### STATElVIENT OF CERTIFICATION I certify under penalty oflaw that I have personally examined and am familiar with thc information submitted in this documcnt and all attachments and that, based on my inquiry ofthose individuals immediately responsible for obtaining information, I believe that the information is true, accurate, and complete. I am aware that there are significant penalties for submitting false information, including the possibility offine or imprisonment.

Signaturc

\ I ,) v \ ' Title

### Attachment A Plum Creek Northwest Lumber, Inc. Request for Information Pursuant to Section 114 ofthe CAA Part I: General Facility Data I. Name offacility: Plum Creek Manufacturing, L.P.

- Ksanka Mill Site 2. Complete street address offacility (physical location): a. Street Address: : Highway 93 south SE l;4 

### SE 1/4/ of Section 25, NE l;4 

### NE l;4 

### of Section 36, SW l;4 

### SW l;4 

### ofSection 30, Section 31, Township 35 North, Ranges 25 and 26 West b. City: Fortine c. State: Montana d. Zip: 59918 e. County: Lincoln County 3. Facility contact a. Name (First Name, Last Name): Mitchell Leu b. Title: Environmental Engineer c. Telephone number: (406) 892-6217 d. Fax number: 406-892-6150 e. E-mail: mitchell.leu@plumcreek.com f. 

### Mailing address: PO Box 28, Fortine, MT 59918 Part II: Boiler Emission Unit Data (Please complete entire section for each boiler, additional copies may be necessary) 1. 

### Emission Unit Name: EUOOI a. Type ofBoiler (e.g., spreader stoker, suspension-fired, fluidized bed): Fuel Cell b. Make: Wellons Fuel Cell with a Nebraska Type A boiler package c. Model: WTS-2-40 d. Model Year: 1979 e. Year installed: 1979 

### f. Expected equipment life: ? g. lJ'nit Is Currently Operational (Check One): X YES 

## =: NO I

## ryou answered YES ab()\'e. continue on to h. Ifyou answered NO above, answer the following and thcn continue to next unit: I. 

### Date oftinal operation: 11. 

### Will this unit be opcrated in the future (check onc)? A-I

### ::: YES =NO Ifyou ans\vered YES above, indicate possible date ofoperation and continue to h: h. Unit Capacity (MMBtu/hr): 20 J\fMBtu/hr

'I 

### Boiler Unit Outlet Information Ifthis unit exhausts to a shared stack, please provide the exhaust infonnation below before the shared outlet. a. Boiler Outlet Volumetric Flowrate (acfm):18500 b. Boiler Outlet Temperature (F):500 c. Boiler Outlet Moisture (%): 17% 

### d. Stack Height (ft):44 e. Stack Diameter (ft): 2.5 f. 

### Maximum Gross Heat Input (MMBtu/hr): 40 

### g. I-lours ofOperation:8760 h. Design Percent Load: 100% 1. 

### Average Uncontrolled PM Emissions (lb/hr): 9.1 j. 

### Average Uncontrolled NOx Emissions (lb/hr): 3.6 

### k. Average Uncontrolled S02 Emissions (lblhr): 0.5 

### 1. Does this unit share an exhaust stack with another unit? :::J 

### YES X NO 3. Existing Pollution Control Equipment (Complete the following for each piece ofcontrol equipment, make additional copies to provide infonnation for all equipment). a. PM Control Technology Inf0l111ation 1. 

### Type ofPM Control Technology: multiclone II. 

### Make/Model ofPM Control Technology: 

### Wellons 111. 

### Year installed: 1979 IV. 

### Installed Cost ofControl Device (S): 

### ? v. Annual Operating Cost ofControl Device ($/yr):n/a VI. 

### Expected life ofequipment: 

### ? V11. 

### Relevant sizing infoD11ation (for example, ifthe control device is an ESP, provide number offields, collector plate area, etc.): 

### 35 cyclones V111. 

### Design control efficiency (%): 

### ?

IX. 

### Average Controlled PM Emissions (lb/hr): 9.1 

### b. NOx Control Technology Information: 1. 

### Type ofNOx Control Technology: 

### none 11. 

### Make/Model ofNOx Control Technology: 111. 

### Year installed: IV. 

### Installed Cost ofControl Device 

### ($): v. Annual Operating Cost ofControl Device (S/yr): VI. 

### Expected life ofequipment: A-2V11. Relcvant sIzing information (for example, ifthe control device is an NCSR, provide catalyst volume, system capacity, etc.): VIl1. Design control efficiency (%):

IX. Average Controlled NOx Emissions (lb/hr): c. S02 Control Technology Infonnation 1. Type ofS02 Control Technology: none II. Make/Model ofS02 Control Technology: 111. Year installed: IV. Installed Cost ofControl Device 

### ($): v. Annual Operating Cost ofControl Device ($/yr): VI. Expected life ofequipment: VII. Relevant sizing information (for example, ifthe control device is a packed caustic scrubber, provide caustic usage, packing volume, etc.): V11l. Design control efficiency (%):

IX. Average Controlled S02 Emissions (1b/hr): 

### Thefollmving information shouldbe completed usingdatafor theyear2002. Ifinformation for 2002 is notrepresentative o.!,curl'ent operations (/01'

### example, ({this unit is no longer using naturalgas), provide**iJ~{ormation** 

### for a representativeyearandprovide reasons for why the alternativeyear is more representative thall 2002.

4. Fuel Information

List Eaeh Type of Fuel Used Amount of Fuel Used and Units Heating Value of Fuel (Btu/lb or Btu/set) Maximum Fuel Firing Rate (ton/hr or se£'hr) Sulfur Content ofFuel (%S Wt.) Year ofdata ifnot 2002 andreason for not using 2002 Hog fuel 

### 19000 tons 4800 btu/lb 

### 4.2 tonslhr trace 

### 2002

, I I

A-3

### Attachment A Plum Creek :\'1anufacturing, L.P.

- Evergreen Division Request for Information Pursuant to Section 114 ofthe CAA Part I: General Facility Data 1. Name offacility: Plum Creek Manufacturing, L.P.

- Evergreen Division 2. Complete street address offacility (physical location): a. Street Address: 75 Sunset Drive SW ofSection 33, Township 29 North, Range 21 West b. City: Kalispell c. State: Montana d. Zip: 59903 e. County: Flathead County 3. Facility contact a. Name (First Name, Last Name): Mitchell Leu b. Title: Environmental Engineer c. Telephone number: (406) 892-6217 d. Fax number: 406-892-6150 e. E-mail: mitchell.leu@plumcreek.com 1'. 

### Mailing address: PO Box 5447, Kalispell, MT 59903 Part II: Boiler Emission Unit Data (Please complete entire section for each boiler, additional copies may be necessary) 1. Emission Unit Name: EVOOI 

### a. Type ofBoiler (e.g., spreader stoker, suspension-fired, fluidized bed): spreader stoker b. Make: Riley Stoker c. Model:Stoker d. Model Year:1971 e. Year installed: 1971 f. 

### Expected equipment life: ? 

### g. Unit Is CUlTently Operational (Check One): XYES :::J 

### NO Ifyou answered YES above, continue on to h. Ifyou answered NO above, answer the following and then continue to next unit: 1. 

### Date offinal operation: 11. 

### Will this unit be operated in the future (check one)? A-IJ 

### YES Ifyou answered YES above, indicatc possible date ofoperation and continue to h: h. Unit Capacity (MMBtu/hr): 196 MMBtu/hr 2. Boiler Unit Outlet Information Ifthis unit exhausts to a shared stack, please provide the exhaust information belowbefore thc shared outlet. a. 

### Boiler Outlet Volumetric Flowrate (acfm): 55500 b. 

### Boilcr Outlet Temperature (F):430 c. Boiler Outlet Moisture (%): 

### 14% d. Stack Height (ft): 102 e. Stack Diameter (ft): 

### 7 f. 

### Maximum Gross Heat Input (MMBtu/hr):240 g. Hours ofOperation:8760 h. Design Percent Load:100 I. 

### Average Uncontrolled PM Emissions (lb/hr): ? J. 

### Average Uncontrolled NO

### x Emissions (lb/hr): 37 k. Average Uncontrolled S02 Emissions (lb/hr): 1.75 

### 1. Does this unit share an exhaust stack with another unit? J 

### YES X 

### NO 3. 

### Existing Pollution Control Equipment (Complete the following for each piece ofcontrol equipment, make additional copies to provide information for all equipment). a. PM Control Technology Infonnation 1. 

### Type ofPM Control Technology: dry 

### ESP 11. 

### Make/Model ofPM Control Technology: 

### PPC Industries 23R-1331­ 3712 Ill. 

### Year installed:1992 IV. 

### Installed Cost ofControl Device ($): -$1,000,000 v. Annual Operating Cost ofControl Device ($/yr): ? VI. 

### Expected life ofequipment: ? VII. 

### Relevant sizing infom1ation (for example, ifthe control device is an ESP, provide number offields, collector plate area, etc.): 3 fields V111. 

### Design control efficiency (%): 

### 99%

IX. 

### Average Controlled PM Emissions (lb/hr): 3.2 b. NOx Control Technology Information: I. 

### Type ofNOx Control Technology: none II. 

### Make/Model ofNOx Control Technology: 111. 

### Year installed: IV. 

### Installed Cost ofControl Device (S): v. Annual Operating Cost ofControl Device ($/yr): A-2VI. Expected life ofequipment: VII. Relevant sizing information (for example, ifthe control device is an NCSR, provide catalyst volume, system capacity, etc.): Vll1. Design control efficiency (%):

IX. Average Controlled NOx Emissions (lb/hr): c. SO= Control Technology Inf01111ation I. Type ofS02 Control Technology: none 11. Make/Model ofS02 Control Technology: 111. Year installed: IV. Installed Cost ofControl Device ($): v. Annual Operating Cost ofControl Device ($/yr): VI. Expected life ofequipment: VB. Relevant sizing infOlmation (for example, ifthe control device is a packed caustic scrubber, provide causticusage, packing volume, etc.): Vll1. Design control efficiency (%):

IX. Average Controlled S02Emissions (lb/hr): 

### Thefo/loJVing information shouldbe completed usingdatafor theyear 2002. Ifinformation for2002 is not representative of current operations (for example, 

## if this unitis no longer using naturalgas),provide informationfor a representativeyear andprovide reasons for why the alternativeyear is more representative than 2002.

4. Fuel Information Amount of Heating Value of Maximum Fuel Sulfur Content Year ofdata ifnot List Each Type of Fuel Used Fuel Firing Rate ofFuel 2002 and reason fuel Used and Units (Btu/lb or Btu/set) (ton/hr or scf/hr) (%S Wt.) for not using 2002 112,500 24.6 tons/hr Hog fuel 4,900 btu/lb trace 2002 tons

I I I I I , I I 

# L

__

# ~_--,-----------_-------,-------_~_-------,-------_

A-3Attachment A Plum CreekManufacturing, L.P. Request for Information Pursuant to Section 114 ofthe CAA Part I: General Facility Data 1. Name offacility: Plum Creek Manufacturing, L.P. Columbia Falls Operations 2. Complete street address offacility (physical location): a. StreetAddress: 500 12th Ave West Section 7 and the SW ofSection 8, Township 30 North, Range 20 West b. City: Columbia Falls c. State: MT d. Zip: 59912 e. County: Flathead County 3. Facility contact a. Name (First Name, Last Name): Mitchell Leu b. Title: Environmental Engineer c. Telephone number: 406-892-6217 d. Fax number: 406-892-6150 e. E-mail: mitchell.leu@plumcreek.com f. Mailing address: PO Box 1990, Columbia Falls, MT 59912

Part II: Boiler Emission Unit Data (Please complete entire section for each boiler, additional copies may be necessary) 1. Emission Unit Name: Riley Stoker Boiler a. Type ofBoiler (e.g., spreader stoker, suspension-fired, fluidized bed): Stoker b. Make: Riley-Union c. Model: Type UO Field Erected d. Model Year: 1973 e. Year installed: 1973 f. Expected equipment life: ? g. Unit Is CUlTently Operational (Check One): 

### X YES J NO Ifyou answered YES above, continue on to h. Ifyou answered NO above, answer the following and then continue to next unit: 1. Date offinal operation: 11. Will this unit be operated in the future (cheek one)? 

## := YES 

## := NO

A-IIfyou answered YES above, indicated possible date ofoperation and then continue on to h: h. Fuel Data (provide data for each type offuel used) 1. Unit Capacity (MMBtu/hr): 

### 292.4 MMBtu!hr 11. Maximum Fuel Consumption Rate (tons/hI) 

### 28 111. Maximum Natural Gas Firing Rate (MMcf/hr): 

### 0.25 IV. High heating value (Btu/lb): 

### 5000 2. Boiler Unit Outlet Infol111ation (Complete the following exhaust gas parameters for the indicated boiler. Ifthe boiler shares a common stack with anotherboiler, please only provide exhaust infol111ation for the specified boiler). a. Does this unit share an exhaust stack with another unit? (Check One) J YES XNO Ifyou answered YES above, please indicate which other units or emission sources share this stack: b. Maximum Boiler Outlet Volumetric Flowrate 

### (acfm):151000 c. Maximum Boiler Outlet Temperature (F): 

### 500 d. Boiler Outlet Moisture (%):15 e. Stack Height 

### (ft): 102 

### f. Stack Diameter (ft): 7 g. Maximum Gross Heat Input (MMBtu/hr): 

### 292.4 h. Annual Hours ofOperation: 

### 8760 1. Design Percent Load (CapacityFactor): 100 J. 2001

- 2003 Maximum 24-hourAverage PM Emissions (lb/hr): 

### 1.65 k. 2001

- 2003 Maximum 24-hourAverage PM10 Emissions (lb/hr):1.65 

### 1. 2001

- 2003 Maximum 24-hour Average NOx Emissions (lb/hr): 

### 134 m. 2001

- 2003 Maximum 24-hour Average S02 Emissions (lb/hr): 

### 2.75 

### 3. Existing Pollution Control Equipment (Complete the following for each piece ofcontrol equipment, make additional copies to provide infol111ation for all equipment). 

### a. PM Control Technology Infol1nation 1. Type ofPM Control Technology: 

### dry ESP 11. Make/Model ofPMControl Technology: 

### PPC Industries 23R 1431­ 4712 111. Year installed: 

### 1993 IV. Installed Cost ofControl Device ($): 

### $1,300,000 v. Direct Annual Cost ofControl Device ($!yr): VI. Expected life ofequipment: ? Vl1. Relevant sizing information (for example, ifthe control device is an ESP, provide number offields, collector plate area, etc.): 

### 4 fields, 58,229 sq.ft. A-2V111. Design control efficiency (%): 99% IX. 2007 Average Controlled PM Emissions (lbihr): 0.59 x. 2007 Average Controlled PMlo Emissions (lbihr): 0.59 b. NOx Control Technology Infonnation: 1. Type ofNOx Control Technology: none II. MakeiModel ofNOx Control Technology: 111. Year installed: IV. Installed Cost ofControl Device ($): v. DirectAnnual Cost ofControl Device ($iyr): VI. Expected life ofequipment: Vll. Relevant sizing infonnation (Please provide infonnation suHicient to apply the EPA Air Pollution Control Cost Manual

- Sixth Edition (EPA 

### 452iB-02-001) Section 4 - NOx Controls Section 4.2

- NOx PostControl Chapter 1 - Selective Non-Catalytic Reduction and the EPA Air Pollution Control Cost Manual

- Sixth Edition (EPA 

### 452iB-02-001) Section 4 - NOx Controls Section 4.2

- NOx Post-Control Chapter 2 ­ Selective Catalytic Reduction.): V111. Design control efficiency (%):

IX. 2007 Average Controlled NOx Emissions (lbillr): c. 802 Control Technology Infonnation 1. Type ofS02 Control Technology: none 11. MakeiMode1 ofS02 Control Technology: 111. Year installed: IV. Installed Cost ofControl Device 

### ($): v. Direct Annual Cost ofControl Device ($iyr): Vl. Expected life ofequipment: VII. Relevant sizinginformation (for example, ifthe control device is a packed caustic scrubber, provide caustic usage, packing volume, etc.): V111. Design control efficiency (%):

IX. 2007 Average Controlled S02Emissions (lbihr):



### Thefollowing information shouldbe completed usingdatafor theyear 2002. Ifinformation for 2002 is notrepresentative ofcurrent operations (/01' 

### example,**~lthis** 

### unitis no longer using naturalgas), provide in/ormationfor a representativeyear andprovide reasons for why the alternative,veal' is more representative than 2002.

A-34. Fuel Information List Each Type of Fuel Used Amount of fuel used and units Heating Value of Fuel (BmiJb or Btuiscf) Maximum Fuel Firing Rate (tonihr or scUlu') Sulfur Content ofFuel (%S WI.) Year ofdata ifnot 2002 and reason for not using 2002 I I Hog Fuel 157,432 tons 5000 btu/lb 30 tonsihr trace

Natural Gas 20.2 mm scf 1000 btuiscf trace

I I [ 

# L

1. Emission Unit Name: Natural Gas/Diesel Boiler a. Type ofBoiler (e.g., spreader stoker, suspension-fired, fluidized bed): b. Make: 

### Babcock and Wilcox c. Model: 

### D Style d. Model Year: 

### 1993 e. Year installed: 

### 2004 

### f. Expected equipment life: ? g. Unit Is Currently Operational (Check One): X YES 

### J NO Ifyou answered YES above, continue on to h. Ifyou answered NO above, answer the following and then continue to next unit: 1. Date offinal operation: ii. Will this unitbe operated in the future (check one)? ] YES J NO Ifyou answered YES above, indicated possible date ofoperation and then continue on to h: h. Fuel Data (provide data for each type offuel used) 1. Unit Capacity (MMBtu/hr): 

### 96.4 MMBtu/hr H. Maximum Fuel Consumption Rate (tons/hr): HI. Maximum Natural Gas Firing Rate (MMcf/hr): 

### 96170 scf/hr IV, High heating value (Btuilb): 2. Boiler Unit Outlet Infonnation (Complete the following exhaust gas parameters for the indicated boiler. Ifthe boiler shares a common stack with anotherboiler, please onlyprovide exhaust information for the specifiedboiler). a. Does this unit share an exhaust stack with another unit? (Check One) A-4YES X 1\0 Ifyou answered YES above, please indicate which other units or emission sources share this stack: b. Boiler Outlet Volumetric Flowrate (acfm): 26000 c. Boiler OutletTemperature (F): 350 d. Boiler Outlet Moisture (%): 18% e. StackHeight (ft): 75 f. Stack Diameter (ft): 4 g. Maximum Gross Heat Input (MMBtu/hr): 96.4 MMBtu/hr h. I-lours ofOperation: 8760 I. Design Percent Load: 100 

### J. Average Uncontrolled PM Emissions (lb/hr):0.6 k. Average Uncontrolled PMIO Emissions (lb/hr): 0.6 

### 1. Average Uncontrolled NOx Emissions (lb/hr): 6 m. Average Uncontrolled S02 Emissions (lb/hr):O.06 3.Existing Pollution Control Equipment (Complete the following for each piece ofcontrol equipment, make additional copies to provide infonnation for all equipment). a. PM Control Technology Infonnation I. Type ofPM Control Technology: none 11. Make/Model ofPM Control Technology: 111. Year installed: iv. Installed Cost ofControl Device ($): v. Annual Operating Cost ofControl Device (S/yr): VI. Expected life ofequipment: VII. Relevant sizing infom1ation (for example, ifthe control device is an ESP, provide number offields, collectorplate area, etc.): V111. Design control efficiency (%):

IX. Average Controlled PM Emissions (lb/hr): x. Average Controlled PM 10 Emissions (lb/hr): b. NOx Control Technology Inf01111ation: I. Type ofNOx Control Technology: Recycled flue gas 11. Make/Model ofNOx Control Technology: n/a 111. Year installed: 2004 IV. Installed Cost ofControl Device ($): $30,000 v. Annual Operating Cost ofControl Device (S/yr): n/a VI. Expected life ofequipment: ? VII. Relevant sizing information (for example, ifthe control device is an NCSR, provide catalyst volume, system capacity, etc.): n/a V111. Design control efficiency (%): n/a

A-5IX. 

### Average Controlled NOx Emissions (lbihr): 5.7 c. S02 Control Technology Infonnation 1. 

### Type ofS02 Control Technology: none 11. 

### MakeiModel ofS02 Control Technology: 111. 

### Year installed: IV. 

### Installed Cost ofControl Device ($): v. Annual Operating Cost ofControl Device (Siyr): VI. 

### Expected life ofequipment: VII. 

### Relevant sizing infonnation (for example, ifthe control device is a packed caustic scrubber, provide caustic usage, packing volume, etc.): VI1I. 

### Design control efficiency (%):

IX. 

### Average Controlled S02Emissions (lbihr):



### Thefollowing information shouldbe completedusingdatafor theyear2002. If information for 2002 is not representative of current operations ({or example, if 

### this unit is no longer using naturalgas),provide informationfor a representativeyearandprovide reasons for why the alternativeyear is more representative than 2002.

4.Fuel Infonnation

List Each Type of Fuel Used



### Natural Gas

. diesel 

## I ,-­ I I Amount of fuel used and units 

### 160 mmscf

. 4263 gal ! Heating Value of Fuel (Btu/lb or Btu/gal) 

### 1000 btuiscf

17900 btu/lb Maximum Fuel Firing Rate (ton/hr or gal/hr) 

### 96,170 scfihr

750 galihr Sulfur Content ofFuel (%S Wt.)



### trace

trace Year ofdata ifnot 2002 and reason for not using 2002 

### 2005 not installed till 2004 2005 I



## I 1. Emission Unit Name: Veneer dryer (this is a direct tired dryer for dryingwood) a. Type ofBoiler (e.g., spreader stoker, suspension-fired, fluidized bed): fuel cell b. Make: Wellons cell e. Model: 

### nia d. Model Year: 1965

A-6

### e. Year installed: 

### 1965 f. 

### Expected equipment life: 

### ? g. Unit Is Cunently Operational (Check One): X YES 

# =NO 

## r fyou answered YES above, continue on to h. Ifyou answered NO above, answer the follmving and then continue to next unit: 1. 

### Date offinal operation: 11. 

### Will this unit be operated in the future (check one)? YES :::: NO Ifyou answered YES above, indicatedpossible date ofoperation and continue on to h: h. Fuel Data (provide data for each type offuel used) 1. 

### Unit Capacity (MMBtu/hr): 

### 30 MMBtu/hr 11. 

### Maximum Fuel Consumption Rate (tons/In) 2.5 111. 

### Maximum Natural Gas Firing Rate (MMcf/hr): IV. 

### High heating value (Btu/lb): 

### 6000 2. 

### Boiler Unit Outlet Information (Complete the following exhaust gas parameters for the indicated boiler. Ifthe boiler shares a common stack with anotherboiler, please only provide exhaust infonnation for the specified boiler). a. Does this unit share an exhaust stack with another unit? (Check One) ::J 

### YES X NO 

### Ifyou answered YES above, please indicate which other units or emission sources share this stack: b. Boiler Outlet Volumetric Flowrate (acfm): 

### 33,330 c. Boiler OutletTemperature (F): 

### 145 d. Boiler Outlet Moisture (%): 

### 15% e. Stack Height (ft): 

### 60 f. Stack Diameter (ft):4' g. Maximum Gross Heat Input (MMBtu/hr): 

### 30 h. Hours ofOperation: 

### 8760 1. 

### Design Percent Load:I

### 00% J. 

### Average Uncontrolled PM Emissions (lb/hr): ? k. Average Uncontrolled PM10 Emissions (lb/hr): ? 

### 1. Average Uncontrolled NOx Emissions (lb/hr): 1.8 m. Avcrage Cncontrolled S02 Emissions (lb/hr): 0.4 3. Existing Pollution Control Equipment (Complete the following for each piece ofcontrol equipment, make additional copies to provide information for all equipment). a. PM Control Technology Infonnation 1. 

### Type ofPM Control Technology: wet ESP 11. 

### Make/Model ofPM Control Technology: Geoenergy 111. 

### Year installed: 

### 1991 A-7IV. Installed Cost ofControl Device ($):**~$800,OOO** v. Annual Operating Cost ofControl Device ($/yr): VI. Expected life ofequipment: ? VII. Relevant sizing information (for example, ifthe control device is an ESP, provide number offields, collectorplate area, etc.): 176 tubes Vlll. Design control efficiency (%): 99%

IX. Average Controlled PM Emissions (lb/hr): 1.2 x. Average Controlled PM 10 Emissions (lb/hr): 1.2 b. NOx Control Technology Information: J. Type ofNOx Control Technology: none II. Make/Model ofNOx Control Technology: 111. Year installed: IV. Installed Cost ofControl Device ($): v. Annual Operating Cost ofControl Device ($/yr): VI. Expected life ofequipment: V11. Relevant sizing infonnation (for example, ifthe control device is an NCSR, provide catalyst volume, system capacity, etc.): Vlll. Design control efficiency (%):

IX. Average ControlledNOx Emissions (lb/hr): c. S02 Control Technology Infonnation I. Type ofS02 Control Technology: none II. Make/Model ofS02 Control Technology: 111. Year installed: IV. Installed Cost ofControl Device ($): v. Annual Operating Cost ofControl Device ($/yr): VI. Expected life ofequipment: VII. Relevant sizing infonnation (for example, ifthe control device is a packed caustic scrubber, provide causticusage, packing volume, etc.): VUI. Design control efficiency (%):

IX. Average Controlled S02Emissions (lb/hr):



### Thefollowing information shouldbe completed usingdatafor theyear 2002. If information for 2002 is not representative of current operations ({or example, if this unit is no longer using naturalgas),provide informationfor a representativeyear andprovide reasonsfor why the alternativeyear is more representative thall 2002.

A-84.Fucl Information List Each Type of Fuel Used Amount of fuel used and units Heating Value of Fuel (Btu/lb orBtulsct) Maximum Fuel Firing Rate (ton/hr or scf/hr) Sulfur Content ofFuel (%S Wl.) Year ofdata ifnot 2002 and reason for not using 2002 Hog fuel 18160 tons 6000 btu/lb 2.5 tons/hr trace 2002



# I

Part III: MDF Fiber Dryers (Please complete entire section for each Fiber dryer, additional copies may be necessary) 

### 1. Emission Unit Name: Line 1MDF Fiber Dryers (used for direct fired wood fiber drying) a. Make:eoen SanderDust burners b. Model: 50 mmbtu/hr each (two ofthem) c. Model Year: d. Year Installed: 

### 1986 and 

### 2006 e. Expected equipment life: 

### ? f. Unit Is Currently Operational (Check One): X YES 

# = NO Ifyou answered YES above, continue on to g. Ifyou answered NO above, answer the following and then continue to next unit: I. Date offinal operation: tl. Will this unit be operated in the future (check one)?**~~** YES NO Ifyou answered YES above, indicated possible date ofoperation and then continue on to g: g. Fuel data: 1. Unit Capacity (MMBtu/hr): 50 MMBtu/hr each 11. Maximum Drying Capacity (ton/hr ofbone dry fiber): 57 111. Maximum Sanderdust Firing Rate (MMcflhr): 6.7 tons/hr tv. Ifother fuels are bumed in boiler as supplemental fuel, please list each fuel and its maximum fuel firing rate (MMBtul/hr). v. Maximum Sulfur Content ofeach supplemental fuel listed in (iv.) (%): trace 

### A-92. Unit Stack Infol111ation (Complete the following exhaust gas parameters for the indicated unit. 

### Ifthe unit shares a common stack with another unit, please onlyprovide exhaust infol111ation for the specified unit). a. Does this unit share an exhaust stack with another unit? (Check One) X YES 

### :=: NO Ifyou ans\vered YES above, please indicate which other units or emission sources sharethis stack: Line 1 press vents and metering bin baghouse b. Stack Volumetric Flowrate (acfil1): 280000 c. Stack Exhaust Temperature (F): 150 fOi' the wet 

### ESP d. Stack Exhaust Moisture (%): 20% e. Stack Height (ft):80 

### f. StackDiameter (ft): 12 ft each (there are two stacks out ofthe biofilter) 

### g. Maximum Gross Heat Input (MMBtulhr): 100 mmBTU/hr h. Hours ofOperation:8500 1. Design Percent Load: 

### J. Average Uncontrolled PM Emissions (lb/hr): ? k. Average Uncontrolled PMIQ Emissions (lb/hr):? 

### 1. Average Uncontrolled NO

### x Emissions (lb/hr): 75 m. Average Uncontrolled S02 Emissions (lb/hr): 1.0 3. Existing Pollution Control Equipment (Complete the following for each piece ofcontrol equipment, make additional copies to provide infonl1ation for all equipment). a. PM Control Technology Information 1. Type ofPM Control Technology: wet ESP 11. Make/Model ofPM Control Technology: GeoEnergy 111. Year installed: 1995 IV. Installed Cost ofControl Device ($): $6,000,000 v. Annual Operating Cost ofControl Device (S/yr): VI. Expected life ofequipment: ? V11. Relevant sizing infonnation (for example, ifthe control device is an ESP, providenumber offields, collector plate area, etc.): 1200 tubes V11I. Design control efficiency (%): 99%

IX. Average Controlled PM Emissions (lblhr): 13.5 

### x. Average Controlled PMIQ Emissions (lb/hr): 13.5 b. NO

### x Control Technology Infol111ation: 1. Type ofNO

### x Control Technology: none 11. Make/Model ofNOx Control Technology: lll. Year installed: IV. Installed Cost ofControl Device ($):

A-I0

### v. Annual Operating Cost ofControl Device ($/yr): v\. Expected life ofequipment: Vll. 

### Relevant sizing infonnation (for example, ifthe control device is an NCSR, provide catalyst volume, system capacity, etc.): Vl11. 

### Design control efficiency (%):

IX. 

### Average Controlled NOx Emissions (lb/hr): c. S02 Control Technology Inf01111ation 1. 

### Type ofS02 Control Technology: none 11. 

### Make/Model ofS02 Control Technology: 111. 

### Year installed: IV. 

### Installed Cost ofControl Device 

### ($): v. Annual Operating Cost ofControl Device ($/yr): VI. 

### Expected equipment life: Vl1. 

### Relevant sizing information (for example, ifthe control device is a packed caustic scrubber, provide caustic usage, packing volume, etc.): Vl11. 

### Design control efficiency (%):

IX. 

### Average Controlled S02 Emissions (lb/hr): 

### The/ollowing i,?!ormation shouldbe completed using data/or theyear 2002. !fin/ormationfor 2002 is not representative of current operations (for example, 

## if this unit is 

### no longer using naturalgas), provide informationfor a representativeyearandprovide reasonsfor why the alternativeyear is 

### more representative than 2002. 4. Fuel Infonnation

List Each Type of Fuel Used 

### sanderdust Amount of Fuel Used and Units 

### 52890 tons Heating Value of Fuel (Btu/lb orBtu/set) 

### 8000 BTU/lb Maximum Fuel Firing Rate (ton/hr or scUhr) 

### 6.25 tons/hr Sulfur Content ofFuel (%S WI.) 

### trace Year ofdata ifnot 2002 and reason for not using 2002 

### 2002

:

# rI i I I i 

## i I

1. 

### Emission Unit Name: Line 2 MDF Fiber Dryers A-II

### a. Make: Coen Sander Dust burners b. Model:85 mm BTU/hr c. !v1odel Year:200 1 d. Year Installed:2001 c. Expected equipment life:? 

## r Unit Is Currently Operational (Check One): X YES -: NO Ifyou answered YES above, continue on to g. Ifyou answered NO above, answer the following and then continue to next unit:

1. 

### Date offinal operation: 11. 

### Will this unit be operated in the future (check one)? J 

### YES :::J 

### NO Ifyou answered YES above, indicated possible date ofoperation and then continue on to g: g. Fuel data: 1. 

### Unit Capacity (MMBtu/hr): 85 IVIIVIBtu/hr 11. 

### Maximum Drying Capacity (ton/hr ofbone dry fiber): 49 ton/hr 111. 

### Maximum SanderdustFiring Rate (MMcf/hr): 5.3 tons/hr IV. 

### Ifother fuels are burned in boiler as supplemental fuel, please list each fuel and its maximum fuel firing rate (MMBtul/hr). 

### natural gas 80 mm BTU/hr v. Maximum Sulfur Content ofeach supplemental fuel listed in (l.g.iv.) (%): 

### trace 2. Unit Stack Information If

### this unit exhausts to a shared stack, please provide the exhaust infon11ation below before the shared outlet. a. Stack Volumetric Flowrate (acfm): 600,000 b. Stack Exhaust Temperature (F): 105 c. Stack Exhaust Moisture (%): 

### 9% d. Stack Height (ft): 40 e. Stack Diameter (ft):8.5ft each 3 ofthem f. 

### Maximum Gross Heat Input (MMBtu/hr): 85 g. Hours ofOperation: 8760 h. Design Percent Load: 1. 

### Average Uncontrolled PM Emissions (lb/hr): ? 

### J. Average Uncontrolled PMIO 

### Emissions (lb/hr): k. Average Uncontrolled NOx Emissions (lb/hr): 45.6 1. 

### Average Uncontrolled S02 Emissions (lb/hr): 0.85 m. Does this unit share an exhaust stack with another unit?

# = YES == 

### NO 3. Existing Pollution Control Equipment (Complete the following for each piece ofcontrol equipment, make additional copies to provide information for all equipment).



### A-12a. P\I1. Control Technology Information I. Type ofPM Control Technology: 

### venturi scrubber II. Make/Model ofPM Control Technology: 

### Geoenergy 111. Year installed: 

### 200] IV. Installed Cost ofControl Device ($):**~$800,000** v. Annual Operating Cost ofControl Device ($/yr): VI. Expected life ofequipment? VII. Relevant sizing information (for example, ifthe control device is an ESP, provide number offields, collector plate area, etc.): VIII. Design control efficiency (%):

IX. Average Controlled PM Emissions (lb/hr): 

### 21.2 x. Average Uncontrolled PM IO Emissions (lb/hr):21.2 b. NO;.: Control Technology Information: I. Type ofNOx Control Technology: 

### staged burning II. Make/Model ofNOx Control Technology: 

### Coen 111. Year installed: 

### 2001 IV. Installed Cost ofControl Device ($): 

### nla v. AIIDual Operating Cost ofControl Device ($/yr): 

### nla VI. Expected life ofequipment? V11. Relevant sizing infonnation (for example, ifthe control device is an NCSR, provide catalyst volume, system capacity, etc.): ? Vlll. Design control efficiency 

### (%): ?

IX. Average ControlledNOx Emissions (lb/hr): 

### 45.6 c. SOz Control Technology Infonnation I. Type ofS02 Control Technology: 

### none II. Make/Model ofS02 Control Technology: 111. Year installed: IV. Installed Cost ofControl Device 

### ($): v. Annual Operating Cost ofControl Device ($/yr): VI. Expected equipment life: VII. Relevant sizing information (for example, ifthe control device is a packed caustic scrubber, provide caustic usage, packing volume, etc.): VIII. Design control efficiency 

### (%):

IX. Average Controlled SOz Emissions (lb/hr): 

### Thefollmving il?formation shouldbe completed using datafor theyear 2002. ffil?formationfor 2002 is 

### not representative of current operations (for example, (fthis unit is 

### no longer using naturalgas), provide il?formationfor a representativeyearandprovide reasonsfor why the alternativeyear is 

### more representative than 2002.

A-134. Fuel Information

List Eaeh Type of Fuel Used sanderdust Amount of Fuel Used and Units 45940 tons Heating Value of Fuel (Btullb or Btu/se±) 8000 BTU/lb Maximum Fuel Firing Rate (ton/hI' or se£!hr) 5.3 ton/hr Sulfur Content ofFuel (%S WI.) trace

1 Year ofdata ifnot 2002 and reason for not using 2002 2002 I I

II

I

I 

## I

A-14