1 9 kraft

pulp mills are controlled using a n ele ctrostatic precipitator (ESP). T hree of these 1 9 mills also

use other control mea sures, in additio n to the ESP. One also use s a wet scrubber, a 2 nd 

## also limit s

the recovery furnace firing rate and pulp production rate, and the 3 rd 

## also use s good combustion

practices.

Recovery furnaces at 9 of the 1 9 mills have filterable PM emission limits below the

N SPS limit of 0.044 grain per dry standard cubic foot (gr/dscf) at 8 percent O 2



## . These recovery

furnaces are listed in T able 1 below. The filterable PM limits more stringent than the NSPS

ranged from 0.02 to 0.036 gr/dscf at 8 percent O 2



## . All but one of the recovery furnaces control

PM emissions using just an ESP; the other recovery furnace uses an ESP in conjunction with

limits on its recovery furnace firing rate and pulp production.

## 5 Table 1. Recovery Fu rnaces with Filterable PM Limits More Stringent Than the NSPS

FACILITY NAME CO UNTY ST ATE PROCESS

NAME CONTROL

METHOD EMISSION LIMIT

Georgia

- Pacific Corp

. - Crossett Paper Operations Ashley AR 8R Recovery

Boiler Wet ESP 0.02 gr/dscf @ 8% O 2 

### (3

- hr average)

Rock

- Tenn Mill Co

. , LLC Marengo AL Recovery

Furnace ESP 0.021 gr/dscf @ 8% O 2 

### (3

- hr average)

Georgia Pacific Corp.

- Cedar Spring Operations Early GA Recovery Boiler ESP 0.032 gr/dscf @ 8% O 2



### Georgia

- Pacific Corp.

- Port Hudson Operations East Baton

Rouge Parish LA Recovery

Furnace No. 1 ESP 0.025 gr/dsc f @ 8% O 2



### Georgia

- Pacific

- Port

Hudson Operations East Baton

Rouge Parish LA Recovery

Furnace No. 2 ESP 0.025 gr/dscf @ 8% O 2



### International Paper

-

Mansfield Mill Desoto LA Recovery Boilers

No. 1 &; 2 (EQT

036 & 037) ESP 0.02 gr/dscf @ 8% O 2 

### (annual ave rage)

Weyerheauser Co

. - Marlboro Paper Mill Marlboro SC No. 1 Recovery

Furnace ESP/recovery

furnace firing rate

and pulp production

limits (4.4 MM lb

BLS/d and 1410

ADTBP/d) 0.021 gr/dscf @ 8% O 2



### Bowater York SC No. 3 Recovery

Furnace ESP 0.036 gr/dscf @ 8% O 2



### Mosinee Paper Corp. Marathon WI Recovery Boiler,

Process #B21,

Stack #S11 ESP 0.027 gr/dscf @ 8% O 2



### Domtar

- Nekoosa Mill Wood WI Kraft Black

Liquor Recovery

Furnace, B14 ESP 0.03 gr/dscf @ 8% O 2



### Note: The control method (wet ESP) listed in RBLC f or the Georgia

- Pacific Crossett mill is actually a wet

- bottom ESP, and the

type of ESP bottom is not relevant for PM control.



## The RBLC search results found that l ime kiln PM emissions at 10 kraft pulp mills are

controlled using a PM control device. Of the se 10 mills, 4 use a wet scrubber, 3 use an ESP, 1

uses pre

- cleaner cyclones prior to a wet scrubber, 1 use s a combination ESP/wet scrubber , and 1

uses a wet scrubber on one kiln and a combination ESP/wet scrubber on the other to control PM

emissions

. ( Not e: Although the RBLC search results indicated Lime Kiln No. 2 at the Georgia

Pacific Port Hudson mill was equipped with an ESP only, the ICR response for the mill indicates

it is actually equipped with an ESP and wet scrubber. ) One of the 4 mills using onl y wet

scrubbers also uses the scrubber to control lead compound emissions

.

Lime kilns at 3 of the 10 mills have filterable PM emission limits below the NSPS limits

of 0.066 gr/dscf for gas

- fired kilns and 0.13 gr/dscf for oil

- fired kilns at 10 percent O 2



## . These

lime kilns are listed in Table 2 below. The filterable PM limits more stringent than the NSPS

ranged from 0.01 to 0.05 gr/dscf at 10 percent O 2 

## . The three most stringent limits are met by

kilns with an ESP or a combination ESP/wet scrubber

.

## 6 Table 2

. Lime Kilns with Filterable PM Limits More Stringent Than the NSPS

FACILITY NAME CO UNTY ST ATE PROCESS NAME CONTROL

METHOD EMISSION LIMIT

Georgia

- Pacific Corp.

- Port Hudson Operations East Baton

Rouge Parish LA Lime Kiln No. 1 Wet scrubber 0.05 gr/dscf @ 10% O 2



### Georgia

- Pacific Corp.

- Port Hudson Operations East Baton

Rouge Parish LA Lime Kiln No. 2 ESP and wet

scrubber 0.033 gr/dscf @ 10%

O 2



### Bowater York SC Lime Kiln No. 2 ESP 0.03 gr/dscf @ 10% O 2



### Weyerhaeuser Co.

– Flint River Operations Macon GA R otary Lime Kiln ESP 0.01 gr/dscf @ 10% O 2



### Note: Although the RBLC indicated Lime Kiln No. 2 at the Georgia

- Pacific Port Hudson mill was equipped with an ESP only,

the ICR response for the mill indicates it is equipped with an ESP and wet scrubber.



## Accord ing to the RBLC search results, SDT PM emissions at 6 kraft pulp mills are

controlled using a PM control device. The RBLC results indicated that 1 o f these 6 mills uses an

ESP to control PM emissions

. For clarification , we reviewed the 2011 ICR response f r om this

mill and found that the SDT emissions are actually vented to a n SDT wet scrubber first, then to

the associated recovery furnace, which is equipped with an ESP. The RBLC results also found 4

mills that use a wet scrubber only and 1 mill that use s a wet scrubber in combination with limits

on recovery furnace firing r ate and pulp production rate.

The SDTs at 3 of the 6 mills have filterable PM emission limits below the NSPS limit of

0.2 lb/ton BLS

. These SDTs are listed in Table 3 below. The filterabl e PM limits more stringent

than th e NSPS ranged from 0.133 to 0.199 lb/ton BLS and are coupled with wet scrubber SDT

controls. One of these mills also uses limits on its recovery furnace firing rate and pulp

production in addition to a n SDT wet scrubber.

Table 3

. Smelt Dissolving Tanks with Filterable PM Limits More Stringent Than the NSPS

FACILITY NAME CO UNTY ST ATE PROCESS NAME CONTROL

METHOD EMISSION LIMIT

Georgia

- Pacific Corp.

- Port Hudson Operations East Baton

Rouge Parish LA Smelt Tank No. 1 Wet scr ubber 0.133 lb/ton BLS

(calculated)

Georgia

- Pacific

- Port

Hudson Operations East Baton

Rouge Parish LA Smelt Tank No. 2 Wet scrubbers 0.133 lb/ton BLS

(calculated)

Weyerhaeuser Co.

– Marlboro Paper Mill Marlboro SC Smelt Dissolving

Tank S crubber/recover y

furnace firing and

pulp production

limits (4.4 MM lb

BLS/d and 1410

ADTBP/d) 0.199 lb/ton BLS

Mosinee Paper Corp. Marathon WI Smelt T ank, P rocess

# P 30, S tack # S 12 Venturi scrubber 0.18 lb/ton BLS



## III. European Commission Document

A general search of the In ternet was conducted for information on control options

applicable to the kraft pulp mills NSPS review

. The search identified a 20 1 0 European

Commission document entitled Integrated Pollution Prevention and Control ( IPPC ): Reference

Document on Best Availa ble Techniques in the Pulp and Paper Industry

. (EC 20 1 0 ) The

information provided in the document was intended to be used as an input to the determination of

## 7 best available techniques (BAT) in specific cases. Excerpts of BAT from EC 20 1 0 relevant to the

NS PS review are presented in T able 4 below

.

Table 4 . Summary of BAT for Recovery Furnaces and Lime Kilns

SOURCE TRS CONTROL OPTION PM CONTROL OPTION

Recovery

furnaces A higher dry solids content leads to a high

temperature in the furnace and thus a lower

e mission of H 2 

### S and higher emission of sodium;

increase the dry solids content of black liquor by

installing a superconcentrator to achieve a dry

solids content of up to 80%; the achievable dry

solids content depends on the wood species; may

need to install more efficient ESP to compensate

for the increase in PM emissions that will result

from the higher dry solids content; at very high

dry solids content (>80%), will need to collect

and incinerate the considerable sulfur

compounds released from the last eva porator

stage

. Reduce the emissions of dust (PM) from recovery furnaces

using ESPs (used by modern systems); sufficiently

dimensioned ESPs together with good gas flow distribution

into the ESP and an optimized ESP cleaning regime can

reduce levels down to 15

- 20 milligrams per Normal cubic

meter (mg/Nm 3 

### ) on a daily average (dry gas, 273°K, 6%

oxygen [O 2 

### ]) (converts to 0.0057

- 0.0076 grain per dry

standard cubic foot [gr/dscf] at 8% O 2 

### )

. Reduce the emissions of dust (PM) from recovery furnaces

using two

- sta ge dust removal facilities

-- ESP and wet

scrubber (used by older systems); two

- stage dust removal

facilities achieve dust (PM) concentrations in the clean gas

of 10

- 30 mg/Nm 3 

### as a daily average (dry gas, 273°K, 5%

O 2 

### ) (converts to 0.0035

- 0.011 gr/dscf at 8% O 2 

### )

. Lime kilns Improved washing of lime mud in recausticizing

can reduce the residual content of white liquor in

the mud; more efficient washing reduces the

concentration of sulfide in the lime mud, thus

reducing the formation of H 2 

### S in the lime kiln

du ring the reburning process

. Consider process

- integrated measures before installing a

dust removal facility (e.g., proper design of the lime kiln

will minimize dust formation; proper adjustment of flame

shape and position can control the extent of vaporizat ion)

. Consider fuel use; the use of different fuels also affects

dust emissions (e.g., an oil flame results in high sodium

vaporization from the lime)

. Install ESP (prior to scrubber, if there is also a scrubber);

dust emissions of <25 mg/Nm 3 

### as a da ily average (dry gas,

273°K, 5

- 6% O 2 

### ) (converts to <0.0075 gr/dscf at 10% O 2 

### )

are achieved by well

- designed, dimensioned, and

maintained ESPs

.

Source: EC 2010



## IV. STAPPA/ALAPCO Document

STAPPA/ALAPCO issued a document in 2006 to help state and local governme nts

determin e the most effective ways to control emissions of fine particles (PM 2.5 

## ) and PM 2.5



## precursors from sources in their areas as the governments prepare d their State Implementation

Plans (SIPs) for attaining or maintaining the PM 2.5 

## standard. (STAP PA 2006) The sources

examined in the STAPPA 2006 document included industrial and commercial boilers, electric

generating units, pulp and paper mills , cement manufacturing plants , iron and steel

manufacturing plants , petroleum refineries, diesel engine tec hnologies, diesel trucks and buses,

nonroad equipment, light

- duty cars and trucks, airports, marine ports, residential fuel combustion

and electricity use, commercial cooking, and fugitive dust

.

As noted in STAPPA 2006 , t he primary sources of PM 2.5 

## and it s SO 2 

## and NO

x 

## precursors

from pulp and paper mills are recovery furnaces, SDTs, lime kilns and power boilers. The

document further noted that r ecovery furnaces rely on an ESP or a combination of an ESP and

wet scrubber to control PM emissions , while m ost P M emissions from lime kilns and SDTs are

controlled with wet scrubbers

— typically, venturi scrubbers

. ( STAPPA 2006 )

STAPPA 2006 noted that o pportunities exist to reduce current PM emissions levels by

upgrading or replacing older wet scrubbers or ESPs

. For example, on recovery furnaces, older

## 8 model ESPs have collection efficiencies close to 90 percent, while newer model ESPs have

collection efficiencies greater than 99 percent. The document stated that t he cost of retrofitting a

recovery furnace with an ESP is heavily influenced by site

- specific factors ; t he document also

noted that l ime kilns installed in the past 10 years are likely to have an ESP control system and

indicated that e missions from older units can be reduced by replacing wet scrubbers with ESP s.

(STAPPA 2006)

Table 5 below from STAPPA 2006 provides one estimate of the ESP retrofit costs for a

DCE recovery furnace and an NDCE recovery furnace

. Capital costs range from $18.4 to $29.3

million. Table 5 also shows estimated costs for implementing t his type of replacement for lime

kilns to meet the 0.01 gr/dscf limit for new sources set in 40 CFR part 63, subpart MM

-- the

national emission standard for hazardous air pollutants (NESHAP) for chemical recovery

combustion sources at kraft, soda, sulfite, and stand

- alone semichemical pulp mills (STAPPA

2006)

Table 5 . Estimated ESP Retrofit Costs

EQUIPMENT CHARACTERISTICS CAPITAL COST ANNUAL COST

NDCE recovery furnace , 3.7 MM lb BLS/d $29.3 million $1.9 million

DCE recovery furnace , 1.7 MM lb BLS/d $18.4 million $1.2 million

Lime kiln, 270 ton CaO/d $3.4 million $0.2 million

Notes: BLS = black liquor solids ; CaO = reburned lime product

Source: STAPPA 2006

V. Conclusions

The RBLC and documents from the European Commission and STAPPA/ALAPCO were

reviewed to identify emission limits and/or control measures more stringent than the current kraft

pulping NSPS limits for TRS and PM.

For recovery fu rnaces, the control measures primarily included recovery furnace design

and operation for TRS control and ESPs for P M control. TRS emission limit s more stringent than

the NSPS (3 to 4 ppm at 8 percent O 2 

## ) were noted for 2 mills. Filterable PM emission limits

more stringent than the NSPS ( 0.02 to 0.036 gr/dscf at 8 percent O 2 

## ) were noted for 9 mills.

For lime kilns, th e control measures primarily included kiln design and operation and wet

scrubbers for TRS control and wet scrubbers and ESPs for PM control

. A TRS emission limit

more stringent than the NSPS (6.5 ppm at 8 percent O 2 

## ) w as noted for 1 mill

. Filterable PM

e mission limits more stringent than the NSPS (0.01 to 0.05 gr/dscf at 10 percent O 2 

## ) were noted

for 3 mills.

For SDTs, the control measures primarily included recovery furnace design and operation

and SDT wet scrubbers for TRS control and SDT wet scrubber s for PM control

. TRS emission

limits more stringent than the NSPS (0.03 to 0.032 lb/ton BLS) were noted for 2 mills. Filterable

PM emission limits more stringent than the NSPS ( 0.133 to 0.199 lb/ton BLS) were noted for 3

mills

.

## 9 VI. References

EC 20 1 0 Europ ean Commission

. Integrated Pollution Prevention and Control

(IPPC): Reference Document on Best Available Techniques in the Pulp

and Paper Industry

. April 20 1 0

.

STAPPA 2006 State and Territorial Air Pollution Program Administrators and the

Association of Local Air Pollution Control Offi cials

(STAPPA/ALAPCO)

. Controlling Fine Particulate Matter Under the

Clean Air Act: A Menu of Options. March 2006

.

## Appendix A

Summary of RACT/BACT/LAER Clearinghouse Search Results for Process Type Code

30.200 (Kraft Pulp & Paper Processes) for TRS and Other Similarly

- Controlled PollutantsRTI SORTCODE RBLCID CORPORATE_OR_COMPANY_NAME FACILITY_COUNTYFACILITY_STATERTI ProcessCode PROCESS_NAME POLLUTANT CONTROL_METHOD_DESCRIPTIONEMISSION_LIMIT_1EMISSION_LIMIT_1_UNITEMISSION_LIMIT_1_AVGE_TIME_CONDITION1823 TN-0128 PACKAGING CORPORATION OF AMERICA HARDIN TN Digester DIGESTERS, TURPENTINE RECOVERY, ANDEVAPORATOR SYSSulfur, Total Reduced (TRS)EMISSIONS ARE ROUTED TO THE LIME KILNS FORTHERMAL OXIDATION01822 TN-0128 PACKAGING CORPORATION OF AMERICA HARDIN TN Digester DIGESTERS, TURPENTINE RECOVERY, ANDEVAPORATOR SYSVolatile Organic Compounds (VOC)EMISSIONS ARE ROUTED TO THE LIME KILNS FORTHERMAL OXIDATION.01970AR-0081DELTA NATURAL KRAFTJEFFERSONARDigesterDIGESTERVolatile Organic Compounds (VOC)EMISSIONS TO THE LIME KILN FOR THERMAL OXIDATION2.8LB/H1971AR-0081DELTA NATURAL KRAFTJEFFERSONARDigesterDIGESTERMethanolROUTED TO LIME KILN FOR THERMAL OXIDATION0.08LB/H1973AR-0081DELTA NATURAL KRAFTJEFFERSONARDigesterDIGESTERSulfur, Total Reduced (TRS)ROUTED TO LIME KILN FOR THERMAL OXIDATION0.1LB/H514MS-0075GEORGIA PACIFIC CORP.LAWRENCEMSDigesterDIGESTER SYSTEMVolatile Organic Compounds (VOC)EMISSIONS COLLECTED AND COMBUSTED IN THE NCG SYSTEM0SEE NOTE1975 AR-0088 GEORGIA PACIFIC CORPORATION ASHLEY AR Digester DIGESTERS (SN-59) Sulfur, Total Reduced (TRS) INCINERATOR CONTROLS DIGESTER RELIEF AND BLOW GAS EMISSIONS.HOWEVER, PERMITTED EMISSIONS ARE DURING FILL AND AREUNCONTROLLED. CONTROLLED EMISSIONS ARE BASED UPON 8.7 LBTRS/ADTP (FROM NCASI 858, TABLES 9A-9F AND 9J)4.3 LB/H1974 AR-0088 GEORGIA PACIFIC CORPORATION ASHLEY AR Digester DIGESTERS (SN-59) Volatile Organic Compounds (VOC) INCINERATORCONTROLS DIGESTER RELIEF AND BLOW GAS EMISSIONS.HOWEVER, PERMITTED EMISSIONS ARE DURING FILL AND AREUNCONTROLLED.CONTROLLED EMISSIONS ARE BASED UPON 15.5 LBVOC/ADTP (FROM NCASI 858, TABLES 9A-9F AND 9J)55.9 LB/H48 AL-0237 INTERNATIONAL PAPER CORPERATION -COURTLAND MILLLAWRENCE AL Digester NO. 3 DIGESTION SYSTEM Sulfur, TotalReduced (TRS) VOC WAS INCLUDED IN THIS PROCESS, COLLECT & INCINERATE LVHC &HVLC'S0 SEE NOTE1951 GA-0113 INTERNATIONAL PAPER RICHMOND GA Digester NO. 3DIGESTER SYSTEM Volatile Organic Compounds (VOC) CURRENT NCGCOLLECTION SYSTEM ROUTES EMISSIONS TO THE LIMEKILNS. NO NEW CONTROLS FEASIBLE. FACILITY PRODUCTION LIMIT0 SEE NOTE1952GA-0113INTERNATIONAL PAPERRICHMONDGADigesterNO. 3 DIGESTER SYSTEMSulfur, Total Reduced (TRS)8PPM @ 10% O21993 LA-0205 INTERNATIONAL PAPER MOREHOUSE LA Digester A & B-LINE DIGESTER SYSTEMS Sulfur, Total Reduced (TRS) EMISSIONS ROUTED TO EXISTING LIME KILN OR NCG INCINERATOR0 SEE NOTE1994 LA-0205 INTERNATIONAL PAPER MOREHOUSE LA Digester A & B-LINE DIGESTER SYSTEMS Volatile Organic Compounds(VOC) EMISSIONS ROUTED TO EXISTING LIME KILN OR NCG INCINERATOR 0 SEE NOTE448 LA-0207 INTERNATIONAL PAPER CO DESOTO LA Digester DIGESTER SYSTEMS, PRIMARY,SECONDARY, & SEMI-CHEMICALSulfur, Total Reduced (TRS) THERMAL INCINERATION IN THE LIME KILN OR NCG INCINERATOR 0449 LA-0207 INTERNATIONAL PAPER CO DESOTO LA Digester DIGESTER SYSTEMS, PRIMARY,SECONDARY, & SEMI-CHEMICALVolatile Organic Compounds (VOC) THERMAL INCINERATION INTHE LIME KILN OR NCG INCINERATOR 0 SEE NOTE1976FL-0254STONE CONTAINER CORPORATIONBAYFLDigesterBATCH DIGESTER SYSTEM (21 UNITS)Sulfur, Total Reduced (TRS)ADJUSTMENT OF THE PH OF THE BOILER'S SCRUBBERWATER TO8.05PPM @ 10% O2see noteFL-0254STONE CONTAINER CORPORATIONDigesterBATCH DIGESTER SYSTEM (21 UNITS)Sulfur, Total Reduced (TRS)ADJUSTMENT OF THE PH OF THE BOILERS SCRUBBERWATER TOPRIOR TO INCINERATION OF TRS5PPM @ 10% O2see note49 AL-0237 INTERNATIONAL PAPER CORPERATION -COURTLAND MILLLAWRENCE AL Evaporator NO. 3 EVAPORATION SYSTEM Sulfur, Total Reduced (TRS) VOC WAS ANOTHER POLLUTANT IN THIS PROCESS, COLLECT &INCINERATE HVLC & LVHC GASES0 SEE NOTE458 LA-0207 INTERNATIONAL PAPER CO DESOTO LA Evaporator NOS.1 & 2 EVAPORATOR ANDCONCENTRATOR SYSTEMSSulfur, Total Reduced (TRS) THERMAL INCINERATION IN THE LIME KILN OR NCG INCINERATOR 0 SEE NOTE459 LA-0207 INTERNATIONAL PAPER CO DESOTO LA Evaporator NOS.1 & 2 EVAPORATOR ANDCONCENTRATOR SYSTEMSVolatile Organic Compounds (VOC) THERMAL INCINERATION INTHE LIME KILN OR NCG INCINERATOR 0 SEE NOTE489 MS-0075 GEORGIA PACIFIC CORP. LAWRENCE MS Evaporator MULTIPLE-EFFECT EVAPORATORSYSTEMSVolatile Organic Compounds (VOC) INCINERATERS: LIME KILNOR THERMAL OXIDIZER.0 SEE NOTE490 MS-0075 GEORGIA PACIFIC CORP. LAWRENCE MS Evaporator MULTIPLE-EFFECT EVAPORATORSYSTEMSHydrogen Sulfide INCINERATERS: LIME KILN OR THERMAL OXIDIZER.0 SEE NOTE491 MS-0075 GEORGIA PACIFIC CORP. LAWRENCE MS Evaporator MULTIPLE-EFFECT EVAPORATORSYSTEMSOdorINCINERATERS: LIME KILN OR THERMAL OXIDIZER.0 SEE NOTE1979 LA-0205 INTERNATIONAL PAPER MOREHOUSE LA Evaporator EVAPORATOR SYSTEMS Volatile Organic Compounds (VOC) EMISSIONS ROUTED TO EXISTING LIME KILN OR NCG INCINERATOR 0 SEE NOTE1980 LA-0205 INTERNATIONAL PAPER MOREHOUSE LA Evaporator EVAPORATOR SYSTEMS Sulfur, Total Reduced (TRS) EMISSIONS ROUTED TO EXISTING LIME KILN OR NCG INCINERATOR 0 SEE NOTE292LA-0122INTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLANCGNCG INCINERATORSulfur, Total Reduced (TRS)0.18LB/H293LA-0122INTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLANCGNCG INCINERATORVolatile Organic Compounds (VOC)6.1LB/H562 SC-0083 WEYERHAEUSER COMPANY MARLBORO SC NCG INCINERATOR, NCG Sulfur, Total Reduced (TRS)MINIMUM TEMPERATURE: 1200 DEGREES F; AND 0.5 SECONDRESIDENCE TIME.PULP PRODUCTION LIMIT(1410ADTBP/D)0 see notes563 SC-0083 WEYERHAEUSER COMPANY MARLBORO SC NCG INCINERATOR, NCG Volatile Organic Compounds (VOC)MINIMUM TEMPERATURE AND RESIDENCE TIME/PULPPRODUCTION LIMIT (1410 ADTBP/D)6.1 LB/H728TX-0515INTERNATIONAL PAPER COMPANYCASSTXNCGNCG OXIDATION UNIT SCRUBBERSulfur, Total Reduced (TRS)0.99LB/H729TX-0515INTERNATIONAL PAPER COMPANYCASSTXNCGNCG OXIDATION UNIT SCRUBBERVolatile Organic Compounds (VOC)0.12LB/H1802 LA-0158 STONE CONTAINER CORPORATION JACKSON PARISH LA NCG NCG/SOG THERMAL OXIDIZER MethanolPROPER COMBUSTION AND OPERATION OF THEINCINERATOR.19.7 LB/H7 OK-0103 WEYERHAEUSER MCCURTAIN OK LK LIME KILNVolatile Organic Compounds (VOC) GOOD COMBUSTION PRACTICES0.26 LB/T LB/TON CAO, MONTHLYAVERAGE179LA-0122INTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLALKLIME KILNSulfur, Total Reduced (TRS)VENTURI SCRUBBER USING FRESH WATER6.5PPM180LA-0122INTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLALKLIME KILNVolatile Organic Compounds (VOC)VENTURI SCRUBBER USING FRESH WATER8.3LB/H439LA-0201WEYERHAEUSER CONATCHITOCHESLALKLIME KILN NO. 2Sulfur, Total Reduced (TRS)PROPER KILN DESIGN AND OPERATION WITH OPTIMIZED MUD WASHING8PPM @ 10% O2LA-0201WEYERHAEUSER CONATCHITOCHESLIME KILN NO. 2Sulfur, Total Reduced (TRS)PROPER KILN DESIGN AND OPERATION WITH OPTIMIZED MUD WAPPM @ 10% O2440LA-0201WEYERHAEUSER CONATCHITOCHESLALKLIME KILN NO. 2Volatile Organic Compounds (VOC)PROPER KILN DESIGN AND GOOD COMBUSTION PRACTICES50PPM @ 10% O2478MS-0075GEORGIA PACIFIC CORP.LAWRENCEMSLKLIME KILNVolatile Organic Compounds (VOC)GOOD COMBUSTION PRACTICES0SEE NOTE537 NC-0092 INTERNATIONAL PAPER COMPANY COLUMBUS NC LK LIME KILNSulfur, Total Reduced (TRS)ESP AND A FIXED THROAT SPRAY VENTURI-TYPE WETSCRUBBER8 PPM @ 10% O2598 TX-0263 DONAHUE INDUSTRIES, INC. ANGELINA TX LK LIME KILNSulfur, Total Reduced (TRS) SCRUBBER0.9 LB/H682 TX-0485 INLAND PAPERBOARD AND PACKAGING INC ORANGE TX LK LIME KILNVolatile Organic Compounds (VOC) BEST MANAGEMENT PRACTICESFOR PULP WASHING, AND THEREDUCTION OF VOC ADDITIVES TO THE PAPERMAKING SYSTEM4.78 LB/H2825 MS-0077 GEORGIA PACIFIC CORPORATION LAWRENCE MS LK LIME KILNSulfur, Total Reduced (TRS) WET (VENTURI) SCRUBBER WITH OPTIMAL MUD WASHING 20 PPMV @ 10% O2 SEE NOTEA-1RTI SORTCODE RBLCID CORPORATE_OR_COMPANY_NAME FACILITY_COUNTYFACILITY_STATERTI ProcessCode PROCESS_NAME POLLUTANT CONTROL_METHOD_DESCRIPTIONEMISSION_LIMIT_1EMISSION_LIMIT_1_UNITEMISSION_LIMIT_1_AVGE_TIME_CONDITION9OK-0103WEYERHAEUSERMCCURTAINOKRFCHEMICAL RECOVERY FURNACEVolatile Organic Compounds (VOC)STAGED COMBUSTION AND NON-DIRECT CONTACT EVAPORATORS40PPM @ 8% O2MONTHLY AVERAGE15 AR-0099 GEORGIA-PACIFIC CORPORATION ASHLEY AR RF 8R RECOVERY BOILERVolatile Organic Compounds (VOC) BOILER DESIGN AND COMBUSTION CONTROL25.9 LB/H58 AR-0027 POTLATCH CORPORATION - CYPRESS BENDMILLDESHA AR RF FURNACE, RECOVERY Sulfur, Total Reduced (TRS) PROPER DESIGN AND OPERATION5 PPMDV88 FL-0302 GEORGIA-PACIFIC CONSUMER OPERATIONSLLCPUTNAM FL RF NO. 4 RECOVERY BOILER Volatile Organic Compounds(VOC) NEW PFA SYSTEM (QUARTENARY) COMBUSTION IMPROVEMENTS0.2 LB/T94 FL-0311 BUCKEYE FLORIDA, LP TAYLOR FL RF RECOVERY BOILER NO.2 Particulate matter, total < 10 μ (TPM10) THE EXISTING NOS. 2 AND 3 RECOVERY BOILERS WILL BE PHYSICALLYMODIFIED AND CONVERTED FROM DCE UNITS TO LOW-ODOR, NDCEUNITS (RTI COPIED FROM "PERMIT_NOTES" IN RBLC RESULTS)0.03 GR/DSCF @ 8% O2106GA-0114TEMPLE INLAND, INC.FLOYDGARFRECOVERY FURNACE, BLS FUELSulfur, Total Reduced (TRS)SYSTEM DESIGN AND GOOD OPERATION PRACTICES5PPM @ 8% O2107GA-0114TEMPLE INLAND, INC.FLOYDGARFRECOVERY FURNACE, BLS FUELVolatile Organic Compounds (VOC)STAGED COMBUSTION AND GOOD COMBUSTION PRACTICES0.04LB/MMBTU108GA-0114TEMPLE INLAND, INC.FLOYDGARFRECOVERY FURNACE, BLS FUELHydrogen SulfideSYSTEM DESIGN AND GOOD OPERATION PRACTICES4PPM @ 8% O2120GA-0114TEMPLE INLAND, INC.FLOYDGARFRECOVERY FURNACE, FUEL OILVolatile Organic Compounds (VOC)STAGED COMBUSTION AND GOOD COMBUSTION PRACTICES0.02LB/MMBTU123 KY-0085 MEADWESTVACO KENTUCKY, INC BALLARD KY RF RECOVERY FURNACE Sulfur, Total Reduced (TRS)GOOD ENGINEERING PRACTICE, CEM MONITORING, WETSCRUBBER40 PPMV @ 8% O2 for 60 min in a 24 h period185LA-0122INTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLARFRECOVERY BOILER NO.1 AND NO.2Sulfur, Total Reduced (TRS)GOOD PROCESS CONTROLS5PPMV186LA-0122INTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLARFRECOVERY BOILER NO.1 AND NO.2Volatile Organic Compounds (VOC)GOOD PROCESS CONTROLS, NDCE DESIGN25.6LB/H452 LA-0207 INTERNATIONAL PAPER CO DESOTO LA RF RECOVERY BOILERS NO. 1 & 2 (EQT036& 037)Sulfur, Total Reduced (TRS) PROPER DESIGN AND GOOD COMBUSTION PRACTICES 25.1 T/YR ANNUAL MAXIMUM453 LA-0207 INTERNATIONAL PAPER CO DESOTO LA RF RECOVERY BOILERS NO. 1 & 2 (EQT036& 037)Volatile Organic Compounds (VOC) PROPER DESIGN AND GOODCOMBUSTION PRACTICES 32.1 LB/H HOURLY MAXIMUM348LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLARFRECOVERY FURNACE NO. 1Sulfur, Total Reduced (TRS)UPGRADE BLOX SYSTEM4.53LB/H364LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLARFRECOVERY FURNACE NO. 2Sulfur, Total Reduced (TRS)UPGRADE BLOX SYSTEM6.13LB/H429 LA-0201 WEYERHAEUSER CO NATCHITOCHES LA RF RECOVERY BOILER NO. 3Sulfur, Total Reduced (TRS) PROPER BOILER DESIGN AND OPERATION3 PPM @ 8% O2430LA-0201WEYERHAEUSER CONATCHITOCHESLARFRECOVERY BOILER NO. 3Volatile Organic Compounds (VOC)PROPER BOILER OPERATION10PPM @ 8% O2515MS-0078GEORGIA PACIFIC CORPORATIONLAWRENCEMSRFBOILER, NO. 1 RECOVERYSulfur, Total Reduced (TRS)COMBUSTION CONTROL31.5LB/H516MS-0078GEORGIA PACIFIC CORPORATIONLAWRENCEMSRFBOILER, NO. 1 RECOVERYVolatile Organic Compounds (VOC)COMBUSTION CONTROL0SEE NOTE531NC-0092INTERNATIONAL PAPER COMPANYCOLUMBUSNCRFRECOVERY BOILERVolatile Organic Compounds (VOC)GOOD COMBUSTION PRACTICE37LB/HNC-0092INTERNATIONAL PAPER COMPANYCOLUMBUSRECOVERY BOILERVolatile Organic Compounds (VOC)GOOD COMBUSTION PRACTICE555NC-0108INTERNATIONAL PAPERHALIFAXNCRFNO. 7 RECOVERY FURNACESulfur, Total Reduced (TRS)FURNACE DESIGN AND COMBUSTION OPTIMIZATION5PPM8% O2 12-HOUR556NC-0108INTERNATIONAL PAPERHALIFAXNCRFNO. 7 RECOVERY FURNACEVolatile Organic Compounds (VOC)FURNACE DESIGN AND COMBUSTION OPTIMIZATION50PPM8% O2 24-HOUR569 SC-0083 WEYERHAEUSER COMPANY MARLBORO SC RF NO. 1 RECOVERY FURNACESulfur, Total Reduced (TRS) LOW ODOR RECOVERY FURNACE/GOOD COMBUSTIONPRACTICE/RECOVERY FURNACE FIRING RATE AND PULPPRODUCTION LIMITS(4.4MM LB BLS/D AND1410ADTBP/D)4 PPM @ 8% O2570 SC-0083 WEYERHAEUSER COMPANY MARLBORO SC RF NO. 1 RECOVERY FURNACEVolatile Organic Compounds (VOC) LOW ODOR RECOVERY FURNACE/GOOD COMBUSTIONCONTROL/RECOVERY FURNACE FIRING RATE AND PULPPRODUCTION LIMITS(4.4MM LB BLS/D AND1410ADTBP/D)40 PPM @ 8% O2777*VA-0306MEADWESTVACOCOVINGTONVARFPAPER BOARD MILLVolatile Organic Compounds (VOC)TRS AND AN ESP GOOD COMBUSTION PRACTICES38.4LB/H789 WA-0303 LONGVIEW FIBRE PAPER AND PACKAGING, INC WA RF RECOVERY FURNACE 18 Volatile Organic Compounds (VOC)GOOD COMBUSTION CONTROL OF FLAME TEMPERATURE ANDEXCESS AIR.612 T/YR842 WA-0303 LONGVIEW FIBRE PAPER AND PACKAGING, INC WA RF RECOVERY FURNACE 19 Volatile Organic Compounds (VOC)GOOD COMBUSTION CONTROL OF FLAME TEMPERATURE ANDEXCESS AIR.1020 T/YR877 WI-0141 MOSINEE PAPER CORPORATION MARATHON WI RF RECOVERY BOILER, PROCESS #B21, STACK#S11Formaldehyde THE PERMITTEE SHALL DEMONSTRATE GOOD COMBUSTIONOPERATIONS BY MONITORING THE TEMPERATURE OF THE GASSTREAM AND THE IN-STU PERCENT OFOXYGEN OF THE FLUE GAS.0.146 LB/H878 WI-0141 MOSINEE PAPER CORPORATION MARATHON WI RF RECOVERY BOILER, PROCESS #B21, STACK#S11Sulfur, Total Reduced (TRS)THE PERMITTEE SHALL CONTROL TRS EMISSION USING GOODCOMBUSTION CONTROL. THE PERMITTEE SHALL DEMONSTRATE GOODCOMBUSTION OPERATIONS BY MONITORING THE TEMPERATURE OFTHE GAS STREAM.7.23 T/YR886 WI-0208 DOMTAR INDUSTRIES INC. WOOD WI RF KRAFT BLACK LIQUORRECOVERYFURNACE, B14Sulfur, Total Reduced (TRS) GOOD OPERATING PRACTICES5 PPMDV @ 8% O2 12 HOUR AVG. LIMIT887 WI-0208 DOMTAR INDUSTRIES INC. WOOD WI RF KRAFT BLACK LIQUORRECOVERYFURNACE, B14Volatile Organic Compounds (VOC) GOOD COMBUSTION CONTROL65 PPMDV @ 8% O2 3 HOUR AVG. LIMIT287LA-0122INTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLASDTSMELT DISSOLVING TANK NO.1 AND NO.2Volatile Organic Compounds (VOC)GOOD PROCESS CONTROLS, NDCE DESIGN57.9LB/H379LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLASDTSMELT TANK NO. 2Sulfur, Total Reduced (TRS)WET SCRUBBER0.63LB/H434 LA-0201 WEYERHAEUSER CO NATCHITOCHES LA SDT SMELT TANK NO.3 Sulfur, Total Reduced (TRS) PROPER BOILER DESIGN AND OPERATION3 PPM @ 8% O2*435LA-0201WEYERHAEUSER CONATCHITOCHESLASDTSMELT TANK NO. 3Volatile Organic Compounds (VOC)PROPER BOILER OPERATION10PPM @ 8% O2*576 SC-0083 WEYERHAEUSER COMPANY MARLBORO SC SDT SMELT DISSOLVING TANK Sulfur, Total Reduced (TRS)LOW SULFIDE WATER SCRUBBER/RECOVERY FURNACE FIRING RATEAND PULP PRODUCTION RATE (4.4 MM LB BLS/D AND 1410 ADTBP/D)AND PULP PRODUCTIONLIMITS0.03 LB/T BLS577 SC-0083 WEYERHAEUSER COMPANY MARLBORO SC SDT SMELT DISSOLVING TANK Volatile Organic Compounds (VOC)RECOVERY FURNACE FIRING RATE AND PULP PRODUCTION LIMITS (4.4MM LB BLS/D AND 1410 ADTBP/D)0.16 LB/T BLSNotes:1. Highlighted in yellow those limits more stringent than NSPS.2. Additional emission limits of 5 ppmv at 8% O2for Recovery Furnaces Nos. 1 and 2 atGeorgia-Pacific mill in East Baton Rouge, LA.3. Additional emission limit of 35 ppm, expressed as H2S on a dry gas basis corrected to 8%O2on a 12-hour average basis.A-2CORPORATE_OR_COMPANY_NAME FACILITY_COUNTYFACILITY_STATEPACKAGING CORPORATION OF AMERICA HARDIN TNPACKAGING CORPORATION OF AMERICA HARDIN TNDELTA NATURAL KRAFTJEFFERSONARDELTA NATURAL KRAFTJEFFERSONARDELTA NATURAL KRAFTJEFFERSONARGEORGIA PACIFIC CORP.LAWRENCEMSGEORGIA PACIFIC CORPORATION ASHLEY ARGEORGIA PACIFIC CORPORATION ASHLEY ARINTERNATIONAL PAPER CORPERATION -COURTLAND MILLLAWRENCE ALINTERNATIONAL PAPER RICHMOND GAINTERNATIONAL PAPERRICHMONDGAINTERNATIONAL PAPER MOREHOUSE LAINTERNATIONAL PAPER MOREHOUSE LAINTERNATIONAL PAPER CO DESOTO LAINTERNATIONAL PAPER CO DESOTO LASTONE CONTAINER CORPORATIONBAYFLCASE-BYCASE_BASISOTHER_APPLICABLE_REQUIREMENTSPERCENT_EFFICIENCYEMISSION_LIMIT_2EMISSION_LIMIT_2_UNITEMISSION_LIMIT_2_AVGE_TIME_CONDITIONSTANDARD_EMISSION_LIMITSTANDARD_EMISSION_LIMIT_UNITSTANDARD_LIMIT_AVGE_TIME_CONDITIONBACT-PSD0 00BACT-PSD0 00BACT-PSDSIP015.2T/YR0BACT-PSDMACT920.43T/YR92% REDUCTIONBY WEIGHTBACT-PSDSIP00.4T/YR40PPMV @ 10% O2SEE NOTEBACT-PSD000BACT-PSD NSPS , OPERATINGPERMIT99.9 18.9 T/YR0BACT-PSD OPERATING PERMIT 99.9 244.7 T/YR0BACT-PSD NESHAP 0 00MACT 0 00NESHAP008PPM @ 10% O2BACT-PSD NSPS , OPERATINGPERMIT0 00BACT-PSD MACT , OPERATINGPERMIT0 00BACT-PSD NSPS , OPERATINGPERMIT0 00BACT-PSD MACT , OPERATINGPERMIT0 00Other Case-by-8005PPM @ 10% O2STONE CONTAINER CORPORATIONBAYFLINTERNATIONAL PAPER CORPERATION -COURTLAND MILLLAWRENCE ALINTERNATIONAL PAPER CO DESOTO LAINTERNATIONAL PAPER CO DESOTO LAGEORGIA PACIFIC CORP. LAWRENCE MSGEORGIA PACIFIC CORP. LAWRENCE MSGEORGIA PACIFIC CORP. LAWRENCE MSINTERNATIONAL PAPER MOREHOUSE LAINTERNATIONAL PAPER MOREHOUSE LAINTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLAINTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLAWEYERHAEUSER COMPANY MARLBORO SCWEYERHAEUSER COMPANY MARLBORO SCINTERNATIONAL PAPER COMPANYCASSTXINTERNATIONAL PAPER COMPANYCASSTXSTONE CONTAINER CORPORATION JACKSON PARISH LAWEYERHAEUSER MCCURTAIN OKINTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLAINTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLAWEYERHAEUSER CONATCHITOCHESLAOther Case-byCase8005PPM @ 10% O2BACT-PSD NESHAP 0 00BACT-PSD OPERATING PERMIT ,NSPS0 00BACT-PSD MACT 0 00BACT-PSD0 00BACT-PSD0 00BACT-PSD0 00BACT-PSD MACT , OPERATINGPERMIT0 00BACT-PSD NSPS , OPERATINGPERMIT0 00BACT-PSD00.8T/YR0BACT-PSD02.8T/YR0BACT-PSD0 00BACT-PSD0 26.7 T/YR0BACT-PSD04.36T/YR0BACT-PSD00.53T/YR0BACT-PSD0 86.4 T/YR0BACT-PSD0 00BACT-PSD020.8T/YR0BACT-PSD036.3T/YR0BACT-PSDNSPS , OPERATING008PPM @ 10% O2*WEYERHAEUSER CONATCHITOCHESLAWEYERHAEUSER CONATCHITOCHESLAGEORGIA PACIFIC CORP.LAWRENCEMSINTERNATIONAL PAPER COMPANY COLUMBUS NCDONAHUE INDUSTRIES, INC. ANGELINA TXINLAND PAPERBOARD AND PACKAGING INC ORANGE TXGEORGIA PACIFIC CORPORATION LAWRENCE MSBACT-PSDNSPS , OPERATINGPERMIT008PPM @ 10% O2*BACT-PSDOPERATING PERMIT0050PPM @ 10% O2*BACT-PSD000N/A NSPS 0 00Other Case-byCase0 3.8 T/YR0LAER0 21.03 T/YR0BACT-PSD0 020 PPMV @ 10% O2A-3CORPORATE_OR_COMPANY_NAME FACILITY_COUNTYFACILITY_STATEPACKAGING CORPORATION OF AMERICAHARDINTNWEYERHAEUSERMCCURTAINOKGEORGIA-PACIFIC CORPORATION ASHLEY ARPOTLATCH CORPORATION - CYPRESS BENDMILLDESHA ARGEORGIA-PACIFIC CONSUMER OPERATIONSLLCPUTNAM FLBUCKEYE FLORIDA, LP TAYLOR FLTEMPLE INLAND, INC.FLOYDGATEMPLE INLAND, INC.FLOYDGATEMPLE INLAND, INC.FLOYDGATEMPLE INLAND, INC.FLOYDGAMEADWESTVACO KENTUCKY, INC BALLARD KYINTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLAINTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLAINTERNATIONAL PAPER CO DESOTO LAINTERNATIONAL PAPER CO DESOTO LAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAWEYERHAEUSER CO NATCHITOCHES LAWEYERHAEUSER CONATCHITOCHESLAGEORGIA PACIFIC CORPORATIONLAWRENCEMSGEORGIA PACIFIC CORPORATIONLAWRENCEMSINTERNATIONAL PAPER COMPANYCOLUMBUSNCCASE-BYCASE_BASISOTHER_APPLICABLE_REQUIREMENTSPERCENT_EFFICIENCYEMISSION_LIMIT_2EMISSION_LIMIT_2_UNITEMISSION_LIMIT_2_AVGE_TIME_CONDITIONSTANDARD_EMISSION_LIMITSTANDARD_EMISSION_LIMIT_UNITSTANDARD_LIMIT_AVGE_TIME_CONDITIONBACT-PSD7000BACT-PSD SIP , OPERATINGPERMIT0 98.6 T/YR0BACT-PSD0 5.45 LB/H5 PPMBACT-PSD0 21 LB/H THC DETERMINED ASMETHANE0BACT-PSD0 31.6 LB/H0BACT-PSDSIP , NSPS000BACT-PSD000BACT-PSD000BACT-PSD000Other Case-byCase0 15 PPMV @8% O2 24 h avg0BACT-PSD024.2T/YR0BACT-PSD0112.1T/YR0BACT-PSD OPERATING PERMIT 0 5 PPMVD @ 8%O2SHORT TERM 2.41 PPMVD @ 8% O2 ANNUAL AVERAGEBACT-PSD OPERATING PERMIT 0 133.7 T/YR ANNUAL MAXIMUM 0BACT-PSD019.84T/YR0BACT-PSD026.85T/YR0BACT-PSD NSPS , OPERATINGPERMIT0 03 PPM @ 8% O2*BACT-PSDOPERATING PERMIT0010PPM @ 8% O2*BACT-PSD0138T/YR0BACT-PSD000BACT-PSD000INTERNATIONAL PAPER COMPANYCOLUMBUSNCINTERNATIONAL PAPERHALIFAXNCINTERNATIONAL PAPERHALIFAXNCWEYERHAEUSER COMPANY MARLBORO SCWEYERHAEUSER COMPANY MARLBORO SCMEADWESTVACOCOVINGTONVALONGVIEW FIBRE PAPER AND PACKAGING, INC WALONGVIEW FIBRE PAPER AND PACKAGING, INC WAMOSINEE PAPER CORPORATION MARATHON WIMOSINEE PAPER CORPORATION MARATHON WIDOMTAR INDUSTRIES INC. WOOD WIDOMTAR INDUSTRIES INC. WOOD WIINTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAWEYERHAEUSER CO NATCHITOCHES LAWEYERHAEUSER CONATCHITOCHESLAWEYERHAEUSER COMPANY MARLBORO SCBACT-PSD000000000BACT-PSD0 23.75 T/YR0BACT-PSD0 112 T/YR0BACT-PSDOPERATING PERMIT0140T/YR38.4LB/HBACT-PSD0 00BACT-PSD0 00BACT-PSD0 00BACT-PSD0 05 PPM @ 8% O2N/A NSPS 0 00Other Case-byCase0 00BACT-PSD0254T/YR0BACT-PSD02.76T/YR0.032LB/T BLSCALCULATEDBACT-PSD NSPS , OPERATINGPERMIT0 00BACT-PSDOPERATING PERMIT000BACT-PSD0 12 T/YR0 Not AvailableWEYERHAEUSER COMPANY MARLBORO SCNotes:1. Highlighted in yellow those limits more stringent than NSPS.2. Additional emission limits of 5 ppmv at 8% O2for Recovery Furnaces Nos. 1 and 2 atGeorgia-Pacific mill in East Baton Rouge, LA.3. Additional emission limit of 35 ppm, expressed as H2S on a dry gas basis corrected to 8%O2on a 12-hour average basis.BACT-PSD0 64.2 T/YR0A-4

## Appendix B

Summary of RACT/BACT/LAER Clearinghouse Search Results for Process Type Code

30.200 (Kraft Pulp & Paper Processes) for Filterable PM and Other Similarly

- Controlled

Pollutant sRTISORTCODE RBLCID CORPORATE_OR_COMPANY_NAME FACILITY_COUNTYFACILITY_STATERTIProcessCode PROCESS_NAME POLLUTANT CONTROL_METHOD_DESCRIPTIONEMISSION_LIMIT_1EMISSION_LIMIT_1_UNITEMISSION_LIMIT_1_AVGE_TIME_CONDITION91 FL-0302 GEORGIA-PACIFIC CONSUMER OPERATIONSLLCPUTNAM FL LK NO. 4 LIME KILN Particulate Matter (PM) EXISTING MECHANICAL PRE-CLEANER CYCLONESFOLLOWED BY A VENTURI WET SCRUBBER SYSTEM.0.55 LB/T126KY-0085MEADWESTVACO KENTUCKY, INCBALLARDKYLKLIME KILNParticulate Matter (PM)SCRUBBER1LB/T ADPlb/t unbleached air dried pulp183LA-0122INTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLALKLIME KILNParticulate matter, filterable < 10 μ (FPM10)VENTURI SCRUBBER USING CAUSTIC SOLUTION39.2LB/H383LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLALKLIME KILN NO. 1Particulate Matter (PM)WET SCRUBBERS25.76LB/H387LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLALKLIME KILN NO. 1Particulate matter, filterable < 10 μ (FPM10)WET SCRUBBERS25.76LB/H389LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLALKLIME KILN NO. 2Particulate Matter (PM)ELECTROSTATIC PRECIPITATOR & VENTURI SCRUBBER20.45LB/H393LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLALKLIME KILN NO. 2Particulate matter, filterable < 10 μ (FPM10)ELECTROSTATIC PRECIPITATOR & VENTURI SCRUBBER20.45LB/H442LA-0201WEYERHAEUSER CONATCHITOCHESLALKLIME KILN NO. 2Particulate matter, filterable < 10 μ (FPM10)ELECTROSTATIC PRECIPITATOR0.01GR/DSCF @ 10% O2483MS-0075GEORGIA PACIFIC CORP.LAWRENCEMSLKLIME KILNLead (Pb) / Lead CompoundsSCRUBBER0SEE NOTE484MS-0075GEORGIA PACIFIC CORP.LAWRENCEMSLKLIME KILNParticulate matter, filterable < 10 μ (FPM10)SCRUBBER21.2LB/H2827MS-0077GEORGIA PACIFIC CORPORATIONLAWRENCEMSLKLIME KILNParticulate matter, filterable < 10 μ (FPM10)VENTURI SCRUBBER29.9LB/H536 NC-0092 INTERNATIONAL PAPER COMPANY COLUMBUS NC LK LIME KILN Particulate Matter (PM)ESP AND A FIXED THROAT SPRAY VENTURI-TYPE WETSCRUBBER0.13 GR/DSCF @ 10% O2582SC-0084BOWATERYORKSCLKLIME KILN, NO. 2Particulate Matter (PM)ESP0.03GR/DSCF @ 10% O2602TX-0263DONAHUE INDUSTRIES, INC.ANGELINATXLKLIME KILNParticulate matter, filterable < 10 μ (FPM10)SCRUBBER22.7LB/H2466 GA-0095 WEYERHAEUSER - FLINT RIVER OPERATIONS MACON GA LK ROTARY LIME KILN Particulate Matter (PM) ESP0.01 GR/DSCF @ 10% O214 AR-0099 GEORGIA-PACIFIC CORPORATION ASHLEY AR RF 8R RECOVERY BOILER Particulate Matter (PM) WET ESP0.02 G/DSCF @ 8% O2 3 HR AVERAGE, 8% O241AL-0222ROCK-TENN MILL COMPANY, LLCMARENGOALRFRECOVERY FURNACEParticulate Matter (PM)ELECTROSTATIC PRECIPITATOR0.021GR/DSCF @ 8% O23HR55 AL-0237 INTERNATIONAL PAPER CORPERATION -COURTLAND MILLLAWRENCE AL RF NO. 3 RECOVERY FURNACE Particulate matter, filterable < 10 μ (FPM10) ESP0.015 GR/DSCF 3HRS102GA-0092GEORGIA PACIFIC CORP.EARLYGARFRECOVERY BOILERParticulate Matter (PM)ESP49.7LB/H110 GA-0114 TEMPLE INLAND, INC. FLOYD GA RF RECOVERY FURNACE, BLS FUEL Particulate matter, filterable < 10μ (FPM10) ESP0.021 GR/DSCF @ 8% O2122KY-0085MEADWESTVACO KENTUCKY, INCBALLARDKYRFRECOVERY FURNACEParticulate Matter (PM)WET BOTTOM ESP & WET SCRUBBER1.35LB/T ADPlb/t of unbleached ADP189LA-0122INTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLARFRECOVERY BOILER NO.1 AND NO.2Particulate matter, filterable < 10 μ (FPM10)ESP96.5LB/H310LA-0155CROWN PAPER COMPANYWEST FELICIANA PARISHLARFRECOVERY FURNACEParticulate Matter (PM)ELECTROSTATIC PRECIPITATOR31.25LB/HHOURLY MAXIMUM347LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLARFRECOVERY FURNACE NO. 1Particulate Matter (PM)ELECTROSTATIC PRECIPITATOR37.31LB/H351LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLARFRECOVERY FURNACE NO. 1Particulate matter, filterable < 10 μ (FPM10)ELECTROSTATIC PRECIPITATOR37.31LB/H363LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLARFRECOVERY FURNACE NO. 2Particulate Matter (PM)ELECTROSTATIC PRECIPITATOR56LB/H367LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLARFRECOVERY FURNACE NO. 2Particulate matter, filterable < 10 μ (FPM10)ELECTROSTATIC PRECIPITATOR56LB/H432LA-0201WEYERHAEUSER CONATCHITOCHESLARFRECOVERY BOILER NO. 3Particulate matter, filterable < 10 μ (FPM10)ELECTROSTATIC PRECIPITATOR0.015GR/DSCF @ 8% 02451 LA-0207 INTERNATIONAL PAPER CO DESOTO LA RF RECOVERYBOILERS NO. 1 & 2(EQT036 & 037)Particulate Matter (PM) ELECTROSTATIC PRECIPITATOR100.5 LB/H HOURLY MAXIMUM497MS-0075GEORGIA PACIFIC CORP.LAWRENCEMSRFRECOVERY BOILER NO. 1Particulate matter, filterable < 10 μ (FPM10)ESP194.3LB/H510MS-0075GEORGIA PACIFIC CORP.LAWRENCEMSRFRECOVERY BOILER NO. 2Particulate Matter (PM)ESP194.3LB/H520MS-0078GEORGIA PACIFIC CORPORATIONLAWRENCEMSRFBOILER, NO. 1 RECOVERYParticulate matter, filterable < 10 μ (FPM10)TWO ELECTROSTATIC PRECIPITATORS194.3LB/H527MS-0078GEORGIA PACIFIC CORPORATIONLAWRENCEMSRFBOILER, NO. 2 RECOVERYParticulate matter, filterable < 10 μ (FPM10)TWO ESP194.3LB/H529NC-0092INTERNATIONAL PAPER COMPANYCOLUMBUSNCRFRECOVERY BOILERParticulate Matter (PM)ESP0.044GR/DSCF @ 8% O2559NC-0108INTERNATIONAL PAPERHALIFAXNCRFNO. 7 RECOVERY FURNACEParticulate matter, filterable < 10 μ (FPM10)EXISTING MULTIFIELD ELECTROSTATIC PRECIPITATOR0.021GR/DSCF8% O2568 SC-0083 WEYERHAEUSER COMPANY MARLBORO SC RF NO. 1 RECOVERY FURNACE Particulate Matter (PM) ELECTROSTATIC PRECIPITATOR/ RECOVERY FURNACEFIRING RATE AND PULP PRODUCTION (4.4 MM LB BLS/DAND1410ADTBP/D LIMITS0.021 GR/DSCF@ 8% O2579SC-0084BOWATERYORKSCRFNO. 3 RECOVERY FURNACEParticulate Matter (PM)ESP0.036GR/DSCF @ 8% O2778 *VA-0306 MEADWESTVACO COVINGTON VA RF RECOVERY FURNACE (revised fromPROCESS NOTES column)Particulate Matter (PM), Organic Condensables TRS AND AN ESP GOOD COMBUSTION PRACTICES 68.3 LB/H779 *VA-0306 MEADWESTVACO COVINGTON VA RF RECOVERY FURNACE (revised fromPROCESS NOTES column)Particulate matter, filterable < 10 μ (FPM10) TRSAND AN ESP GOOD COMBUSTION PRACTICES 51.3 LB/H876 WI-0141 MOSINEE PAPER CORPORATION MARATHON WI RF RECOVERY BOILER, PROCESS #B21,STACK #S11Particulate Matter (PM) ESP79.76 T/YR885 WI-0208 DOMTAR INDUSTRIES INC. WOOD WI RF KRAFT BLACKLIQUOR RECOVERYFURNACE, B14Particulate Matter (PM) EXISTING ESP0.03 GR/DSCF @ 8% O2288 LA-0122 INTERNATIONAL PAPER - MANSFIELD MILL DE SOTO PARISH LA SDT SMELT DISSOLVING TANK NO.1 ANDNO.2Particulate matter, filterable < 10 μ (FPM10) WETSCRUBBERS14.2 LB/H373LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLASDTSMELT TANK NO. 1Particulate Matter (PM)WET SCRUBBER9.22LB/H376LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLASDTSMELT TANK NO. 1Particulate matter, filterable < 10 μ (FPM10)WET SCRUBBER9.22LB/H378LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLASDTSMELT TANK NO. 2Particulate Matter (PM)WET SCRUBBERS6.24LB/H381LA-0174GEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLASDTSMELT TANK NO. 2Particulate matter, filterable < 10 μ (FPM10)WET SCRUBBERS6.24LB/H437LA-0201WEYERHAEUSER CONATCHITOCHESLASDTSMELT TANK NO. 3Particulate matter, filterable < 10 μ (FPM10)ELECTROSTATIC PRECIPITATOR0.015GR/DSCF @ 8% O2*475MS-0075GEORGIA PACIFIC CORP.LAWRENCEMSSDTSMELT DISSOLVING TANKS (4)Particulate Matter (PM)SCRUBBERS, 4 EACH0.2LB/TAIR-DRIED PULP PER TANK476MS-0075GEORGIA PACIFIC CORP.LAWRENCEMSSDTSMELT DISSOLVING TANKS (4)Particulate matter, filterable < 10 μ (FPM10)SCRUBBERS, 4 EACH5.8LB/HEACH TANK575 SC-0083 WEYERHAEUSER COMPANY MARLBORO SC SDT SMELT DISSOLVING TANK Particulate Matter (PM) SCRUBBER/RECOVERY FURNACE FIRING AND PULPPRODUCTION LIMITS (4.4 MM LB BLS/D AND 1410ADTBP/D)0.199 LB/T BLS870 WI-0141 MOSINEE PAPER CORPORATION MARATHON WI SDT SMELT TANK, PROCESS #P30, STACK#S12Particulate Matter (PM) VENTURI SCRUBBER.11.43 T/YRNotes:1. Highlighted in yellow those limits more stringent than NSPS.2. Included corrected control method description (ESP & wet scrubber) for Georgia-Pacific Port Hudsonmill.B-1CORPORATE_OR_COMPANY_NAME FACILITY_COUNTYFACILITY_STATEGEORGIA-PACIFIC CONSUMER OPERATIONSLLCPUTNAM FLMEADWESTVACO KENTUCKY, INCBALLARDKYINTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAWEYERHAEUSER CONATCHITOCHESLAGEORGIA PACIFIC CORP.LAWRENCEMSGEORGIA PACIFIC CORP.LAWRENCEMSGEORGIA PACIFIC CORPORATIONLAWRENCEMSINTERNATIONAL PAPER COMPANY COLUMBUS NCBOWATERYORKSCDONAHUE INDUSTRIES, INC.ANGELINATXWEYERHAEUSER - FLINT RIVER OPERATIONS MACON GAGEORGIA-PACIFIC CORPORATION ASHLEY ARROCK-TENN MILL COMPANY, LLCMARENGOALINTERNATIONAL PAPER CORPERATION -COURTLAND MILLLAWRENCE ALGEORGIA PACIFIC CORP.EARLYGATEMPLE INLAND, INC. FLOYD GAMEADWESTVACO KENTUCKY, INCBALLARDKYINTERNATIONAL PAPER - MANSFIELD MILLDE SOTO PARISHLACROWN PAPER COMPANYWEST FELICIANA PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAWEYERHAEUSER CONATCHITOCHESLAINTERNATIONAL PAPER CO DESOTO LAGEORGIA PACIFIC CORP.LAWRENCEMSGEORGIA PACIFIC CORP.LAWRENCEMSGEORGIA PACIFIC CORPORATIONLAWRENCEMSGEORGIA PACIFIC CORPORATIONLAWRENCEMSINTERNATIONAL PAPER COMPANYCOLUMBUSNCINTERNATIONAL PAPERHALIFAXNCWEYERHAEUSER COMPANY MARLBORO SCBOWATERYORKSCMEADWESTVACO COVINGTON VAMEADWESTVACO COVINGTON VAMOSINEE PAPER CORPORATION MARATHON WIDOMTAR INDUSTRIES INC. WOOD WIINTERNATIONAL PAPER - MANSFIELD MILL DE SOTO PARISH LAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAGEORGIA-PACIFIC CORPORATIONEAST BATON ROUGE PARISHLAWEYERHAEUSER CONATCHITOCHESLAGEORGIA PACIFIC CORP.LAWRENCEMSGEORGIA PACIFIC CORP.LAWRENCEMSWEYERHAEUSER COMPANY MARLBORO SCMOSINEE PAPER CORPORATION MARATHON WINotes:1. Highlighted in yellow those limits more stringent than NSPS.2. Included corrected control method description (ESP & wet scrubber) for Georgia-Pacific Port Hudsonmill.CASE-BYCASE_BASISOTHER_APPLICABLE_REQUIREMENTSPERCENT_EFFICIENCYEMISSION_LIMIT_2EMISSION_LIMIT_2_UNITEMISSION_LIMIT_2_AVGE_TIME_CONDITIONSTANDARD_EMISSION_LIMITSTANDARD_EMISSION_LIMIT_UNITSTANDARD_LIMIT_AVGE_TIME_CONDITIONBACT-PSD95 22.9 LB/H 3 TEST RUN 0Other Case-by-Case000see noteBACT-PSD99.8114.3T/YR1.93GR/DSCFCALCULATEDBACT-PSD0112.85T/YR0.05GR/DSCF @ 10% O2ASSUMING STANDARD CONDITIONSBACT-PSD0112.85T/YR0.05GR/DSCF @ 10% O2ASSUMING STANDARD CONDITIONSBACT-PSD089.57T/YR0.033GR/DSCF @ 10% O2ASSUMING STANDARD CONDITIONSBACT-PSD089.57T/YR0.033GR/DSCF @ 10% O2ASSUMING STANDARD CONDITIONSBACT-PSDOPERATING PERMIT , MACT000.01GR/DSCF @ 10% O2*BACT-PSD000BACT-PSDMACT092.9T/YR0.066GR/DSCF @ 10% O2BACT-PSDMACT0131T/YR0.064GR/DSCF @ 10% O2N/A NSPS0 00.13 GR/DSCF @ 10% O2BACT-PSD00.03GR/DSCF @ 10% 020BACT-PSD096.7T/YR0NOT AVAILABLEMACT MACT0 00.01 GR/DSCF @ 10% O2BACT-PSD NSPS , NESHAP , MACT , SIP ,OPERATING PERMIT99.9 00BACT-PSDMACT9944.9LB/H3HR0BACT-PSD99.8 0.021 GR/DSCF 3HRS 0BACT-PSD9900.032GR/DSCF @ 8% O2BACT-PSD NSPS , NESHAP , MACT , SIP 0 00.021 GR/DSCF @ 8% O2Other Case-by-Case000see noteBACT-PSD99.7190.3T/YR0.009GR/DSCF @ 8 % O2CONVERTED FROM GR/DSCMBACT-PSDNSPS , OPERATING PERMIT0125.12T/YRANNUAL MAXIMUM0.044GR/DSCF @ 8% O2THREE ONE-HOUR TEST AVERAGEBACT-PSD0165.17T/YR0.025GR/DSCF @ 8% O2ASSUMING STANDARD CONDITIONSBACT-PSD0165.17T/YR0.025GR/DSCF @ 8% O2ASSUMING STANDARD CONDITIONSBACT-PSD0245.28T/YR0.025GR/DSCF @ 8% O2ASSUMING STANDARD CONDITIONSBACT-PSD0245.28T/YR0.025GR/DSCF @ 8% O2ASSUMING STANDARD CONDITIONSBACT-PSDMACT , OPERATING PERMIT000BACT-PSD NSPS , OPERATING PERMIT 0 198 T/YR ANNUAL MAXIMUM 0.02 GR/DSCF @ 8% O2 ANNUAL AVERAGEBACT-PSDMACT0851.1T/YR0.044GR/DSCF @ 8% O2BACT-PSDMACT0851.1T/YR0.044GR/DSCF @ 8% O2BACT-PSDMACT0851.1T/YR0.044GR/DSCF @ 8% O2BACT-PSDMACT0851.1T/YR0.044GR/DSCF @ 8% O2SEE NOTEN/ANSPS000.044GR/DSCF @ 8% O2000.021GR/DSCF @ 8% O2BACT-PSD0 203 T/YR0.021 GR/DSCF @ 8% O2BACT-PSD00.036GR/DSCF @ 8% 020BACT-PSD OPERATING PERMIT 0 173.8 T/YR0BACT-PSD OPERATING PERMIT 0 10 T/YR0BACT-PSD99.5 00.027 GR/DSCF @ 8% O2BACT-PSD0 0.1 LB/MMBTU STATE LIMIT 0.03 GR/DSCF @ 8% O2BACT-PSD99.8 62.2 T/YR0.2 LB/T BLS CALCULATED USING THROUGHPUTBACT-PSD040.4T/YR0.133LB/T BLSCALCULATEDBACT-PSD040.4T/YR0.133LB/T BLSCALCULATEDBACT-PSD027.31T/YR0.133LB/T BLSCALCULATEDBACT-PSD027.31T/YR0.123LB/T BLSCALCULATEDBACT-PSDMACT , OPERATING PERMIT000BACT-PSDMACT06.5LB/HPER TANK0.2LB/TBLS PER TANKBACT-PSDMACT025.3T/YREACH TANK0.15LB/TBLS EACH TANK*BACT-PSD0 79.9 T/YR0.199 LB/T BLSBACT-PSD0 2.89 LB/H0.18 LB/T blsB-2