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 

of those 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 of fine or 

imprisonment. 

Signaturc 

\ I ,) 

v \ ' 

Title 
Attachment A
 

Plum Creek Northwest Lumber, Inc.
 

Request for Information Pursuant to Section 114 of the CAA
 

Part I: General Facility Data 

I.	 Name of facility: Plum Creek Manufacturing, L.P. - Ksanka Mill Site 

2.	 Complete street address of facility (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 of Section 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 of Boiler (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 

Ir you answered YES ab()\'e. continue on to h. If you answered NO above, answer 

the following and thcn continue to next unit: 

I.	 Date of tinal operation: 

11.	 Will this unit be opcrated in the future (check onc)?
 

A-I
 
::: YES =NO 

If you ans\vered YES above, indicate possible date of operation and continue to h: 

h.	 Unit Capacity (MMBtu/hr): 20 J\fMBtu/hr 

'I	 Boiler Unit Outlet Information 

If this 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 of Operation: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 of control 

equipment, make additional copies to provide infonnation for all equipment). 

a.	 PM Control Technology Inf0l111ation 

1. Type of PM Control Technology: multiclone 

II. Make/Model of PM Control Technology: Wellons 

111. Year installed: 1979 

IV. Installed Cost of Control Device (S): ? 

v. Annual Operating Cost of Control Device ($/yr):n/a 

VI. Expected life of equipment: ? 

V11. Relevant sizing infoD11ation (for example, if the control device is an 

ESP, provide number of fields, 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 of NOx Control Technology: none 

11. Make/Model of NOx Control Technology: 

111. Year installed: 

IV. Installed Cost of Control Device ($): 

v. Annual Operating Cost of Control Device (S/yr): 

VI. Expected life of equipment: 

A-2 
V11. Relcvant sIzing information (for example, if the 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 of S02 Control Technology: none 

II. Make/Model of S02 Control Technology: 

111. Year installed: 

IV. Installed Cost of Control Device ($): 

v. Annual Operating Cost of Control Device ($/yr): 

VI. Expected life of equipment: 

VII. Relevant sizing information (for example, if the 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 should be completed using data for the year 2002. Ifinformation 

for 2002 is not representative o.!,curl'ent operations (/01' example, ({this unit is no longer using 

natural gas), provide iJ~{ormation for a representative year and provide reasons for why the 

alternative year 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 

of Fuel 

(%S Wt.) 

Year of data if not 

2002 and reason 

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 of the CAA 

Part I: General Facility Data 

1.	 Name of facility: Plum Creek Manufacturing, L.P. - Evergreen Division 

2.	 Complete street address of facility (physical location): 

a.	 Street Address: 75 Sunset Drive SW of Section 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 of Boiler (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 

If you answered YES above, continue on to h. If you answered NO above, answer 

the following and then continue to next unit: 

1. Date of final operation: 

11. Will this unit be operated in the future (check one)? 

A-I 
J YES 

If you answered YES above, indicatc possible date of operation and continue to h: 

h.	 Unit Capacity (MMBtu/hr): 196 MMBtu/hr 

2.	 Boiler Unit Outlet Information 

If this unit exhausts to a shared stack, please provide the exhaust information below before 

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 of Operation:8760 

h.	 Design Percent Load:100 

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

J.	 Average Uncontrolled NOx 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 of control 

equipment, make additional copies to provide information for all equipment). 

a.	 PM Control Technology Infonnation 

1. Type of PM Control Technology: dry ESP 

11. Make/Model of PM Control Technology: PPC Industries 23R-1331­

3712
 

Ill. Year installed:1992
 

IV. Installed Cost of Control Device ($): -$1,000,000 

v. Annual Operating Cost of Control Device ($/yr): ? 

VI. Expected life of equipment: ? 

VII. Relevant sizing infom1ation (for example, if the control device is an 

ESP, provide number of fields, 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 of NOx Control Technology: none 

II. Make/Model of NOx Control Technology: 

111. Year installed: 

IV. Installed Cost of Control Device (S): 

v. Annual Operating Cost of Control Device ($/yr): 

A-2 
VI. Expected life of equipment: 

VII. Relevant sizing information (for example, if the 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 of S02 Control Technology: none 

11. Make/Model of S02 Control Technology: 

111. Year installed: 

IV. Installed Cost of Control Device ($): 

v. Annual Operating Cost of Control Device ($/yr): 

VI. Expected life of equipment: 

VB. Relevant sizing infOlmation (for example, if the control device is a 

packed caustic scrubber, provide caustic usage, packing volume, etc.): 

Vll1. Design control efficiency (%): 

IX. Average Controlled S02 Emissions (lb/hr): 

Thefo/loJVing information should be completed using datafor the year 2002. Ifinformation 

for 2002 is not representative ofcurrent operations (for example, ifthis unit is no longer using 

natural gas), provide information for a representative year andprovide reasons for why the 

alternative year is more representative than 2002. 

4. Fuel Information 

Amount of Heating Value of Maximum Fuel Sulfur Content Year of data if not 

List Each Type of Fuel Used Fuel Firing Rate of Fuel 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-3 
Attachment A
 

Plum Creek Manufacturing, L.P.
 

Request for Information Pursuant to Section 114 of the CAA
 

Part I: General Facility Data 

1.	 Name of facility: Plum Creek Manufacturing, L.P. Columbia Falls Operations 

2.	 Complete street address of facility (physical location): 

a.	 Street Address: 500 12th Ave West 

Section 7 and the SW of Section 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 of Boiler (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 

If you answered YES above, continue on to h. If you answered NO above, answer 

the following and then continue to next unit: 

1. Date of final operation: 

11.	 Will this unit be operated in the future (cheek one)? 

:= YES := NO 

A-I
 
If you answered YES above, indicated possible date of operation and then continue 

on to h: 

h.	 Fuel Data (provide data for each type of fuel 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. If the boiler shares a common stack with another boiler, 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 

If you 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 of Operation: 8760 

1.	 Design Percent Load (Capacity Factor): 100 

J.	 2001 - 2003 Maximum 24-hour Average PM Emissions (lb/hr): 1.65 

k.	 2001 - 2003 Maximum 24-hour Average 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 of control 

equipment, make additional copies to provide infol111ation for all equipment). 

a.	 PM Control Technology Infol1nation 

1.	 Type of PM Control Technology: dry ESP 

11.	 Make/Model of PM Control Technology: PPC Industries 23R 1431­

4712 

111.	 Year installed: 1993 

IV.	 Installed Cost of Control Device ($): $1,300,000 

v.	 Direct Annual Cost of Control Device ($!yr): 

VI.	 Expected life of equipment: ? 

Vl1.	 Relevant sizing information (for example, if the control device is an 

ESP, provide number of fields, collector plate area, etc.): 4 fields, 

58,229 sq.ft. 

A-2 
V111.	 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 of NOx Control Technology: 

111.	 Year installed: 

IV.	 Installed Cost of Control Device ($): 

v. DirectAnnual Cost of Control Device ($iyr): 

VI.	 Expected life of equipment: 

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-02-00 1) 

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 of S02 Control Technology: none 

11. MakeiMode1 of S02 Control Technology: 

111.	 Year installed: 

IV.	 Installed Cost of Control Device ($): 

v. Direct Annual Cost of Control Device ($iyr): 

Vl. Expected life of equipment: 

VII.	 Relevant sizing information (for example, if the control device is a 

packed caustic scrubber, provide caustic usage, packing volume, etc.): 

V111. Design control efficiency (%): 

IX.	 2007 Average Controlled S02 Emissions (lbihr): 

The following information should be completed using data for the year 2002. Ifinformation 

for 2002 is not representative of current operations (/01' example, ~lthis unit is no longer using 

natural gas), provide in/ormation for a representative year and provide reasons for why the 

alternative ,veal' is more representative than 2002. 

A-3
 
4. 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 

of Fuel 

(%S WI.) 

Year of data if not 

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 of Boiler (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 

If you answered YES above, continue on to h. If you answered NO above, answer 

the following and then continue to next unit: 

1.	 Date offinal operation: 

ii.	 Will this unit be operated in the future (check one)? 

] YES J NO 

If you answered YES above, indicated possible date of operation 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. If the boiler shares a common stack with another boiler, please only provide 

exhaust information for the specified boiler). 

a.	 Does this unit share an exhaust stack with another unit? (Check One) 

A-4 
YES X 1\0 

If you answered YES above, please indicate which other units or emission sources 

share this stack: 

b. Boiler Outlet Volumetric Flowrate (acfm): 26000 

c. Boiler Outlet Temperature (F): 350 

d. Boiler Outlet Moisture (%): 18% 

e. Stack Height (ft): 75 

f. Stack Diameter (ft): 4 

g. Maximum Gross Heat Input (MMBtu/hr): 96.4 MMBtu/hr 

h. I-lours of Operation: 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 of control 

equipment, make additional copies to provide infonnation for all equipment). 

a. PM Control Technology Infonnation 

I. Type of PM Control Technology: none 

11. Make/Model of PM Control Technology: 

111. Year installed: 

iv. Installed Cost of Control Device ($): 

v. Annual Operating Cost of Control Device (S/yr): 

VI. Expected life of equipment: 

VII. Relevant sizing infom1ation (for example, if the control device is an ESP, 

provide number of fields, collector plate area, etc.): 

V111. Design control efficiency (%): 

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

x. Average Controlled PM10 Emissions (lb/hr): 

b. NOx Control Technology Inf01111ation: 

I. Type of NOx Control Technology: Recycled flue gas 

11. Make/Model of NOx Control Technology: n/a 

111. Year installed: 2004 

IV. Installed Cost of Control Device ($): $30,000 

v. Annual Operating Cost of Control Device (S/yr): n/a 

VI. Expected life of equipment: ? 

VII. Relevant sizing information (for example, if the control device is an 

NCSR, provide catalyst volume, system capacity, etc.): n/a 

V111. Design control efficiency (%): n/a 

A-5
 
IX. Average Controlled NOx Emissions (lbihr): 5.7 

c. S02 Control Technology Infonnation 

1. Type of S02 Control Technology: none 

11. MakeiModel of S02 Control Technology: 

111. Year installed: 

IV. Installed Cost of Control Device ($): 

v. Annual Operating Cost of Control Device (Siyr): 

VI. Expected life of equipment: 

VII. Relevant sizing infonnation (for example, if the control device is a packed 

caustic scrubber, provide caustic usage, packing volume, etc.): 

VI1I. Design control efficiency (%): 

IX. Average Controlled S02 Emissions (lbihr): 

The following information should be completed using data for the year 2002. Ifinformation 

for 2002 is not representative ofcurrent operations ({or example, ifthis unit is no longer using 

natural gas), provide information for a representative year and provide reasons for why the 

alternative year 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 

of Fuel 

(%S Wt.) 

trace 

trace 

Year of data if not 

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 drying wood) 

a. Type of Boiler (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 

rf you answered YES above, continue on to h. If you answered NO above, answer the 

follmving and then continue to next unit: 

1. Date of final operation: 

11. Will this unit be operated in the future (check one)? 

YES :::: NO 

If you answered YES above, indicated possible date of operation and continue on to h: 

h.	 Fuel Data (provide data for each type of fuel 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. If the boiler shares a common stack with another boiler, 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 

If you answered YES above, please indicate which other units or emission sources 

share this stack: 

b.	 Boiler Outlet Volumetric Flowrate (acfm): 33,330 

c.	 Boiler Outlet Temperature (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 of Operation: 8760 

1.	 Design Percent Load: I00% 

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 of control 

equipment, make additional copies to provide information for all equipment). 

a.	 PM Control Technology Infonnation 

1.	 Type of PM Control Technology: wet ESP 

11.	 Make/Model of PM Control Technology: Geoenergy 

111. Year installed: 1991 

A-7
 
IV. Installed Cost of Control Device ($): ~$800,OOO

v. Annual Operating Cost of Control Device ($/yr): 

VI. Expected life of equipment: ? 

VII. Relevant sizing information (for example, if the control device is an ESP, 

provide number of fields, collector plate area, etc.): 176 tubes 

Vlll. Design control efficiency (%): 99% 

IX. Average Controlled PM Emissions (lb/hr): 1.2 

x. Average Controlled PM10 Emissions (lb/hr): 1.2 

b. NOx Control Technology Information: 

J. Type of NOx Control Technology: none 

II. Make/Model ofNOx Control Technology: 

111. Year installed: 

IV. Installed Cost of Control Device ($): 

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

VI. Expected life of equipment: 

V11. Relevant sizing infonnation (for example, if the control device is an 

NCSR, provide catalyst volume, system capacity, etc.): 

Vlll. Design control efficiency (%): 

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

c. S02 Control Technology Infonnation 

I. Type of S02 Control Technology: none 

II. Make/Model of S02 Control Technology: 

111. Year installed: 

IV. Installed Cost ofControl Device ($): 

v. Annual Operating Cost of Control Device ($/yr): 

VI. Expected life of equipment: 

VII. Relevant sizing infonnation (for example, if the control device is a packed 

caustic scrubber, provide caustic usage, packing volume, etc.): 

VUI. Design control efficiency (%): 

IX. Average Controlled S02 Emissions (lb/hr): 

The following information should be completed using data for the year 2002. Ifinformation 

for 2002 is not representative of current operations ({or example, ifthis unit is no longer using 

natural gas), provide information for a representative year and provide reasonsfor why the 

alternative year is more representative thall 2002. 

A-8
 
4.Fucl Information 

List Each Type of 

Fuel Used 

Amount of 

fuel used 

and units 

Heating Value of 

Fuel 

(Btu/lb or Btulsct) 

Maximum Fuel 

Firing Rate 

(ton/hr or scf/hr) 

Sulfur Content 

of Fuel 

(%S Wl.) 

Year of data if not 

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 Sander Dust burners 

b.	 Model: 50 mmbtu/hr each (two of them) 

c.	 Model Year: 

d.	 Year Installed: 1986 and 2006 

e.	 Expected equipment life: ? 

f.	 Unit Is Currently Operational (Check One): X YES =NO 

If you answered YES above, continue on to g. If you answered NO above, answer 

the following and then continue to next unit: 

I. Date of final operation:
 

tl. Will this unit be operated in the future (check one)?
 

~~ YES NO 

If you answered YES above, indicated possible date of operation and then continue 

on to g: 

g.	 Fuel data: 

1. Unit Capacity (MMBtu/hr): 50 MMBtu/hr each 

11.	 Maximum Drying Capacity (ton/hr of bone dry fiber): 57 

111.	 Maximum Sanderdust Firing Rate (MMcflhr): 6.7 tons/hr 

tv.	 If other fuels are bumed in boiler as supplemental fuel, please list each fuel and 

its maximum fuel firing rate (MMBtul/hr). 

v.	 Maximum Sulfur Content of each supplemental fuel listed in (iv.) (%): trace 

A-9 
2.	 Unit Stack Infol111ation (Complete the following exhaust gas parameters for the indicated 

unit. If the unit shares a common stack with another unit, please only provide exhaust 

infol111ation for the specified unit). 

a.	 Does this unit share an exhaust stack with another unit? (Check One) 

X YES :=: NO 

If you ans\vered YES above, please indicate which other units or emission sources 

share this 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.	 Stack Diameter (ft): 12 ft each (there are two stacks out of the biofilter) 

g.	 Maximum Gross Heat Input (MMBtulhr): 100 mmBTU/hr 

h.	 Hours of Operation:8500 

1.	 Design Percent Load: 

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

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

1.	 Average Uncontrolled NOx Emissions (lb/hr): 75 

m.	 Average Uncontrolled S02 Emissions (lb/hr): 1.0 

3.	 Existing Pollution Control Equipment (Complete the following for each piece of control 

equipment, make additional copies to provide infonl1ation for all equipment). 

a.	 PM Control Technology Information 

1. Type of PM Control Technology: wet ESP 

11. Make/Model of PM Control Technology: GeoEnergy 

111. Year installed: 1995 

IV. Installed Cost of Control Device ($): $6,000,000 

v. Annual Operating Cost of Control Device (S/yr): 

VI. Expected life of equipment: ? 

V11. Relevant sizing infonnation (for example, if the control device is an 

ESP, provide number of fields, 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.	 NOx Control Technology Infol111ation: 

1. Type of NOx Control Technology: none 

11. Make/Model of NOx Control Technology: 

lll. Year installed: 

IV. Installed Cost of Control Device ($): 

A-I0 
v. Annual Operating Cost of Control Device ($/yr): 

v\. Expected life of equipment: 

Vll. Relevant sizing infonnation (for example, if the 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 of S02 Control Technology: none 

11. Make/Model of S02 Control Technology: 

111. Year installed: 

IV. Installed Cost of Control Device ($): 

v. Annual Operating Cost of Control Device ($/yr): 

VI. Expected equipment life: 

Vl1. Relevant sizing information (for example, if the 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 should be completed using data/or the year 2002. !fin/ormationfor 

2002 is not representative ofcurrent operations (for example, ifthis unit is no longer using 

natural gas), provide information for a representative year and provide reasons for why the 

alternative year 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 or Btu/set) 

8000 BTU/lb 

Maximum Fuel 

Firing Rate 

(ton/hr or scUhr) 

6.25 tons/hr 

Sulfur Content 

of Fuel 

(%S WI.) 

trace 

Year of data if not 

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 

If you answered YES above, continue on to g. If you answered NO above, answer 

the following and then continue to next unit: 

1.	 Date of final operation: 

11. Will this unit be operated in the future (check one)? 

J YES :::J NO 

If you answered YES above, indicated possible date of operation and then 

continue on to g: 

g.	 Fuel data: 

1.	 Unit Capacity (MMBtu/hr): 85 IVIIVIBtu/hr 

11.	 Maximum Drying Capacity (ton/hr of bone dry fiber): 49 ton/hr 

111.	 Maximum Sanderdust Firing Rate (MMcf/hr): 5.3 tons/hr 

IV.	 If other 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 of each 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 of them 

f.	 Maximum Gross Heat Input (MMBtu/hr): 85 

g.	 Hours of Operation: 8760 

h.	 Design Percent Load: 

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

J.	 Average Uncontrolled PM IO 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 of control 

equipment, make additional copies to provide information for all equipment). 

A-12 
a. P\I1. Control Technology Information 

I. Type of PM Control Technology: venturi scrubber 

II. Make/Model of PM Control Technology: Geoenergy 

111.	 Year installed: 200] 

IV.	 Installed Cost of Control Device ($): ~$800,000

v. Annual Operating Cost of Control Device ($/yr): 

VI.	 Expected life of equipment? 

VII.	 Relevant sizing information (for example, if the control device is an 

ESP, provide number of fields, collector plate area, etc.): 

VIII.	 Design control efficiency (%): 

IX.	 Average Controlled PM Emissions (lb/hr): 21.2 

x. Average Uncontrolled PMIO Emissions (lb/hr):21.2 

b. NO;.: Control Technology Information: 

I. Type of NOx Control Technology: staged burning 

II. Make/Model ofNOx Control Technology: Coen 

111.	 Year installed: 2001 

IV.	 Installed Cost of Control Device ($): nla 

v. AIIDual Operating Cost of Control Device ($/yr): nla 

VI. Expected life of equipment? 

V11. Relevant sizing infonnation (for example, if the control device is an 

NCSR, provide catalyst volume, system capacity, etc.): ? 

Vlll. Design control efficiency (%): ? 

IX.	 Average Controlled NOx Emissions (lb/hr): 45.6 

c. SOz Control Technology Infonnation 

I. Type of S02 Control Technology: none 

II. Make/Model of S02 Control Technology: 

111.	 Year installed: 

IV.	 Installed Cost of Control Device ($): 

v. Annual Operating Cost of Control Device ($/yr): 

VI.	 Expected equipment life: 

VII.	 Relevant sizing information (for example, if the control device is a 

packed caustic scrubber, provide caustic usage, packing volume, etc.): 

VIII.	 Design control efficiency (%): 

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

The follmving il?formation should be completed using data for the year 2002. ff il?formationfor 

2002 is not representative ofcurrent operations (for example, (f this unit is no longer using 

natural gas), provide il?formation for a representative year and provide reasons for why the 

alternative year is more representative than 2002. 

A-13 
4. 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 

of Fuel 

(%S WI.) 

trace 

1 

Year of data if not 

2002 and reason 

for not using 2002 

2002 

I 

I 

II 

I 

I 

I 

A-14