adeq · 2019. 12. 30. · impinjet scrubber on the roofto atmosphere as sn-07. solid waste from the...

ADEQARK A N S A SDepartment of Environmental Quality

March 18, 2009

Fred McLane, HSE OfficerGerber Products CompanyP.O. Box 10010Fort Smith, AR 72917-0010

Dear Mr. McLane:

The enclosed Permit No. 1220-AR-6 is your authority to construct, operate, and maintain theequipment and/or control apparatus as set forth in your application initially received on 7/2/2008.

After considering the facts and requirements of A.C.A. §8-4-101 et seq., and implementingregulations, I have determined that Permit No. 1220-AR-6 for the construction, operation andmaintenance of an air pollution control system for Gerber Products Company to be issued andeffective on the date specified in the permit, unless a Commission review has been properlyrequested under §2.1.14 of Regulation No.8, Arkansas Department of Pollution Control &Ecology Commission's Administrative Procedures, within thirty (30) days after service of thisdecision.

All persons submitting written comments during this thirty (30) day period, and all other personsentitled to do so, may request an adjudicatory hearing and Commission review on whether thedecision of the Director should be reversed or modified. Such a request shall be in the form andmanner required by §2.1.14 ofRegulation No.8.

Sincerely,

~~Mike BatesChief, Air Division

ARKANSAS DEPARTMENT OF ENVIRONMENTAL QUALITY5301 NORTHSHORE DRIVE / NORTH UTILE ROCK / ARKANSAS 72118-5317 / TELEPHONE 501-682-0744 / FAX 501-682-0880

www.adeq.state.ar.us

RESPONSE TO COMMENTS

Gerber Products Company4301 Harriet Lane

Fort Smith, AR 72904Permit No.: 1220-AR-6

AFIN: 66-00054

On January 13,2009 the Director of the Arkansas Department of Environmental Qualitygave notice of a draft permitting decision for the above referenced facility. During thecomment period, the facility submitted written comments, data, views, or arguments on thedraft permitting decision. The Department's response to these issues is as follows:

Comments received via email on February 16 and March 2,2009from Fred McLane. Safety,Health & Environmental Officer. Gerber.

Comment #1

Gerber's ammonia losses are far lower than the 35,000 pounds per 12-month rolling total.Use of a maximum 9,840 pounds per 12-month rolling total is sufficient.

Response #1

Agreed.

PC3/2/09

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ADEQMINOR SOURCE

AIR PERMITPermit No.: 1220-AR-6

IS ISSUED TO:

Gerber Products Company4301 Harriet Lane

Fort Smith, AR 72904Sebastian CountyAFIN: 66-00054

THIS PERMIT IS THE ABOVE REFERENCED PERMITTEE'S AUTHORITY TOCONSTRUCT, MODIFY, OPERATE, AND/OR MAINTAIN THE EQUIPMENT AND/ORFACILITY IN THE MANNER AS SET FORTH IN THE DEPARTMENT'S MINOR SOURCEAIR PERMIT AND THE APPLICATION. THIS PERMIT IS ISSUED PURSUANT TO THEPROVISIONS OF THE ARKANSAS WATER AND AIR POLLUTION CONTROL ACT(ARK. CODE ANN. SEC. 8-4-101 ET SEQ.) AND THE REGULATIONS PROMULGATEDTHEREUNDER, AND IS SUBJECT TO ALL LIMITS AND CONDITIONS CONTAINEDHEREIN.

Signed:

lLMMike BatesChief, Air Division

March 18, 2009

Date

Gerber Products CompanyPermit #1220-AR-6AFIN: 66-00054

Table of Contents

Section I: FACILITY INFORMATION 4Section II: INTRODUCTION 5

Summary ofPermit Activity 5Process Description 5Regulations 7Total Allowable Emissions 8

Section III: PERMIT HISTORY 9Section IV: EMISSION UNIT INFORMATION 10Section V: INSIGNIFICANT ACTIVITIES 15Section VI: GENERAL CONDITIONS 16APPENDIX A 21

40 CFR Part 60, Subpart Dc NSPS 21

2


List of Acronyms and Abbreviations

A.c.A. Arkansas Code Annotated

AFIN ADEQ Facility Identification Number

BTU British Thermal Units

CFR Code ofFederal Regulations

CO Carbon Monoxide

HAP Hazardous Air Pollutant

lblhr Pound Per Hour

MMBtulhr million BTU per hour

MSDS Material Safety Data Sheet

No. Number

NOx Nitrogen Oxide

NSPS New Source Performance Standards

PM Particulate Matter

PM10 Particulate Matter Smaller Than Ten Microns

PTE Potential to Emit

scf standard cubic feet

SN Source Number

S02 Sulfur Dioxide

tpy tons per year

UTM Universal Transverse Mercator

VOC Volatile Organic Compound

3


Section I: FACILITY INFORMATION

PERMITTEE: Gerber Products Company

AFIN: 66-00054

PERMIT NUMBER: 1220-AR-6

FACILITY ADDRESS: 4301 Harriet LaneFort Smith, AR 72904

MAILING ADDRESS: PO Box 10010Fort Smith, AR 72917-0010

COUNTY: Sebastian County

CONTACT NAME: Fred McLane

CONTACT POSITION: SHE Officer

TELEPHONE NUMBER: (479) 784-5234

REVIEWING ENGINEER: Patty Campbell

UTM North South (Y):

UTM East West(X):

Zone 15: 3921564.88 m

Zone 15: 374668.64 m

4


Section II: INTRODUCTION

Summary of Permit Activity

Gerber Products Company (Gerber) owns and operates a canned baby food processing facility(NAICS 311422) located at 4301 Harriet Lane, Fort Smith, Sebastian County, Arkansas 72904.This permitting action is necessary to:

1. Update the heat input capacities and revise emission estimates for Boiler #1 (SN01A) to 125 MMBtu/hr; for Boiler #2 (SN-02A) to 122.4 MMBtu/hr; and forBoiler #3 (SN-22) to 57.11 MMBtu/hr;

2. Remove SN-23, the Wastewater Treatment Plant Boiler and Flare, from service;and

3. Reduce maximum make-up Ammonia (SN-27) to 9,840 pounds per consecutive12-months.

This modification is covered by the existing natural gas facility-wide emissions "bubble".Changes in total permitted emissions are: -4.0 tpy PMIPM IO, -12.6 tpy SOz, 0.3 tpy VOC, 22.7tpy CO, -1.6 tpy NOX, -1.7 tpy HzSO, and -12.58 tpy Ammonia.

Process Description

Gerber manufactures and packages baby and toddler foods at their Fort Smith facility. Thesefoods are divided into 1) Cereals and 2) Baby Foods. Baby food includes produce (includingvegetable/meat blends), dry ingredients, and meats. Process descriptions for each of these twocategories along with other process operations are provided.

Cereal Manufacture

Various grain flours and nutrients are weighed and dry blended. The blended ingredients arethen conveyed to a slurry tank where water is added. The resultant slurry is preheated and thenpumped through a heat exchanger bringing the temperature above 200°F. The slurry is thenpumped to one of the facility's six steam heated drum dryers where it is dehydrated. Exhaustblowers from the dryers vent steam, moisture vapor and flour particulate matter to theatmosphere as SN-08A through SN-13B.

The dried product is conveyed to flakers, gravity separators and finally to storage bins. Thisproduct is then conveyed to the filler where it is packaged in paper cartons. The cased product isthen transported to the warehouse for subsequent shipment to customers. Cereal and flour dustfrom the blending and gravity flaker unit operation is exhausted through a Sly Model #145Impinjet Scrubber on the roof to atmosphere as SN-07. Solid waste from the gravity separatorsis either recycled or routed to the Fort Smith landfill.

On an annual basis, the Gerber Fort Smith cereal plant processes approximately 9000 tons ofgrain flours such as rice, wheat, com, and oats, as well as vitamin and mineral supplementalnutrient ingredients, to manufacture 2,800,000 cases of eight ounce baby cereals.

5

Gerber Products CompanyPermit #1 220-AR-6AFIN: 66-00054

Baby Food Manufacture

Over 110 varieties of baby food are manufactured at the Fort Smith facility. Annually, 11,506tons of dry ingredients are used to manufacture 43,800,000 cases (dozens) of various baby fooditems in this process.

Produce: Produce is brought from cool storage, pre-inspected, washed and (if need be) peeled ina lye bath or steam peelers. This produce is then rewashed and any remaining defects areremoved by human inspectors. The produce is chopped and then blanched and softened in screwsteamers. Moisture vapor is vented to atmosphere at the screw steamers and at the steam peelers.The heated produce particle size is reduced through a series of milling steps and the resultantpuree is accumulated in formulation tanks.

Dry Ingredients: If the formula requires other ingredients, these are weighed, blended, andmilled before being combined with the produce ingredients. Dust from this process is collectedand vented through a Sly Model #140 Impinjet scrubber, to atmosphere as SN-06.

Meat: Ifthe formula requires a meat ingredient, the meat is ground, precooked and milled toreduce particle size. This ingredient is then pumped to the formulation tanks. Moisture vapor isvented to atmosphere at the milling equipment used for meat.

The combined ingredients are heated above 185 qF, and then pumped to filling equipment whichdelivers the product into glass jars. The jars are capped and pressure cooked in retorts. After thecommercial sterilization process is completed, the jars are cooled, labeled and cased. The casesare transported to a warehouse facility and remain there until shipped to customers.

Other Process Operations

Boilers: Boiler No.1 (East, SN-OlA) and Boiler No.2 (West, SN-02A) provide steam for theCereal and Baby Food Departments. One boiler (SN-02A) is on-line nearly all the time, whilethe second boiler (SN-OlA) operates during periods of high steam loads. To maximizeoperational flexibility, Gerber operates natural gas sources "under a bubble". This providesoperational flexibility without increasing total allowable emissions. A third boiler (SN-22)approximately one-fourth the size of the original boilers operates during periods oflow heatrequirements when the other two boilers are not operating. Two QuikWater water heaters (SN24 and SN-25) with a maximum input capacity of 11 MMBTU/hr each are located in the mainboiler room. The natural gas consumed in the facility is supplied through one meter and theemissions from the natural gas usage is "bubbled."

Maintenance and Material Handling Activities: The facility has a maintenance shop. Thewelding operation (SN-05) has a fume hood which vents to atmosphere. Fume emissions are lessthan 0.01 Ibs/hr and 0.1 tons/year, and are therefore considered negligible. Materials aretransported between areas at the facility by forklift. Lead-acid batteries used to power the forklifts are recharged at the facility. Fumes generated by the recharge process are vented to theatmosphere via fume hoods (SN-14 through SN-17). These sources were deleted from the firstpermit issued April 29, 1992.

Ammonia Refrigeration System: The facility utilizes an ammonia-based refrigeration system tomaintain proper temperature for various operational rooms, storage areas, and offices. Bothsystems use pressurized ammonia stored in a receiver located on the roof of the facility. Some

6


operations and areas require a temperature of 55 degrees Fahrenheit (OF). For these operations,ammonia is supplied to a chiller. In the chiller, the ammonia refrigerant cools a glycol solution.The glycol solution is circulated to the various areas. The areas which utilize the glycolcirculation system are finished goods storage, flour silos, dry ingredients storage and meatbatching.

Other areas require colder temperatures. For these areas, ammonia is circulated directly to thearea and serves as the refrigerant in direct expansion heat exchanger coils. The liquid ammoniais converted to gaseous ammonia by absorbing heat from air circulated over coils to thetemperature controlled rooms. The gaseous ammonia is then compressed and condensed andreturned to the receiver. Two freezers are maintained between 32 of and 72 of depending ontemperature requirements. This would include cereal operations rooms, meat stick operationsroom, brine chiller in the smokehouse, produce storage, and liquid ingredient storage. Thesystem has rated capacity of approximately 1500 tons of refrigeration (one ton of refrigeration =

12,000 BTUIhr). At anyone time the entire system contains about 50,000 pounds of liquidammonia. Make-up ammonia, non-point emissions, are designated SN-27.

Carton Printing Operation: Palletized, precut, corrugated carton blanks are delivered to theprinting area (SN-20) located in the Labeling and Casing Room. The company and productnames are printed on these blanks through the use of water based flexographic inks andHottendorf printers. After printing is complete, printed cartons are repalletized and stored inwarehouse locations until used. This process is classified as an Insignificant Activity.

Ink-Jet Printers: For quality control purposes, each jar, cup, box or sleeve must be printed withcode date information as, expiration date, product code, batch number, etc. The ink-jets aresmall, portable and interchangeable between product lines. Gerber has approximately thirty-four(34) ink-jet printers (SN-26). The quantity of ink and make-up ink emissions used annual in theink-jet printers does not exceed 5.0 VOC tpy and an insignificant amount of HAPs; therefore, theink-jet printers are considered an Insignificant Activity.

Natural Gas Emergency Generator: A natural gas emergency generator (SN-21) will be used toprovide emergency lighting during power outages. The fuel consumption at full load will be 683cubic feet per hour (ft3/hr) of natural gas.

Regulations

The following table contains the regulations applicable to this permit.

Source Number Regulations

Facility-wide Arkansas Air Pollution Control Code, Regulation 18, effective January25,2009

Facility-wide Regulations ofthe Arkansas Plan ofImplementation for Air PollutionControl, Regulation 19, effective January 25,2009

7


Source Number Regulations

40 CFR Part 60 Subpart Dc - New Source Performance Standard22,24 & 25 (NSPS) - Standards ofPerformance for Small Industrial - Commercial -

Institutional Steam Generating Units (Appendix A)

The two large boilers (SN-Ol & SN-02) were installed in 1963; therefore, they are not subject toNSPS 40 CFR Part 60, Subpart Dc - Standards ofPerformance for Small Industrial Commercial- Institutional Steam Generating Units.

Total Allowable Emissions

The following table is a summary of emissions from the facility. This table, in itself, is not anenforceable condition of the permit.

TOTAL ALLOWABLE EMISSIONS

Emission RatesPollutant

Ib/hr tpy

PM 4.2 7.9

PMIO 4.2 7.9

S02 0.5 0.4

VOC 2.1 3.7

CO 27.2 55.8

NOx 41.4 91.5

Ammonia* --- 4.92

* Maximum Make-up Ammonia = 9,840 Ibs/consecutive 12-month period.

8


Section III: PERMIT HISTORY

Permit No. 1220-A was issued to Gerber Products Company on April 19, 1992. Permit limitswere: PM - 109.20 tpy, VOC - 4.28 tpy, NOx -109.60 tpy, CO - 27.42 tpy, S02 - 32.44 tpy,and Methyl Bromide - 10.95 tpy.

Permit No. 1220-AR-1 was issued to Gerber Products Company on April 19, 1995. Permit limitswere: PM lO - 86.5 tpy, VOC - 1.8 tpy, NOx - 63.5 tpy, CO - 16.0 tpy, S02 - 0.7 tpy, MethylBromide - 9.2 tpy, and Ammonia - 17.5 tpy.

Permit No. 1220-AR-2 was issued to Gerber Products Company on June 14, 1996. Permit limitswere: PM lO - 12.3 tpy, VOC - 2.7 tpy, NOx - 92.1 tpy, CO - 23.6 tpy, S02 - 16.2 tpy, MethylBromide - 9.9 tpy, and Ammonia -17.5 tpy.

Permit No. 1220-AR-3 was issued to Gerber Products Company on September 19,2000. Permitlimits were: PM/PMlO - 11.7 tpy, VOC - 3.0 tpy, NOx - 89.4 tpy, CO - 22.4 tpy, S02 - 0.6 tpy,and Ammonia - 17.5 tpy.

Permit No. 1220-AR-4 was issued on October 27,2004. The permit was modified to allow theinstallation of a wastewater treatment plant (SN-23). The wastewater treatment plant included aboiler, which can be fired with natural gas or biogas, and a flare, which burns biogas and has anatural gas fired pilot. Annual permitted emissions were: 12.0 tpy PM/PM lO, 13.1 tpy S02, 3.5tpy VOC, 33.2 tpy CO, 93.6 tpy NOx, 17.5 tpy Ammonia, and 1.7 tpy H2S.

Permit No. 1220-AR-5 was issued on August 26, 2007. Gerber permitted two (2) existing waterheaters (SN-24 and SN-25) each rated 11 million BTUIhr, as emission sources. Thismodification was covered by the existing facility-wide emissions "bubble" for natural gasemissions and there were no increases in total permitted emissions.

• Permit No. 1220-AR-5 was amended on September 27,2007. The modificationswere: 1) the physical removal of one natural gas fired engine driven air compressor(SN-19) and 2) the addition of several small, portable Ink-Jet printers (SN-26) to theinsignificant activity list.

• Permit No. 1220-AR-5 was amended on August 6,2008. The modifications were toremove Specific Condition #7 and the reference to Specific Condition #7 in SpecificCondition #8. No physical rearrangements or modifications were made and noemission limits were changed.

9


Section IV: EMISSION UNIT INFORMATION

Specific Conditions

1. The permittee shall not exceed the emission rates set forth in the following table. Allsources are permitted at maximum capacity for both hourly and annual emissions.Annual natural gas emissions are limited by the fuel usage limit contained in SpecificCondition #8. [Regulation 19, §19.501 et seq., and AC.A §8-4-203 as referenced byAC.A §8-4-304 and §8-4-311]

SN Description Pollutant lb/hr tpy

PM10 1.0Boiler No.1 S02 0.1

alA (Natural Gas, 125 MMBtu/hr) VOC 0.7(Installed 1963) CO 10.3

NOx 16.9

PM10 1.0Boiler No. 2 S02 0.1

02A (Natural Gas, 122.4 MMBtu/hr) VOC 0.7(Installed 1963) CO 10.1

NOx 16.6

PM IO 0.1

Natural Gas Engine Driven S02 0.121 VOC 0.1 *Emergency Generator

CO 0.1NOx 0.1

PM10 0.5Boiler No. 3 S02 0.1

22 (Natural Gas, 57.11 MMBtu/hr) VOC 0.4(Installed 2000) CO 4.8

NOx 5.6

PM10 0.2Two QuikWater Water Heaters S02 0.1

24&25 (Natural Gas, 11 MMBtu/hr each) VOC 0.2(Installed 1998) CO 1.9

NOx 2.2

PM10 5.101A, 02A, * Total Annual Natural Gas

S02 0.421,22,24, VOC 3.7

Emissions (1,328,235,000 sct) ---&25 CO 55.8I

NOx 91.5

10



06 Sly Scrubber (Baby Food) PM10 0.1 0.2

07 Sly Scrubber (Cereal) PM10 0.1 0.2

08A Drum Dryer No.1 & Blower No. 1 PMlO 0.1 0.3

08B Drum Dryer No. 1 & Blower No.2 PM10 0.1 0.1

09A Drum Dryer No.2 & Blower No. 1 PM10 0.1 0.3

09B Drum Dryer No.2 & Blower No.2 PM10 0.1 0.1

lOA Drum Dryer No.3 & Blower No.1 PM10 0.1 0.3

lOB Drum Dryer No.3 & Blower No.2 PM10 0.1 0.1

llA Drum Dryer No.4 & Blower No. 1 PM10 0.1 0.3

lIB Drum Dryer No.4 & Blower No.2 PM10 0.1 0.1

12A Drum Dryer No.5 & Blower No. 1 PM10 0.1 0.3

12B Drum Dryer No.5 & Blower No.2 PMlO 0.1 0.1

13A Drum Dryer No.6 & Blower No. 1 PMlO 0.1 0.3

13B Drum Dryer No.6 & Blower No.2 PM10 0.1 0.1

5,14-17,Insignificant Activity

20 &26

3,19&23 Removed from Service.

2. The permittee shall not exceed the emission rates set forth in the following table.[Regulation 18, §18.80l and A.C.A. §8-4-203 as referenced by A.C.A. §8-4-304 and§8-4-311]


Boiler No. 1alA (Natural Gas, 125 MMBtu/hr) PM 1.0 *

(Installed 1963)

11



Boiler No. 202A (Natural Gas, 122.4 MMBtu/hr) PM 1.0

(Installed 1963)

21Natural Gas Engine Driven

PM 0.1Emergency Generator

Boiler No. 322 (Natural Gas, 57.11 MMBtu/hr) PM 0.5

(Installed 2000)

Two QuikWater Water Heaters24&25 (Natural Gas, 11 MMBtu/hr each) PM 0.2

(Installed 1998)

Facility- *Total Annual Natural GasPM 5.1

wide Emissions (1,328,235,000 sci)

06 Sly Scrubber (Baby Food) PM 0.1 0.2

07 Sly Scrubber (Cereal) PM 0.1 0.2

08A Drum Dryer No.1 & Blower No.1 PM 0.1 0.3

08B Drum Dryer No.1 & Blower NO.2 PM 0.1 0.1


09B Drum Dryer No.2 & Blower No.2 PM 0.1 0.1

lOA Drum Dryer No.3 & Blower No. 1 PM 0.1 0.3

lOB Drum Dryer No.3 & Blower No.2 PM 0.1 0.1


lIB Drum Dryer No.4 & Blower No.2 PM 0.1 0.1

12A Drum Dryer No.5 & Blower No. I PM 0.1 0.3


13A Drum Dryer No.6 & Blower No. 1 PM 0.1 0.3

12




27Total Coolant Equipment Leaks

Ammonia --- 4.92(9,840 lbs make-up Ammonia)

5, 14-17,Insignificant Activity

20 &26

3, 19 & 23 Removed from Service.

3. Visible emissions may not exceed the limits specified in the following table of this permitas measured by EPA Reference Method 9. [AC.A §8-4-203 as referenced by A.C.A.§8-4-304 and §8-4-311]

SN Limit Regulatory Citation

All Sources 5% §18.501

4. The permittee shall not cause or permit the emission of air contaminants, including odorsor water vapor and including an air contaminant whose emission is not otherwiseprohibited by Regulation #18, if the emission of the air contaminant constitutes airpollution within the meaning of A.C.A §8-4-303. [Regulation 18, §18.801 andAC.A. §8-4-203 as referenced by AC.A. §8-4-304 and §8-4-311]

5. The permittee shall not conduct operations in such a manner as to unnecessarily cause aircontaminants and other pollutants to become airborne. [Regulation 18, §18.901 andAC.A. §8-4-203 as referenced by AC.A §8-4-304 and §8-4-311]

6. The permittee shall add no more than 9,840 pounds of make-up ammonia (SN-27) torecharge the coolant system at the facility per consecutive 12-month period. [Regulation19, §19.705 and AC.A §8-4-203 as referenced by AC.A §8-4-304 and §8-4-311]

7. The permittee shall maintain monthly records which demonstrate compliance withSpecific Condition #6. The permittee shall update the records by the fifteenth day of themonth following the month to which the records pertain. The records shall be keptonsite, and shall be made available to Department personnel upon request. [Regulation19, §19.705 and AC.A §8-4-203 as referenced by AC.A §8-4-304 and §8-4-311]

8. Fuel usages at the facility shall not exceed the limits listed in the following table:[Regulation 19, §19.705 and AC.A §8-4-203 as referenced by AC.A. §8-4-304 and §84-311 ]

Fuel

Natural Gas

Facility-wide - Rolling 12 Month Total

l,328,235,000 scf

13

Gerber Products CompanyPennit #1220-AR-6AFIN: 66-00054

9. The pennittee shall maintain monthly records which demonstrate compliance withSpecific Condition #8. Records shall be updated by the fifteenth day of the monthfollowing the month to which the records pertain. These records shall be kept on site,and shall be made available to Department personnel upon request. [Regulation 19,§19.705 and A.C.A. §8-4-203 as referenced by A.c.A. §8-4-304 and §8-4-311]

10. The pennittee shall only use natural gas or LP gas as fuel for SN-OlA, 02A, 21, 22, 24,and/or 25 unless this pennit has been amended. [Regulation 19, §19.705 and 40 CFR 60,Subpart Dc]

11. The pennittee shall simultaneously conduct tests for CO and NOx on one of the twoboilers greater than 100 MMBtulhr, Boilers #1 and #2. (SN-OIA and SN-02A) at thefacility within 180 days of pennit issuance and every five years thereafter. EPAReference Method 7E shall be used to detennine NOx and EPA Reference Method 10shall be used to detennine CO. The pennittee shall follow the schedule and reportingrequirements in General Condition #7 and shall submit the test results to the Departmentat the address listed in General Condition #6. The pennittee shall test the boilers within90% of their rated capacity. Ifthe tests are not perfonned within this range, the pennitteeshall be limited to operating within 10% above the tested rate. The Department reservesthe right to select the boiler to be tested. The boilers tested shall be rotated so that noboiler is tested twice before the other boiler is tested once. If the tested emission rate forany pollutant is in excess of the pennitted emission rate, both boilers SN-OIA and SN02A shall be tested for that pollutant. [Regulation 19, §19.702 and/or Regulation 18§18.1002 and A.C.A. §8-4-203 as referenced by A.c.A. §8-4-304 and §8-4-311]

NSPS Conditions

12. The pennittee is subject to and shall comply with all applicable provisions ofNew SourcePerfonnance Standards (NSPS), 40 CFR 60, Subpart Dc. The pennittee shall calculate,record and maintain records of the amount of natural gas or LP gas combusted in theboiler (SN-22) and water heaters (SN-24 and SN-25) subject to Subpart Dc during eachmonth. [Regulation 19, §19.705 and 40 CFR 60, Subpart Dc]

13. The pennittee is responsible for other requirements listed in Subpart Dc that may affectthe facility. All records required by Subpart Dc shall be maintained by the pennittee fora period of two (2) years following the date of such record. A copy of Subpart Dc isattached to this pennit as Appendix A. [Regulation 19, §19.705 and §60.48c]

14


Section V: INSIGNIFICANT ACTIVITIES

The Department deems the following types of activities or emissions as insignificant on the basisof size, emission rate, production rate, or activity in accordance with Group A of theInsignificant Activities list found in Regulation 18 and 19 Appendix A. Insignificant activityemission determinations rely upon the information submitted by the permittee in an applicationdated July 2, 2008.

Description Category

Carton Printing Operation (formerly SN-20) A-9

Thirty-four (34) small, portable Ink-Jet Printers (formerly SN-26)A-13

(Ink and Make-up ink not to exceed 5.0 tpy VOC)

Fork Lift Battery Recharging (formerly SN-14 through SN-17) B-20

Maintenance Shop (formerly SN-05) B-14

15

Gerber Products CompanyPermit #1 220-AR-6AFIN: 66-00054

Section VI: GENERAL CONDITIONS

I. Any terms or conditions included in this permit that specify and reference ArkansasPollution Control & Ecology Commission Regulation 18 or the Arkansas Water and AirPollution Control Act (A.C.A. §8-4-1 0 I et seq.) as the sole origin of and authority for theterms or conditions are not required under the Clean Air Act or any of its applicablerequirements, and are not federally enforceable under the Clean Air Act. ArkansasPollution Control & Ecology Commission Regulation 18 was adopted pursuant to theArkansas Water and Air Pollution Control Act (A.C.A. §8-4-101 et seq.). Any terms orconditions included in this permit that specify and reference Arkansas Pollution Control& Ecology Commission Regulation 18 or the Arkansas Water and Air Pollution ControlAct (A.C.A. §8-4-101 et seq.) as the origin of and authority for the terms or conditionsare enforceable under this Arkansas statute.

2. This permit does not relieve the owner or operator of the equipment and/or the facilityfrom compliance with all applicable provisions ofthe Arkansas Water and Air PollutionControl Act and the regulations promulgated under the Act. [A.C.A. §8-4-203 asreferenced by A.C.A. §8-4-304 and §8-4-311]

3. The permittee shall notify the Department in writing within thirty (30) days aftercommencement of construction, completion ofconstruction, first operation of equipmentand/or facility, and first attainment of the equipment and/or facility target production rate.[Regulation 19, §19.704 and/or A.c.A. §8-4-203 as referenced by A.C.A. §8-4-304 and§8-4-311]

4. Construction or modification must commence within eighteen (18) months from the dateofpermit issuance. [Regulation 19, §19.41 O(B) and/or Regulation 18, §18.309(B) andA.C.A. §8-4-203 as referenced by A.C.A. §8-4-304 and §8-4-311]

5. The permittee must keep records for five years to enable the Department to determinecompliance with the terms of this permit such as hours of operation, throughput, upsetconditions, and continuous monitoring data. The Department may use the records, at thediscretion of the Department, to determine compliance with the conditions of the permit.[Regulation 19, §19.705 and/or Regulation 18, §18.1004 and A.C.A. §8-4-203 asreferenced by A.C.A. §8-4-304 and §8-4-31I ]

6. A responsible official must certify any reports required by any condition contained in thispermit and submit any reports to the Department at the address below. [Regulation 19,§19.705 and/or Regulation 18, §18.1004 and A.c.A. §8-4-203 as referenced by A.C.A.§8-4-304 and §8-4-311]

Arkansas Department of Environmental QualityAir DivisionATTN: Compliance Inspector Supervisor5301 Northshore DriveNorth Little Rock, AR 72118-5317

7. The permittee shall test any equipment scheduled for testing, unless stated in the SpecificConditions of this permit or by any federally regulated requirements, within the followingtime frames: (1) newly constructed or modified equipment within sixty (60) days of

16


achieving the maximum production rate, but no later than 180 days after initial start up ofthe permitted source or (2) existing equipment already operating according to the timeframes set forth by the Department. The permittee must notify the Department of thescheduled date of compliance testing at least fifteen (15) days in advance of such test.The permittee must submit compliance test results to the Department within thirty (30)days after the completion of testing. [Regulation 19, §19.702 and/or Regulation 18,§18.1002 and A.C.A §8-4-203 as referenced by AC.A. §8-4-304 and §8-4-311]

8. The permittee shall provide: [Regulation 19, §19.702 and/or Regulation 18, §18.1002and A.C.A. §8-4-203 as referenced by AC.A §8-4-304 and §8-4-311]

a. Sampling ports adequate for applicable test methods;b. Safe sampling platforms;c. Safe access to sampling platforms; andd. Utilities for sampling and testing equipment.

9. The permittee shall operate equipment, control apparatus and emission monitoringequipment within their design limitations. The permittee shall maintain in goodcondition at all times equipment, control apparatus and emission monitoring equipment.[Regulation 19, §19.303 and/or Regulation 18, §18.1104 and AC.A. §8-4-203 asreferenced by A.C.A. §8-4-304 and §8-4-311]

10. If the permittee exceeds an emission limit established by this permit, the permittee will bedeemed in violation of said permit and will be subject to enforcement action. TheDepartment may forego enforcement action for emissions exceeding any limitsestablished by this permit provided the following requirements are met: [Regulation 19,§19.601 and/or Regulation 18, §18.1101 and AC.A §8-4-203 as referenced by A.C.A.§8-4-304 and §8-4-311]

a. The permittee demonstrates to the satisfaction of the Department that theemissions resulted from an equipment malfunction or upset and are not the resultof negligence or improper maintenance, and the permittee took all reasonablemeasures to immediately minimize or eliminate the excess emissions.

b. The permittee reports the occurrence or upset or breakdown of equipment (bytelephone, facsimile, or overnight delivery) to the Department by the end of thenext business day after the occurrence or the discovery of the occurrence.

c. The permittee must submit to the Department, within five business days after theoccurrence or the discovery of the occurrence, a full, written report of suchoccurrence, including a statement of all known causes and of the scheduling andnature of the actions to be taken to minimize or eliminate future occurrences,including, but not limited to, action to reduce the frequency ofoccurrence of suchconditions, to minimize the amount by which said limits are exceeded, and toreduce the length oftime for which said limits are exceeded. If the information isincluded in the initial report, the information need not be submitted again.

11. The permittee shall allow representatives of the Department upon the presentation ofcredentials: [A.C.A. §8-4-203 as referenced by AC.A. §8-4-304 and §8-4-311]

17


a. To enter upon the permittee's premises, or other premises under the control of thepermittee, where an air pollutant source is located or in which any records arerequired to be kept under the terms and conditions of this permit;

b. To have access to and copy any records required to be kept under the terms andconditions of this permit, or the Act;

c. To inspect any monitoring equipment or monitoring method required in thispermit;

d. To sample any emission of pollutants; ande. To perform an operation and maintenance inspection of the permitted source.

12. The Department issued this permit in reliance upon the statements and presentationsmade in the permit application. The Department has no responsibility for the adequacy orproper functioning of the equipment or control apparatus. [AC.A. §8-4-203 asreferenced by AC.A §8-4-304 and §8-4-3ll]

13. The Department may revoke or modify this permit when, in the judgment of theDepartment, such revocation or modification is necessary to comply with the applicableprovisions of the Arkansas Water and Air Pollution Control Act and the regulationspromulgated the Arkansas Water and Air Pollution Control Act. [Regulation 19,§19A1O(A) and/or Regulation 18, §l8.309(A) and AC.A. §8-4-203 as referenced byAC.A. §8-4-304 and §8-4-311]

14. This permit may be transferred. An applicant for a transfer must submit a written requestfor transfer of the permit on a form provided by the Department and submit the disclosurestatement required by Arkansas Code Annotated §8-1-1 06 at least thirty (30) days inadvance of the proposed transfer date. The permit will be automatically transferred to thenew permittee unless the Department denies the request to transfer within thirty (30) daysofthe receipt ofthe disclosure statement. The Department may deny a transfer on thebasis of the information revealed in the disclosure statement or other investigation or,deliberate falsification or omission of relevant information. [Regulation 19, §19A07(B)and/or Regulation 18, §18.307(B) and AC.A §8-4-203 as referenced by A.C.A §8-4304 and §8-4-311]

15. This permit shall be available for inspection on the premises where the control apparatusis located. [AC.A. §8-4-203 as referenced by A.C.A. §8-4-304 and §8-4-311]

16. This permit authorizes only those pollutant emitting activities addressed herein. [AC.A§8-4-203 as referenced by AC.A §8-4-304 and §8-4-311]

17. This permit supersedes and voids all previously issued air permits for this facility.[Regulation 18 and 19 and AC.A §8-4-203 as referenced by AC.A. §8-4-304 and §8-4311]

18. The permittee must pay all permit fees in accordance with the procedures established inRegulation No.9. [AC.A §8-1-105(c)]

19. The permittee may request in writing and at least 15 days in advance of the deadline, anextension to any testing, compliance or other dates in this permit. No such extensions areauthorized until the permittee receives written Department approval. The Departmentmay grant such a request, at its discretion in the following circumstances: [Regulation

18


18, §18.102(C-D), Regulation 19, §19.103(D), A.C.A. §8-4-203 as referenced by A.C.A.§8-4-304 and §8-4-311, and CFR Part 52, Subpart E]

a. Such an extension does not violate a federal requirement;b. The permittee demonstrates the need for the extension; andc. The permittee documents that all reasonable measures have been taken to meet

the current deadline and documents reasons it cannot be met.

20. The permittee may request in writing and at least 30 days in advance, temporaryemissions and/or testing that would otherwise exceed an emission rate, throughputrequirement, or other limit in this permit. No such activities are authorized until thepermittee receives written Department approval. Any such emissions shall be included inthe facilities total emissions and reported as such. The Department may grant such arequest, at its discretion under the following conditions: [Regulation 18, §18.1 02(C-D),Regulation 19, §19.103(D), A.C.A. §8-4-203 as referenced by A.C.A. §8-4-304 and§8-4-311, and CFR Part 52, Subpart E]

a. Such a request does not violate a federal requirement;b. Such a request is temporary in nature;c. Such a request will not result in a condition of air pollution;d. The request contains such information necessary for the Department to evaluate

the request, including but not limited to, quantification of such emissions and thedate/time such emission will occur;

e. Such a request will result in increased emissions less than five tons of anyindividual criteria pollutant, one ton of any single HAP and 2.5 tons of totalHAPs; and

f. The permittee maintains records of the dates and results of such temporaryemissions/testing.

21. The permittee may request in writing and at least 30 days in advance, an alternativeto the specified monitoring in this permit. No such alternatives are authorized until thepermittee receives written Department approval. The Department may grant such arequest, at its discretion under the following conditions: [Regulation 18, §18.1 02(C-D),Regulationl9, §19.103(D), A.C.A. §8-4-203 as referenced by A.C.A. §8-4-304 and§8-4-311, and CFR Part 52, Subpart E]

a. The request does not violate a federal requirement;b. The request provides an equivalent or greater degree of actual monitoring to the

current requirements; andc. Any such request, if approved, is incorporated in the next permit modification

application by the permittee.

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APPENDIX A

40 CFR Part 60, Subpart Dc NSPS

Standards ofPerformance for Small Industrial Commercial Institutional SteamGenerating Units

21

40 CFR 60, Subpart Dc

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e-CFR Data is current as of December 3,2008

Title 40: Protection of EnvironmentPART 60-STANDARDS OF PERFORMANCE FOR NEW STATIONARY SOURCES

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Subpart Dc-Standards of Performance for Smallindustrial-CommercialInstitutional Steam Generating Units

Source: 72 FR 32759, June 13, 2007, unless otherwise noted.

§ 60.40c Applicability and delegation of authority.

(a) Except as provided in paragraph (d) of this section, the affected facility to which this subpart appliesis each steam generating unit for which construction, modification, or reconstnuction is commenced afterJune 9, 1989 and that has a maximum design heat input capacity of 29 megawatts (MW) (100 millionBritish thermal units per hour (MMBtu/hr)) or less, but greater than or equal to 2.9 MW (10 MMBtulhr).

(b) In delegating implementation and enforcement authority to a State under section 111(c) of the CleanAir Act, §60.48c(a)(4) shall be retained by the Administrator and not transferred to a State.

(c) Steam generating units that meet the applicability requirements in paragraph (a) of this section arenot subject to the sulfur dioxide (S02) or particulate matter (PM) emission limits, performance testing

requirements, or monitoring requirements under this SUbpart (§§60.42c, 60.43c, 60.44c, 60.45c, 60.46c,or 60.47c) during periods of combustion research, as defined in §60.41c.

(d) Any temporary change to an existing steam generating unit for the purpose of conducting combustionresearch is not considered a modification under §60.14.

(e) Heat recovery steam generators that are associated with combined cycle gas turbines and meet theapplicability requirements of subpart GG or KKKK of this part are not subject to this subpart. Thissubpart will continue to apply to all other heat recovery steam generators that are capable of combustingmore than or equal to 2.9 MW (10 MMBtu/hr) heat input of fossil fuel but less than or equal to 29 MW(100 MMBtu/hr) heat input of fossil fuel. If the heat recovery steam generator is subject to this subpart,only emissions resulting from combustion of fuels in the steam generating unit are SUbject to thissubpart. (The gas turbine emissions are subject to subpart GG or KKKK, as applicable, of this part).

(I) Any facility covered by subpart AAAA of this part is not covered by this subpart.

(g) Any facility covered by an EPA approved State or Federal section 111(d)/129 plan implementingsubpart BBBB of this part is not covered by this subpart.

§ 60.41c Definitions.

As used in this subpart, all terms not defined herein shall have the meaning given them in the Clean AirAct and in subpart A of this part.

Annual capacity factor means the ratio between the actual heat input to a steam generating unit from anindividual fuel or combination of fuels during a period of 12 consecutive calendar months and thepotential heat input to the steam generating unit from all fuels had the steam generating unit beenoperated for 8,760 hours during that 12-month period at the maximum design heat input capacity. In thecase of steam generating units that are rented or leased, the actual heat input shall be determinedbased on the combined heat input from all operations of the affected facility during a period of 12consecutive calendar months.

Appendix A, Page 1 of 16


Coal means all solid fuels classified .as anthracite, bituminous, sUbbituminous, or lignite by the AmericanSoaety of Testing and Materials in ASTM 0388 (incorporated by reference, see §60.17), coal refuse,and petroleum coke. Coal-derived synthetic fuels derived from coal for the purposes of creating usefulheat, including but not limited to solvent refined coal, gasified coal, coal-oil mixtures, and coal-watermixtures, are also included in this definition for the purposes of this subpart

Coal refuse means any by-product of coal mining or coal cleaning operations with an ash contentgreater than 50 percent (by weight) and a heating value less than 13,900 kilojoules per kilogram (kJ/kg)(6,000 Btu per pound (Btu/lb) on a dry basis.

Cogeneration steam generating unit means a steam generating unit that simultaneously produces bothelectrical (or mechanical) and thermal energy from the same primary energy source.

Combined cycle system means a system in which a separate source (such as a stationary gas turbine,internal combustion engine, or kiln) provides exhaust gas to a steam generating unit

Combustion research means the experimental firing of any fuel or combination of fuels in a steamgenerating unit for the purpose of conducting research and development of more efficient combustion ormore effective prevention or control of air pollutant emissions from combustion, provided that, duringthese periods of research and development, the heat generated is not used for any purpose other thanpreheating combustion air for use by that steam generating unit ( i.e. , the heat generated is released tothe atmosphere without being used for space heating, process heating, driving pumps, preheatingcombustion air for other units, generating electriaty, or any other purpose).

Conventional technology means wet flue gas desulfurization technology, dry flue gas desulfurizationtechnology, atmospheric fluidized bed combustion technology, and oil hydrodesulfurization technology.

Distillate oil means fuel oil that complies with the specifications for fuel oil numbers 1 or 2, as defined bythe American Society for Testing and Materials in ASTM 0396 (incorporated by reference, see §60.17).

Dry flue gas desulfurization technology means a S02controi system that is located between the steam

generating unit and the exhaust vent or staCk, and that removes sulfur oxides from the combustiongases of the steam generating unit by contacting the combustion gases with an alkaline reagent andwater, whether introduced separately or as a premixed slurry or solution and forming a dry powdermaterial. This definition includes devices where the dry powder material is subsequently converted toanother form. Alkaline reagents used in dry flue gas desulfurization systems include, but are not limitedto, lime and sodium compounds.

Duct burner means a device that combusts fuel and that is placed in the exhaust duct from anothersource (such as a stationary gas turbine, internal combustion engine, kiln, etc.) to allow the firing ofadditional fuel to heat the exhaust gases before the exhaust gases enter a steam generating unit

Emerging technology means any S02controi system that is not defined as a conventional technology

under this section, and for which the owner or operator of the affected facility has received approval fromthe Administrator to operate as an emerging technology under §6048c(a)(4).

Federally enforceable means all limitations and conditions that are enforceable by the Administrator,inclUding the requirements of 40 CFR parts 60 and 61, requirements within any applicable Stateimplementation plan, and any permit requirements established under 40 CFR 52.21 or under 40 CFR51.18 and 51.24.

Fluidized bed combustion technology means a device wherein fuel is distributed onto a bed (or series ofbeds) of limestone aggregate (or other sorbent materials) for combustion; and these materials are forcedupward in the device by the flow of combustion air and the gaseous products of combustion. Fluidizedbed combustion technology includes, but is not limited to, bubbling bed units and arculating bed units.

Fuel pretreatment means a process that removes a portion of the sulfur in a fuel before combustion ofthe fuel in a steam generating unit

Heat input means heat derived from combustion of fuel in a steam generating unit and does not includethe heat derived from preheated combustion air, recirculated flue gases, or exhaust gases from othersources (such as stationary gas turbines, internal combustion engines, and kilns).

Heat transfer medium means any material that is used to transfer heat from one point to another point

Maximum design heat input capacity means the ability of a steam generating unit to combust a statedmaximum amount of fuel (or combination of fuels) on a steady state basis as determined by the physicaldesign and characteristics of the steam generating unit

Natural gas means: (1) A naturally occurring mixture of hydrocarbon and nonhydrocarbon gases found



in geologic formations beneath the earth's surface, of which the principal constituent is methane; or (2)liquefied petroleum (LP) gas, as defined by the American Society for Testing and Materials in ASTMD1835 (incorporated by reference, see §60.17).

Noncontinental area means the State of Hawaii, the Virgin Islands, Guam, American Samoa, theCommonwealth of Puerto Rico, or the Northern Mariana Islands.

Oil means crude oil or petroleum, or a liquid fuel derived from crude oil or petroleum, including distillateoil and residual oil.

Potential sulfur dioxide emission rate means the theoretical S02emissions (nanograms per joule (ng/J)

or Ib/MMBtu heat input) that would result from combusting fuel in an uncleaned state and without usingemission control systems.

Process heater means a device that is primarily used to heat a material to initiate or promote a chemicalreaction in which the material participates as a reactant or catalyst.

Residual oil means crude oil, fuel oil that does not comply with the specifications under the definition ofdistillate oil, and all fuel oil numbers 4, 5, and 6, as defined by the American Society for Testing andMaterials in ASTM D396 (incorporated by reference, see §60.17).

Steam generating unit means a device that combusts any fuel and produces steam or heats water orany other heat transfer medium. This term includes any duct burner that combusts fuel and is part of acombined cycle system. This term does not include process heaters as defined in this subpart.

Steam generating unit operating day means a 24-hour period between 12:00 midnight and the follOWingmidnight during which any fuel is combusted at any time in the steam generating unit. It is not necessaryfor fuel to be combusted continuously for the entire 24-hour period.

Wet flue gas desulfurization technology means an S02controi system that is located between the steam

generating unit and the exhaust vent or stack, and that removes sulfur oxides from the combustiongases of the steam generating unit by contacting the combustion gases with an alkaline slurry or solutionand forming a liquid material. This definition includes devices where the liquid material is subsequentlyconverted to another form. Alkaline reagents used in wet flue gas desulfunzation systems include, butare not limited to, lime, limestone, and sodium compounds.

Wet scrubber system means any emission control device that mixes an aqueous stream or slurry withthe exhaust gases from a steam generating unit to control emissions of PM or S02.

Wood means wood, wood residue, bark, or any derivative fuel or residue thereof, in any form, includingbut not limited to sawdust, sanderdust, wood chips, scraps, slabs, millings, shavings, and processedpellets made from wood or other forest residues.

§ 60.42c Standard for sulfur dioxide (502)'

(a) Except as provided in paragraphs (b), (c), and (e) of this section, on and after the date on which theperformance test is completed or required to be completed under §60.8, whichever date comes first, theowner or operator of an affected facility that combusts only coal shall neither: cause to be dischargedinto the atmosphere from the affected facility any gases that contain S02in excess of 87 ng/J (0.20

Ib/MMBtu) heat input or 10 percent (0.10) of the potential S02emission rate (90 percent reduction), nor

cause to be discharged into the atmosphere from the affected facility any gases that contain S02in

excess of 520 ng/J (1.2 Ib/MMBtu) heat input If coal is combusted with other fuels, the affected facilityshall neither: cause to be discharged into the atmosphere from the affected facility any gases thatcontain S02in excess of 87 ng/J (0.20 Ib/MMBtu) heat input or 10 percent (0.10) of the potential

S02emission rate (90 percent reduction), nor cause to be discharged into the atmosphere from the

affected facility any gases that contain S02in excess of the emission limit is determined pursuant to

paragraph (e)(2) of this section.

(b) Except as provided in paragraphs (c) and (e) of this section, on and after the date on which theperformance test is completed or required to be completed under §60.8, whichever date comes first, theowner or operator of an affected facility that:

(1) Combusts only coal refuse alone in a fluidized bed combustion steam generating unit shall neither:

(i) Cause to be discharged into the atmosphere from that affected facility any gases that contain S02in

excess of 87 ng/J (0.20 Ib/MMBtu) heat input or 20 percent (0.20) of the potential S02emission rate (80



percent reduction); nor

(ii) Cause to be discharged into the atmosphere from that affected facility any gases that contain SOzin

excess of SOzin excess of 520 ng/J (1.2 Ib/MMBtu) heat input. If coal is fired with coal refuse, the

affected facility subject to paragraph (a) of this section. If oil or any other fuel (except coal) is fired withcoal refuse, the affected facility is subject to the 87 ng/J (0.20 Ib/MMBtu) heat input SOzemissions limit

or the 90 percent SOzreduction requirement specified in paragraph (a) of this secbon and the emission

limit is determined pursuant to paragraph (e)(2) of this section.

(2) Combusts only coal and that uses an emerging technology for the control of SOzemissions shall

neither:

(i) Cause to be discharged into the atmosphere from that affected facility any gases that contain SOzin

excess of 50 percent (0.50) of the potential SOzemission rate (50 percent reduction); nor

(ii) Cause to be discharged into the atmosphere from that affected facility any gases that contain SOzin

excess of 260 ng/J (0.60 Ib/MMBtu) heat input. If coal is combusted with other fuels, the affected facilityis subject to the 50 percent SOzreduction requirement specified in this paragraph and the emission limit

determined pursuant to paragraph (e)(2) of this section.

(c) On and after the date on which the initial performance test is completed or required to be completedunder §60.8, whichever date comes first, no owner or operator of an affected faCility that combusts coal,alone or in combination with any other fuel, and is listed in paragraphs (c)(1), (2), (3), or (4) of thissection shall cause to be discharged into the atmosphere from that affected facility any gases thatcontain SOzin excess of the emission limit determined pursuant to paragraph (e)(2) of this section.

Percent reduction requirements are not applicable to affected facilities under paragraphs (c)(1), (2), (3),or (4).

(1) Affected facilities that have a heat input capacity of 22 MW (75 MMBtu/hr) or less.

(2) Affected facilities that have an annual capacity for coal of 55 percent (0.55) or less and are SUbject toa federally enforceable reqUirement limiting operation of the affected facility to an annual capacity factorfor coal of 55 percent (0.55) or less.

(3) Affected facilities located in a noncontinental area.

(4) Affected facilities that combust coal in a duct burner as part of a combined cycle system where 30percent (0.30) or less of the heat entering the steam generating unit is from combustion of coal in theduct burner and 70 percent (0.70) or more of the heat entering the steam generating unit is from exhaustgases entering the duct burner.

(d) On and after the date on which the initial performance test is completed or required to be completedunder §60.8, whichever date comes first, no owner or operator of an affected facility that combusts oilshall cause to be discharged into the atmosphere from that affected facility any gases that contain SOzin

excess of 215 ng/J (0.50 Ib/MMBtu) heat input or, as an alternative, no owner or operator of an affectedfacility that combusts oil shall combust oil in the affected facility that contains greater than 0.5 weightpercent sulfur. The percent reduction reqUirements are not applicable to affected facilities under thisparagraph.

(e) On and after the date on which the initial performance test is completed or required to be completedunder §60.8, whichever date comes first, no owner or operator of an affected facility that combusts coal,oil, or coal and oil with any other fuel shall cause to be discharged into the atmosphere from thataffected facility any gases that contain SOzin excess of the following:

(1) The percent of potential S02emission rate or numerical S02emission rate required under paragraph

(a) or (b)(2) of this section, as applicable, for any affected facility that

(i) Combusts coal in combination with any other fuel;

(Ii) Has a heat input capacity greater than 22 MW (75 MMBtu/hr); and

(iii) Has an annual capacity factor for coal greater than 55 percent (0.55); and

(2) The emission limit determined according to the fallowing formula for any affected facility thatcombusts coal, oil, or coal and oil with any other fuel:



E = (K.H. +K,H, +K,H,), (H. +H,+H,)

Where:

Es=S02emission limit, expressed in ng/J or Ib/MMBtu heat input;

Ka=520 ng/J (1.2 Ib/MMBtu);

Kb=260 ng/J (0.60 Ib/MMBtu);

Kc=215 ng/J (0.50 Ib/MMBtu);

Ha= Heat input from the combustion of coal, except coal combusted in an

affected facility subject to paragraph (b)(2) of this section, in JoUles (J)[MMBtu];

Hb=Heat input from the combustion of coal in an affected facility subject to

paragraph (b)(2) of this section, in J (MMBtu); and

HcKaHb= Heat input from the combustion of oil, in J (MMBtu).

(I) Reduction in the potential S02emission rate through fuel pretreatment is not credited toward the

percent reduction requirement under paragraph (b)(2) of this section unless'

(1) Fuel pretreatment results in a 50 percent (0.50) or greater reduction in the potential S02emission

rate; and

(2) Emissions from the pretreated fuel (without either combustion or post-combustion S02control) are

equal to or less than the emission limits specified under paragraph (b)(2) of this section.

(g) Except as provided in paragraph (h) of this section, compliance with the percent reductionrequirements. fuel oil sulfur limits, and emission limits of this section shall be determined on a 30-dayrolling average basis.

(h) For affected facilities listed under paragraphs (h)(1), (2), or (3) of this section, compliance with theemission limits or fuel oil sulfur limits under this section may be determined based on a certification fromthe fuel supplier, as described under §60.48c(l), as applicable.

(1) Distillate oii-fired affected facilities with heat input capacities between 2.9 and 29 MW (10 and 100MMBtu/hr).

(2) Residual oil-fired affected facilities with heat input capacities between 2.9 and 8.7 MW (10 and 30MMBtu/hr).

(3) Coal-fired facilities with heat input capacities between 2.9 and 8.7 MW (10 and 30 MMBtulhr).

(i) The S02emission limits, fuel oil sulfur limits, and percent reduction requirements under this section

apply at all times, including periods of startup, shutdown, and malfunction.

Ul Only the heat input supplied to the affected facility from the combustion of coal and oil is countedunder this section. No credit is provided for the heat input to the affected facility from wood or other fuelsor for heat derived from exhaust gases from other sources, such as stationary gas turbines, internalcombustion engines, and kilns.

§ 60.43c Standard for particulate matter (PM).

(a) On and after the date on which the initial performance test is completed or required to be completedunder §60.8, whichever date comes first, no owner or operator of an affected facility that commenced



construction, reconstruction, or modification on or before February 28, 2005, that combusts coal orcombusts mixtures of coal with other fuels and has a heat input capacity of 8.7 MW (30 MMBtu/hr) orgreater, shall cause to be discharged into the atmosphere from that affected facility any gases thatcontain PM in excess of the following emission limits:

(1) 22 ng/J (0.051 Ib/MMBtu) heat input if the affected facility combusts only coal, or combusts coal withother fuels and has an annual capacity factor for the other fuels of 10 percent (0.10) or less.

(2) 43 ng/J (0.10 IbIMMBtu) heat input if the affected facility combusts coal with other fuels, has anannual capacity factor for the other fuels greater than 10 percent (0.10), and is subject to a federallyenforceable requirement limiting operation of the affected facility to an annual capacity factor greaterthan 10 percent (0.10) for fuels other than coal.

(b) On and after the date on which the initial performance test is completed or required to be completedunder §60. 8, whichever date comes first, no owner or operator of an affected facility that commencedconstruction, reconstruction, or modification on or before February 28, 2005, that combusts wood orcombusts mixtures of wood with other fuels (except coal) and has a heat input capacity of 8.7 MW (30MMBtulhr) or greater, shall cause to be discharged into the atmosphere from that affected facility anygases that contain PM in excess of the following emissions limits:

(1) 43 ng/J (0.10 Ib/MMBtu) heat input if the affected facility has an annual capacity factor for woodgreater than 30 percent (0.30); or

(2) 130 ng/J (0.30 Ib/MMBtu) heat input if the affected facility has an annual capacity factor for wood of30 percent (030) or less and is subject to a federally enforceable requirement limiting operation of theaffected facility to an annual capacity factor for wood of 30 percent (0.30) or less.

(c) On and after the date on which the initial performance test is completed or required to be completedunder §60.8, whichever date comes first, no owner or operator of an affected facility that combusts coal,wood, or oil and has a heat input capacity of 8.7 MW (30 MMBtulhr) or greater shall cause to bedischarged into the atmosphere from that affected facility any gases that exhibit greater than 20 percentopacity (6-minute average), except for one 6-minute period per hour of not more than 27 percentopacity.

(d) The PM and opacity standards under this section apply at all times, except during periods of startup,shutdown, or malfunction.

(e)(1) On and after the date on which the initial performance test is completed or is required to becompleted under §60.8, whichever date comes first, no owner or operator of an affected facility thatcommences construction, reconstruction, or modification after February 28, 2005, and that combustscoal, oil, wood, a mixture Df these fuels, Dr a mixture Df these fuels with any Dther fuels and has a heatinput capacity Df 8.7 MW (30 MMBtu/hr) Dr greater shall cause tD be discharged intD the atmDspherefrom that affected facility any gases that contain PM in excess of 13 ng/J (0.030 Ib/MMBtu) heat input,except as prDvided in paragraphs (e)(2), (e)(3), and (e)(4) Df this sectiDn.

(2) As an alternative to meeting the requirements Df paragraph (e)(1) Df this sectiDn, the owner DrDperatDr Df an affected facility for which modificatiDn cDmmenced after February 28, 2005, may elect tDmeet the requirements Df this paragraph. On and after the date Dn which the initial perfDrmance test iscompleted or required tD be completed under §60.8, whichever date comes first, nD Dwner Dr DperatDr Dfan affected facility that commences mDdificatiDn after February 28, 2005 shall cause tD be dischargedinto the atmDsphere from that affected facility any gases that contain PM in excess of bDth:

(i) 22 ng/J (0.051 Ib/MMBtu) heat input derived from the cDmbustiDn Df coal, Dil, wDod, a mixture Df thesefuels, or a mixture Df these fuels with any Dther fuels; and

(ii) 0.2 percent Df the combustiDn concentratiDn (99.8 percent reductiDn) when combusting coal, Dil,wood, a mixture of these fuels, Dr a mixture of these fuels with any Dther fuels.

(3) On and after the date Dn which the initial perfDrmance test is completed or is required tD becompleted under §60.8, whichever date comes first, no Dwner Dr operatDr Df an affected facility thatcommences mDdificatiDn after February 28, 2005, and that combusts Dver 30 percent wDod (by heatinput) Dn an annual basis and has a heat input capacity of 8.7 MW (30 MMBtulhr) or greater shall causetD be discharged intD the atmDsphere from that affected facility any gases that contain PM in excess Df43 ng/J (0.10 Ib/MMBtu) heat input.

(4) On and after the date on which the initial perfDrmance test is completed Dr is required to becompleted under §60.8, whichever date comes first, an Dwner Dr DperatDr Df an affected facility thatcommences constructiDn, reconstructiDn, or mDdificatiDn after February 28, 2005, and that combustsDnly Dil that contains no mDre than 0.50 weight percent sulfur Dr a mixture Df 0.50 weight percent sulfurDil with Dther fuels nDt subject tD a PM standard under §60.43c and nDt using a pDst-combustiDntechnDIDgy (except a wet scrubber) tD reduce PM or S02emissiDns is nDt subject tD the PM limit in this



section.

§ 60.44c Compliance and performance test methods and procedures forsulfur dioxide.

(a) Except as provided in paragraphs (g) and (h) of this section and §608(b), performance tests requiredunder §60.8 shall be conducted following the procedures specified in paragraphs (b), (c), (d), (e), and (I)of this section, as applicable. Section 60.8(1) does not apply to this section. The 30-day notice requiredin §60.8(d) applies only to the initial performance test unless otherwise specified by the Administrator.

(b) The initial performance test required under §60.8 shall be conducted over 30 consecutive operatingdays of the steam generating unit. Compliance with the percent reduction requirements andS02emission limits under §60.42c shall be determined using a 30-day average. The first operating day

included in the initial performance test shall be scheduled within 30 days after achieving the maximumproduction rate at which the affect facility will be operated, but not later than 180 days after the initialstartup of the facility. The steam generating unit load during the 30-day period does not have to be themaximum design heat input capacity, but must be representative of future operating conditions.

(c) After the initial performance test required under paragraph (b) of this section and §6D.8, compliancewith the percent reduction requirements and S02emission limits under §60.42c is based on the average

percent reduction and the average S02emission rates for 30 consecutive steam generating unit

operating days. A separate performance test is completed at the end of each steam generating unitoperating day, and a new 30-day average percent reduction and S02emission rate are calculated to

show compliance with the standard.

(d) If only coal, only oil, or a mixture of coal and oil is combusted in an affected facility, the procedures inMethod 19 of appendix A of this part are used to determine the hourly S02emission rate (Eho) and the

3D-day average S02emission rate (Eao)' The hourly averages used to compute the 3D-day averages are

obtained from the CEMS. Method 19 of appendix A of this part shall be used to calculate Eaowhen using

daily fuel sampling or Method 68 of appendix A of this part.

(e) If coal, oil, or coal and oil are combusted with other fuels:

(1) An adjusted Eho(Ehoo) is used in Equation 19-19 of Method 19 of appendix A of this part to compute

the adjusted Eao(Eaoo). The Ehoo is computed using the following formula:

Where:

EhOo = Adjusted Eho

' ng/J (lb/MMBtu);

Eho

=Hourly S02emission rate, ng/J (lb/MMBtu);

Ew=S02concentration in fuels other than coal and oil combusted in the

affected facility, as determined by fuel sampling and analysis procedures inMethod 9 of appendix A of this part, ng/J (Ib/MMBtu). The value Ewfor each

fuel lot is used for each hourly average during the time that the lot is beingcombusted. The owner or operator does not have to measure Ewif the owner

or operator elects to assume Ew=O.

Xk= Fraction of the total heat input from fuel combustion derived from coal and

oil, as determined by applicable procedures in Method 19 of appendix A ofthis part.

(2) The owner or operator of an affected facility that qualifies under the provisions of §60.42c(c) or (d)(where percent reduction is not required) does not have to measure the parameters Ewor Xkif the owner

or operator of the affected facility elects to measure emission rates of the coal or oil using the fuel



sampling and analysis procedures under Method 19 of appendix A of this part.

(I) Affected facilities sUbject to the percent reduction requirements under §60.42c(a} or (b) shalldetermine compliance with the SOzemission limits under §60.42c pursuant to paragraphs (d) or (e) ofthis section, and shall determine compliance with the percent reduction requirements using the followingprocedures:

(1) If only coal is combusted, the percent of potential SOzemission rate is computed using the followingformula:

%P =100(1 - %Rr)(l_ %R'), 100 100

Where:

%Ps= Potential S02emission rate, in percent;

%Rg= SOlemoval efficiency of the control device as determined by Method

19 of appendix A of this part, in percent; and

%Rt SOlemoval efficiency of fuel pretreatment as determined by Method 19

of appendix A of this part, in percent.

(2) If coal, oil, or coal and oil are combusted with other fuels, the same procedures required in paragraph(1)(1) of this section are used, except as provided for in the following:

(i) To compute the 'loPs' an adjusted %Rg(%Rgo} is computed from Eaoo from paragraph (e)(1) of thissection and an adjusted average SOzinlet rate (Eaio) using the following formula:

%R 0 =100(1- E:)f E~

Where:

%Rgo = Adjusted %Rg

, in percent;

Eaoo = Adjusted E ao ' ng/J (lb/MMBtu); and

Eaio =Adjusted average S02iniet rate, ng/J (lb/MMBtu).

(ii) To compute Eaio, an adjusted hourly SOzinlet rate (EhiO) is used. The Ehio is computed using thefollowing formula:

Where:

EhiO =Adjusted E hi, ng/J (lb/MMBtu);

Ehi=Hourly S02iniet rate, ng/J (lb/MMBtu);

Ew=S02concentration in fuels other than coal and oil combusted in the

affected facility, as determined by fuel sampling and analysis procedures in



Method 19 of appendix A of this part, ng/J (lb/MMBtu). The value Ewfor each

fuel lot is used for each hourly average during the time that the lot is beingcombusted. The owner or operator does not have to measure Ewif the owner

or operator elects to assume Ew= 0; and

Xk=Fraction of the total heat input from fuel combustion derived from coal and

oil, as determined by applicable procedures in Method 19 of appendix A ofthis part.

(g) For oil-fired affected facilities where the owner or operator seeks to demonstrate compliance with thefuel oil sulfur limits under §60.42c based on shipment fuel sampling, the initial performance test shallconsist of sampling and analyzing the oil in the initial tank of oil to be fired in the steam generating unit todemonstrate that the oil contains 0.5 weight percent sulfur or less. Thereafter, the owner or operator ofthe affected facility shall sample the oil in the fuel tank after each new shipment of oil is received, asdescribed under §60.46c(d)(2).

(h) For affected facilities subject to §60.42c(h)(1), (2), or (3) where the owner or operator seeks todemonstrate compliance with the S02standards based on fuel supplier certification, the performance

test shall consist of the certification, the certification from the fuel supplier, as described under §60.48c(I), as applicable.

(i) The owner or operator of an affected facility seeking to demonstrate compliance with theS02standards under §60.42c(c)(2) shall demonstrate the maximum design heat input capacity of the

steam generating unit by operating the steam generating unit at this capacity for 24 hours. Thisdemonstration shall be made during the initial performance test, and a subsequent demonstration maybe requested at any other time. If the demonstrated 24-hour average firing rate for the affected facility isless than the maximum design heat input capacity stated by the manufacturer of the affected facility, thedemonstrated 24-hour average firing rate shall be used to determine the annual capacity factor for theaffected facility; otherwise, the maximum design heat input capacity provided by the manufacturer shallbe used.

0) The owner or operator of an affected facility shall use all valid S02emissions data in calculating %

Psand Ehounder paragraphs (d), (e), or (I) of this section, as applicable, whether or not the minimum

emissions data requirements under §60.46c(1) are achieved. All valid emissions data, including validdata collected during periods of startup, shutdown, and malfunction, shall be used in calculating %Psor

Ehopursuant to paragraphs (d), (e), or (I) of this section, as applicable.

§ 60.45c Compliance and performance test methods and procedures forparticulate matter.

(a) The owner or operator of an affected facility subject to the PM and/or opacity standards under§60.43c shall conduct an initial performance test as required under §60.8, and shall conduct subsequentperformance tests as requested by the Administrator, to determine compliance with the standards usingthe following procedures and reference methods, except as specified in paragraph (c) of this section.

(1) Method 1 of appendix A of this part shall be used to select the sampling site and the number oftraverse sampling points.

(2) Method 3 of appendix A of this part shall be used for gas analysis when applying Method 5, 58, or 17of appendix A of this part.

(3) Method 5, 58, or 17 of appendix A of this part shall be used to measure the concentration of PM asfollows:

(i) Method 5 of appendix A of this part may be used only at affected facilities without wet scrubbersystems.

(ii) Method 17 of appendix A of this part may be used at affected facilities with or without wet scrubbersystems provided the stack gas temperature does not exceed a temperature of 160 °C (320 OF). Theprocedures of Sections 8.1 and 11.1 of Method 58 of appendix A of this part may be used in Method 17of appendix A of this part only if Method 17 of appendix A of this part is used in conjunction with a wetscrubber system. Method 17 of appendix A of this part shall not be used in conjunction with a wetscrubber system if the effluent is saturated or laden with water droplets.

(iii) Method 58 of appendix A of this part may be used in conjunction with a wet scrubber system.



(4) The sampling time for each run shall be at least 120 minutes and the minimum sampling volumeshall be 1.7 dry standard cubic meters (dscm) [60 dry standard cubic feet (dscf)) except that smallersampling times or volumes may be approved by the Administrator when necessitated by processvariables or other factors.

(5) For Method 5 or 5B of appendix A of this part, the temperature of the sample gas in the probe andfilter holder shall be monitored and maintained at 160 ±14 °c (320±25 OF).

(6) For determination of PM emissions, an oxygen (02) or carbon dioxide (C02) measurement shall be

obtained simultaneously with each run of Method 5, 5B, or 17 of appendix A of this part by traversing theduct at the same sampling location.

(7) For each run using Method 5, 5B, or 17 of appendix A of this part, the emission rates expressed inng/J (lb/MMBtu) heat input shall be determined using:

(i) The 020r CO2measurements and PM measurements obtained under this section, (ii) The dry basis F

factor, and

(iii) The dry basis emission rate calculation procedure contained in Method 19 of appendix A of this part.

(8) Method 9 of appendix A of this part (6-minute average of 24 observations) shall be used fordetermining the opacity of stack emissions.

(b) The owner or operator of an affected facility seeking to demonstrate compliance with the PMstandards under §60.43c(b)(2) shall demonstrate the maximum design heat input capacity of the steamgenerating unit by operating the steam generating unit at this capacity for 24 hours. This demonstrationshall be made during the initial performance test, and a subsequent demonstration may be requested atany other time. If the demonstrated 24-hour average firing rate for the affected facility is less than themaximum design heat input capacity stated by the manufacturer of the affected facility, thedemonstrated 24-hour average firing rate shall be used to determine the annual capacity factor for theaffected facility; otherwise, the maximum design heat input capacity provided by the manufacturer shallbe used.

(c) In place of PM testing with EPA Reference Method 5, 5B, or 17 of appendix A of this part, an owneror operator may elect to install, calibrate, maintain, and operate a CEMS for monitoring PM emissionsdischarged to the atmosphere and record the output of the system. The owner or operator of an affectedfacility who elects to continuously monitor PM emissions instead of conducting performance testingusing EPA Method 5, 5B, or 17 of appendix A of this part shall install, calibrate, maintain, and operate aCEMS and shall comply with the requirements specified in paragraphs (c)(1) through (c)(13) of thissection.

(1) Notify the Administrator 1 month before starting use of the system.

(2) Notify the Administrator 1 month before stopping use of the system.

(3) The monitor shall be installed, evaluated, and operated in accordance with §60.13 of subpart A ofthis part.

(4) The initial performance evaluation shall be completed no later than 180 days after the date of initialstartup of the affected facility, as specified under §60.8 of subpart A of this part or within 180 days ofnotification to the Administrator of use of CEMS if the owner or operator was previously determiningcompliance by Method 5, 5B, or 17 of appendix A of this part performance tests, whichever is later.

(5) The owner or operator of an affected facility shall conduct an initial performance test for PMemissions as required under §60.8 of subpart A of this part. Compliance with the PM emission limit shallbe detenmined by using the CEMS specified in paragraph (d) of this section to measure PM andcalculating a 24-hour block arithmetic average emission concentration using EPA Reference Method 19of appendix A of this part, section 4.1.

(6) Compliance with the PM emission limit shall be determined based on the 24-hour daily (block)average of the hourly arithmetic average emission concentrations using CEMS outlet data.

(7) At a minimum, valid CEMS hourly averages shall be obtained as specified in paragraph (d)(7)(i) ofthis section for 75 percent of the total operating hours per 3D-day rolling average.

(i) At least two data points per hour shall be used to calculate each 1-hour arithmetic average.

(il) [Reserved]



(8) The 1-hour arithmetic averages required under paragraph (d)(7) of this section shall be expressed inng/J or Ib/MMBtu heat input and shall be used to calculate the boiler operating day daily arithmeticaverage emission concentrations. The 1-hour arithmetic averages shall be calculated using the datapoints required under §60.13(e)(2) of subpart A of this part.

(9) All valid CEMS data shall be used in calculating average emission concentrations even if theminimum CEMS data requirements of paragraph (d)(7) of this section are not met.

(10) The CEMS shall be operated according to Performance Specification 11 in appendix B of this part.

(11) During the correlation testing runs of the CEMS required by Performance Specification 11 inappendix B of this part, PM and 02(or CO2) data shall be collected concurrently (or within a 30- to 60

minute period) by both the continuous emission monitors and the test methods specified in paragraph(d)(7)(i) of this section.

(i) For PM, EPA Reference Method 5, 5B, or 17 of appendix A of this part shall be used.

(ii) For 02(or CO2), EPA reference Method 3, 3A, or 3B of appendix A of this part, as applicable shall be

used.

(12) Quarterly accuracy determinations and daily calibration drift tests shall be performed in accordancewith procedure 2 in appendix F of this part. Relative Response Audit's must be performed annually andResponse Correlation Audits must be performed every 3 years.

(13) When PM emissions data are not obtained because of CEMS breakdowns, repairs, calibrationchecks, and zero and span adjustments, emissions data shall be obtained by using other monitoringsystems as approved by the Administrator or EPA Reference Method 19 of appendix A of this part toprovide, as necessary, valid emissions data for a minimum of 75 percent of total operating hours on a3D-day rolling average.

(d) The owner or operator of an affected facility seeking to demonstrate compliance under §60.43c(e)(4)shall follow the applicable procedures under §60.48c(f). For residual oil-fired affected facilities, fuelsupplier certifications are only allowed for facilities with heat input capacities between 2.9 and 8.7 MW(10 to 30 MMBtu/hr).

§ 60.46c Emission monitoring for sulfur dioxide.

(a) Except as provided in paragraphs (d) and (e) of this section, the owner or operator of an affectedfacility subject to the S02emission limits under §60.42c shall install, calibrate, maintain, and operate a

CEMS for measuring S02concentrations and either 020r C02concentrations at the outlet of the

S02controi device (or the outlet of the steam generating unit if no S02controi device is used), and shall

record the output of the system. The owner or operator of an affected facility subject to the percentreduction requirements under §60.42c shall measure S02concentrations and either 020r

C02concentrations at both the inlet and outlet of the S02controi device.

(b) The 1-hour average S02emission rates measured by a CEMS shall be expressed in ng/J or

Ib/MMBtu heat input and shall be used to calculate the average emission rates under §60.42c. Each 1hour average S02emission rate must be based on at least 30 minutes of operation, and shall be

calculated using the data points required under §60.13(h)(2). Hourly S02emission rates are not

calculated if the affected facility is operated less than 30 minutes in a 1-hour period and are not countedtoward determination of a steam generating unit operating day.

(c) The procedures under §60.13 shall be followed for installation, evaluation, and operation of theCEMS.

(1) All CEMS shall be operated in accordance with the applicable procedures under PerformanceSpecifications 1, 2, and 3 of appendix B of this part.

(2) Quarterly accuracy determinations and daily calibration drift tests shall be performed in accordancewith Procedure 1 of appendix F of this part.

(3) For affected facilities subject to the percent reduction requirements under §60.42c, the span value ofthe S02CEMS at the inlet to the S02controi device shall be 125 percent of the maximum estimated

hourly potential S02emission rate of the fuel combusted, and the span value of the S02CEMS at the

outlet from the S02controi device shall be 50 percent of the maximum estimated hourly potential

S02emission rate of the fuel combusted.

Appendix A, Page 11of 16


(4) For affected facilities that are not subject to the percent reduction requirements of §60.42c, the spanvalue of the S02CEMS at the ouliet from the S02controi device (or outlet of the steam generating unit if

no S02controi device is used) shall be 125 percent of the maximum estimated hourly potential

S02emission rate of the fuel combusted.

(d) As an alternative to operating a CEMS at the inlet to the S02controi device (or ouliet of the steam

generating unit if no S02controi device is used) as required under paragraph (a) of this section, an

owner or operator may elect to determine the average S02emission rate by sampling the fuel prior to

combustion. As an alternative to operating a CEMS at the outlet from the S02controi device (or outlet of

the steam generating unit if no S02controi device is used) as required under paragraph (a) of this

section, an owner or operator may elect to determine the average S02emission rate by using Method 68

of appendix A of this part. Fuel sampling shall be conducted pursuant to either paragraph (d)(1) or (d)(2)of this section. Method 68 of appendix A of this part shall be conducted pursuant to paragraph (d)(3) ofthis section.

(1) For affected facilities combusting coal or oil, coal or oil samples shall be collected daily in an as-firedcondition at the inlet to the steam generating unit and analyzed for sulfur content and heat contentaccording the Method 19 of appendix A of this part. Method 19 of appendix A of this part providesprocedures for converting these measurements into the format to be used in calculating the averageS02input rate.

(2) As an alternative fuel sampling procedure for affected facilities combusting oil, oil samples may becollected from the fuel tank for each steam generating unit immediately after the fuel tank is filled andbefore any oil is combusted. The owner or operator of the affected facility shall analyze the oil sample todetermine the sulfur content of the oil. If a partially empty fuel tank is refilled, a new sample and analysisof the fuel in the tank would be required upon filling. Results of the fuel analysis taken after each newshipment of oil is received shall be used as the daily value when calculating the 3D-day rolling averageuntil the next shipment is received. If the fuel analysis shows that the sulfur content in the fuel tank isgreater than 0.5 weight percent sulfur, the owner or operator shall ensure that the sulfur content ofsubsequent oil shipments is low enough to cause the 3D-day rolling average sulfur content to be 0.5weight percent sulfur or less.

(3) Method 68 of appendix A of this part may be used in lieu of CEMS to measure S02at the inlet or

outlet of the S02controi system. An initial stratification test is required to verify the adequacy of the

Method 68 of appendix A of this part sampling location. The stratification test shall consist of threepaired runs of a suitable S02and C02measurement train operated at the candidate location and a

second similar train operated according to the procedures in §3.2 and the applicable procedures insection 7 of Performance Specification 2 of appendix 8 of this part Method 68 of appendix A of this part,Method 6A of appendix A of this part, or a combination of Methods 6 and 3 of appendix A of this part orMethods 6C and 3A of appendix A of this part are SUitable measurement techniques. If Method 68 ofappendix A of this part is used for the second train, sampling time and timer operation may be adjustedfor the stratification test as long as an adequate sample volume is collected; however, both samplingtrains are to be operated similarly. For the location to be adequate for Method 68 of appendix A of thispart 24-hour tests, the mean of the absolute difference between the three paired runs must be less than10 percent (0.10).

(e) The monitoring requirements of paragraphs (a) and (d) of this section shall not apply to affectedfacilities subject to §60.42c(h) (1), (2), or (3) where the owner or operator of the affected facility seeks todemonstrate compliance with the S02standards based on fuel supplier certification, as described under

§60.48c(l), as applicable.

(I) The owner or operator of an affected facility operating a CEMS pursuant to paragraph (a) of thissection, or conducting as-fired fuel sampling pursuant to paragraph (d)(1) of this section, shall obtainemission data for at least 75 percent of the operating hours in at least 22 out of 30 successive steamgenerating unit operating days. If this minimum data requirement is not met with a single monitoringsystem, the owner or operator of the affected facility shall supplement the emission data with datacollected with other monitoring systems as approved by the Administrator.

§ 60.47c Emission monitoring for particulate matter.

(a) Except as provided in paragraphs (c), (d), (e), and (I) of this section, the owner or operator of anaffected facility combusting coal, 011, or wood that is SUbject to the opacity standards under §60.43c shallinstall, calibrate, maintain, and operate a COMS for measuring the opacity of the emissions dischargedto the atmosphere and record the output of the system.

(b) All COMS for measuring opacity shall be operated in accordance with the applicable proceduresunder Performance Specification 1 of appendix 8 of this part. The span value of the opacity COMS shallbe between 60 and 80 percent.



(c) Affected facilities that burn only distillate oil that contains no more than 0.5 weight percent sulfurand/or liquid or gaseous fuels with potential sulfur dioxide emission rates of 26 ng/J (0.06 Ib/MMBtu)heat input or less and that do not use a post-combustion technology to reduce S020r PM emissions are

not required to operate a CEMS for measuring opacity if they follow the applicable procedures under§60A8c(1)

(d) Owners or operators complying with the PM emission limit by using a PM CEMS monitor instead ofmonitoring opacity must calibrate, maintain, and operate a CEMS, and record the output of the system,for PM emissions discharged to the atmosphere as specified in §60A5c(d). The CEMS specified inparagraph §60A5c(d) shall be operated and data recorded during all periods of operation of the affectedfacility except for CEMS breakdowns and repairs. Data is recorded during calibration checks, and zeroand span adjustments.

(e) An affected facility that does not use post-combustion technology (except a wet scrubber) forreducing PM, SOz' or carbon monoxide (CO) emissions, burns only gaseous fuels or fuel oils that

contain less than or equal to 0.5 weight percent sulfur, and is operated such that emissions of CO to theatmosphere from the affected facility are maintained at levels less than or equal to 0.15 IblMMBtu on aboiler operating day average basis is not required to operate a COMS for measuring opacity. Ownersand operators of affected facilities electing to comply with this paragraph must demonstrate complianceaccording to the procedures specified in paragraphs (e)(1) through (4) of this section.

(1) You must monitor CO emissions using a CEMS according to the procedures specified in paragraphs(e)(1 )(i) through (iv) of this section.

(i) The CO CEMS must be installed, certified, maintained, and operated according to the provisions in§6058b(i)(3) of subpart Eb of this part.

(ii) Each 1-hour CO emissions average is calculated using the data points generated by the CO CEMSexpressed in parts per million by volume corrected to 3 percent oxygen (dry basis).

(iii) At a minimum, valid 1-hour CO emissions averages must be obtained for at least 90 percent of theoperating hours on a 30-day rolling average basis. At least two data points per hour must be used tocalculate each 1-hour average.

(iv) Quarterly accuracy determinations and daily calibration drift tests for the CO CEMS must beperformed in accordance with procedure 1 in appendix F of this part.

(2) You must calculate the 1-hour average CO emissions levels for each steam generating unit operatingday by mUltiplying the average hourly CO output concentration measured by the CO CEMS times thecorresponding average hourly flue gas flow rate and divided by the corresponding average hourly heatinput to the affected source. The 24-hour average CO emission level is determined by calculating thearithmetic average of the hourly CO emission levels computed for each steam generating unit operatingday.

(3) You must evaluate the preceding 24-hour average CO emission level each steam generating unitoperating day excluding periods of affected source startup, shutdown, or malfunction. If the 24-houraverage CO emission level is greater than 0.15 Ib/MMBtu, you must initiate investigation of the relevantequipment and control systems within 24 hours of the first discovery of the high emission incident and,take the appropriate corrective action as soon as practicable to adjust control settings or repairequipment to reduce the 24-hour average CO emission level to 0.15 Ib/MMBtu or less.

(4) You must record the CO measurements and calculations performed according to paragraph (e) ofthis section and any corrective actions taken. The record of corrective action taken must include the dateand time during which the 24-hour average CO emission level was greater than 0.15 Ib/MMBtu, and thedate, time, and description of the corrective action.

(I) An affected facility that burns only gaseous fuels or fuel oils that contain less than or equal to 0.5weight percent sulfur and operates according to a written site-specific monitoring plan approved by theappropriate delegated permitting authority is not required to operate a COMS for measuring opacity.This monitoring plan must include procedures and criteria for establishing and monitoring specificparameters for the affected facility indicative of compliance with the opacity standard.

§ 60ASe Reporting and reeordkeeping requirements.

(a) The owner or operator of each affected facility shall submit notification of the date·of construction orreconstruction and actual startup, as provided by §60.7 of this part. This notification shall include:

(1) The design heat input capacity of the affected facility and identification of fuels to be combusted inthe affected facility.



(2) If applicable, a copy of any federally enforceable requirement that limits the annual capacity factor forany fuel or mixture of fuels under §60.42c, or §60.43c.

(3) The annual capacity factor at which the owner or operator anticipates operating the affected facilitybased on all fuels fired and based on each individual fuel fired.

(4) Notification if an emerging technology will be used for controlling SOzemissions. The Administrator

will examine the description of the control device and will determine whether the technology qualifies asan emerging technology. In making this determination, the Administrator may require the owner oroperator of the affected facility to submit additional information concerning the control device. Theaffected facility is subject to the provisions of §60.42c(a) or (b)(1), unless and until this determination ismade by the Administrator.

(b) The owner or operator of each affected facility subject to the SOzemission limits of §60.42c, or the

PM or opacity limits of §60.43c, shall submit to the Administrator the performance test data from theinitial and any SUbsequent performance tests and, if applicable, the performance evaluation of the CEMSand/or CaMS using the applicable performance specifications in appendix B of this part.

(c) The owner or operator of each coal-fired, oil-fired, or wood-fired affected facility subject to the opacitylimits under §60.43c(c) shall submit excess emission reports for any excess emissions from the affectedfacility that occur during the reporting period.

(d) The owner or operator of each affected facility SUbject to the SOzemission limits, fuel oil sulfur limits,

or percent reduction requirements under §60.42c shall submit reports to the Administrator.

(e) The owner or operator of each affected facility SUbject to the SOzemission limits, fuel oil sulfur limits,

or percent reduction requirements under §60.42c shall keep records and submit reports as requiredunder paragraph (d) of this section, including the following information, as applicable.

(1) Calendar dates covered in the reporting period.

(2) Each 30-day average SOzemission rate (ng/J or Ib/MMBtu), or 30-day average sulfur content (weight

percent), calculated during the reporting period, ending with the last 30-day period; reasons for anynoncompliance with the emission standards; and a description of corrective actions taken.

(3) Each 30-day average percent of potential SOzemission rate calculated during the reporting period,

ending with the last 30-day period; reasons for any noncompliance with the emission standards; and adescription of the corrective actions taken.

(4) Identification of any steam generating unit operating days for which SOzor diluent (Ozor COz) data

have not been obtained by an approved method for at least 75 percent of the operating hours;justification for not obtaining sufficient data; and a description of corrective actions taken.

(5) Identification of any times when emissions data have been excluded from the calculation of averageemission rates; justification for excluding data; and a description of corrective actions taken if data havebeen excluded for periods other than those during which coal or oil were not combusted in the steamgenerating unit.

(6) Identification of the F factor used in calculations, method of determination, and type of fuelcombusted.

(7) Identification of whether averages have been obtained based on CEMS rather than manual samplingmethods.

(8) If a GEMS is used, identification of any times when the pollutant concentration exceeded the full spanof the GEMS.

(9) If a GEMS is used, description of any modifications to the GEMS that could affect the ability of theGEMS to comply with Performance Specifications 2 or 3 of appendix B of this part.

(10) If a GEMS is used, results of daily GEMS drift tests and quarterly accuracy assessments asrequired under appendiX F, Procedure 1 of this part.

(11) If fuel supplier certification is used to demonstrate compliance, records of fuel supplier certificationis used to demonstrate compliance, records of fuel supplier certification as described under paragraph(f}{1), (2), (3), or (4) of this section, as applicable. In addition to records of fuel supplier certifications, thereport shall include a certified statement signed by the owner or operator of the affected facility that therecords of fuel supplier certifications submitted represent all of the fuel combusted during the reporting



period.

(f) Fuel supplier certification shall include the following information:

(1) For distillate oil:

(i) The name of the oil supplier;

(ii) A statement from the oil supplier that the oil complies with the specifications under the definition ofdistillate oil in §60.41c; and

(iii) The sulfur content of the oil.

(2) For residual oil:

(i) The name of the oil supplier;

(ii) The location of the oil when the sample was drawn for analysis to determine the sulfur content of theoil, specifically including whether the oil was sampled as delivered to the affected facility, or whether thesample was drawn from oil in storage at the oil supplier's or oil refiner's facility, or other location;

(iii) The sulfur content of the oil from which the shipment came (or of the shipment itself); and

(iv) The method used to determine the sulfur content of the oil.

(3) For coal:

(i) The name of the coal supplier;

(ii) The location of the coal when the sample was collected for analysis to determine the properties of thecoal, specifically including whether the coal was sampled as delivered to the affected facility or whetherthe sample was collected from coal in storage at the mine, at a coal preparation plant, at a coalsupplier's facility, or at another location. The certification shall include the name of the coal mine (andcoal seam), coal storage facility, or coal preparation plant (where the sample was collected);

(iii) The results of the analysis of the coal from which the shipment came (or of the shipment itself)including the sulfur content, moisture content, ash content, and heat content; and

(iv) The methods used to determine the properties of the coal.

(4) For other fuels:

(i) The name of the supplier of the fuel;

(ii) The potential sulfur emissions rate of the fuel in ng/J heat input; and

(iii) The method used to determine the potential sulfur emissions rate of the fuel.

(g)(1) Except as provided under paragraphs (g)(2) and (g)(3) of this section, the owner or operator ofeach affected facility shall record and maintain records of the amount of each fuel combusted duringeach operating day.

(2) As an alternative to meeting the requirements of paragraph (g)(1) of this section, the owner oroperator of an affected facility that combusts only natural gas, wood, fuels using fuel certification in§60.48c(f) to demonstrate compliance with the S02standard, fuels not subject to an emissions standard

(excluding opacity), or a mixture of these fuels may elect to record and maintain records of the amountof each fuel combusted during each calendar month.

(3) As an alternative to meeting the requirements of paragraph (g)(1) of this section, the owner oroperator of an affected facility or mUltiple affected facilities located on a contiguous property unit wherethe only fuels combusted in any steam generating unit (including steam generating units not subject tothis subpart) at that property are natural gas, wood, distillate oil meeting the most current requirementsin §60.42C to use fuel certification to demonstrate compliance with the S02standard, and/or fuels,

excluding coal and residual oil, not subject to an emissions standard (excluding opacity) may elect torecord and maintain records of the total amount of eaclh steam generating unit fuel delivered to thatproperty during each calendar month.



(h) The owner or operator of each affected facility subject to a federally enforceable requirement limitingthe annual capacity factor for any fuel or mixture of fuels under §60.42c or §60.43c shall calculate theannual capacity factor individually for each fuel combusted. The annual capacity factor is determined ona 12-month rolling average basis with a new annual capacity factor calculated at the end of the calendarmonth.

(i) All records required under this section shall be maintained by the owner or operator of the affectedfacility for a period of two years following the date of such record.

(j) The reporting period for the reports required under this subpart is each six-month period. All reportsshall be submitted to the Administrator and shall be postmarked by the 30th day following the end of thereporting period.

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Section 5081 Accessibility


CERTIFICATE OF SERVICE

I, Cynthia Hook, hereby certify that a copy of this permit has been mailed by first class mail to

Gerber Products Company, P.O. Box 10010, Fort Smith, AR, 72917-0010, on this

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Cynthia Hook, AAII, Air Division

adeq · 2019. 12. 30. · impinjet scrubber on the roofto atmosphere as sn-07. solid waste from the...

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