Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit Category/ sub-category Run #

Method 

used (5, 

17, 26A, 

29,)

Sample time 

(min.)

Sample 

volume 

(dscf)

Filter 

temperature 

(avg. deg. f)

Percent 

H2O (Bws)

Mass - Filter 

(mg)

Mass - Rinse 

(mg)

Re-calculated Based 

on zero filter for 

negative values

Revised Catch 

based on 64 FR 

53028

AK Doyon Utilities/ Unit 4

Solid/Coal 4 5 60 60.2 246 9.6

0.8 2.8

AK Doyon Utilities/ Unit 4 Solid/Coal 5 5 60 61.4 246 11.2 0.6 3.9

AK Doyon Utilities/ Unit 4 Solid/Coal 6 5 60 59.1 247 10.3 0.7 4.4

AK Doyon Utilities/ Unit 7 Solid/Coal 1 5 60 60.7 255 10.1 1.9 3.9

AK Doyon Utilities/ Unit 7 Solid/Coal 2 5 60 59.7 252 10.9 3 4.2

AK Doyon Utilities/ Unit 7 Solid/Coal 3 5 60 56.6 250 9.9 1.3 5.2

AR Weyerhaeuser Dierks Mill / Unit 5 (1997) Solid/Biomass 1 5 60 52.1 255 12.44 7.2 17.4

AR Weyerhaeuser Dierks Mill / Unit 5 (1997) Solid/Biomass 2 5 60 54.4 255 12.48 7.5 12.4

AR Weyerhaeuser Dierks Mill / Unit 5 (1997) Solid/Biomass 3 5 60 50.8 255 13.37 3.5 6.9

AR Weyerhaeuser Dierks Mill/ Unit 7 (1997) Solid/Biomass 1 5 120 77.8 200 17.34 2.2 58.6

AR Weyerhaeuser Dierks Mill/ Unit 7 (1997) Solid/Biomass 2 5 120 80.9 255 19.08 1.8 32.1

AR Weyerhaeuser Dierks Mill/ Unit 7 (1997) Solid/Biomass 3 5 120 78.5 250 18.75 1.1 24.3

FL Smurfit-Stone Solid/Coal 1 5/26a 60 45.5 250 4.93 1.3 2.7

FL Smurfit-Stone Solid/Coal 2 5/26a 60 46.2 250 4.3 0 2.1

FL Smurfit-Stone Solid/Coal 3 5/26a 60 44.3 252 4.08 0 7.1

GA GP Monticello Plywood (2/21/08) Solid/Biomass 1 5 120 91.9 245 13.01 3.8 0

GA GP Monticello Plywood (2/21/08) Solid/Biomass 2 5 120 100.0 245 12.41 1.8 1.1

GA GP Monticello Plywood (2/21/08) Solid/Biomass 3 5 120 95.1 235 14.32 1.2 0.4

GA GP Monticello Plywood (2/7/07) Solid/Biomass 1 5 120 92.8 250 20.05 6.7 8.3

GA GP Monticello Plywood (2/7/07) Solid/Biomass 2 5 120 89.2 250 18.68 8.1 13.6

GA GP Monticello Plywood (2/7/07) Solid/Biomass 3 5 120 93.1 250 17.02 0.9 15

IA ADM Corn Processing Cedar Rapids Solid/Coal 1 5 120 67.6 265 11.7 0 4.3

IA ADM Corn Processing Cedar Rapids Solid/Coal 2 5 120 62.9 267 9.83 0 8.6

IA ADM Corn Processing Cedar Rapids Solid/Coal 3 5 120 64.8 265 11.41 0 2.2

IA Iowa State University B1 Solid/Coal 1 17/202 62.5 35.6 6 0.5 0.2

IA Iowa State University B1 Solid/Coal 2 17/202 62.5 35.5 7.7 0.6 0.4

IA Iowa State University B1 Solid/Coal 3 17/202 62.5 34.5 7.8 0.6 1.1

IA Iowa State University B2

Solid/Coal 1 17/202 62.5 35.4 7.4

0.3 0.3 1

IA Iowa State University B2 Solid/Coal 2 17/202 62.5 36.5 8.2 0 0.7

IA Iowa State University B2

Solid/Coal 3 17/202 62.5 35.3 8.4

0.4 0.1 1

IA Monsanto Muscatine #8 Cond. 1 (5/2007) Solid/Biomass 2 5 60 40.6 10.2 1.15 7.4

IA Monsanto Muscatine #8 Cond. 1 (5/2007) Solid/Biomass 3 5 60 40.8 10.7 2.05 5.5

IA Monsanto Muscatine #8 Cond. 1 (5/2007) Solid/Biomass 10 5 60 39.2 10.4 4.2 6.8

IA Monsanto Muscatine #8 Cond. 3 (5/2007)

Solid/Biomass 7 5 60 39.8 7.2

1.1 6.5

IA Monsanto Muscatine #8 Cond. 3 (5/2007) Solid/Biomass 8 5 60 39.5 7.4 1.7 4.55

IA Monsanto Muscatine #8 Cond. 3 (5/2007) Solid/Biomass 9 5 60 40.6 7.6 3.45 7.95

IA Monsano Muscatine #8 Cond. 1 (8/2007) Solid/Biomass 1 5 60 41.8 11.9 2.25 6.3

IA Monsano Muscatine #8 Cond. 1 (8/2007) Solid/Biomass 2 5 60 40.4 12.6 1.95 8.75

IA Monsano Muscatine #8 Cond. 1 (8/2007) Solid/Biomass 3 5 60 40.7 11.9 0.95 6.15

ID Amalgamated Suger Co. Twin Falls Solid/Coal 1 5/202 120 77.5 250 6.7 0 5.6

ID Amalgamated Suger Co. Twin Falls Solid/Coal 2 5/202 120 76.9 245 6.67 2 6.9

ID Amalgamated Suger Co. Twin Falls Solid/Coal 3 5/202 120 78.9 245 7.22 1.8 9.3
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit Category/ sub-category Run #

Method 

used (5, 

17, 26A, 

29,)

Sample time 

(min.)

Sample 

volume 

(dscf)

Filter 

temperature 

(avg. deg. f)

Percent 

H2O (Bws)

Mass - Filter 

(mg)

Mass - Rinse 

(mg)

Re-calculated Based 

on zero filter for 

negative values

Revised Catch 

based on 64 FR 

53028

IA Monsano Muscatine #8 Cond. 1 (10/2009) Solid/Biomass 1 5/29 240 168.2 10.2 1.65 n/a

IA Monsano Muscatine #8 Cond. 1 (10/2009) Solid/Biomass 2 5/29 240 176.7 10.1 3.45 n/a

IA Monsano Muscatine #8 Cond. 1 (10/2009) Solid/Biomass 3 5/29 240 169.5 10.4 2.15 n/a

IA U of Northern Iowa #3 (10/2009) Solid/Coal 1 29 240 157.2 7 0.5 3.7

IA U of Northern Iowa #3 (10/2009) Solid/Coal 2 29 240 158.0 7.6 0 3.3

IA U of Northern Iowa #3 (10/2009) Solid/Coal 3 29 240 162.2 7.3 0 2

IL PilyOne Boiler 1 (9/2009) Solid/Coal 1 5 240 160.2 250 7.8 0 20.4

IL PilyOne Boiler 1 (9/2009) Solid/Coal 2 5 240 179.0 247 7.7 0 27.1

IL PilyOne Boiler 1 (9/2009) Solid/Coal 3 5 240 172.9 255 7.4 0 61.2

IN Purdue University Boiler 5 (7/2009)

Solid/Coal 1 5 240 207.3 6.78

n/a n/a

IN Purdue University Boiler 5 (7/2009) Solid/Coal 2 5 240 204.5 6.91 n/a n/a

IN Purdue University Boiler 5 (7/2009) Solid/Coal 3 5 240 200.9 6.8 n/a n/a

ME Boralex Stratton Boiler 1 (10/2009) Solid/Biomass 1 5/202 55.6 20.2 240 18.7 n/a n/a 1

ME Boralex Stratton Boiler 1 (10/2009) Solid/Biomass 2 5/202 61.3 20.4 240 18.6 n/a n/a

ME Boralex Stratton Boiler 1 (10/2009) Solid/Biomass 3 5/202 63.5 20.3 235 18.2 n/a n/a

MI Consumer Energy Co - Campbell (9/2009) liquid 1

MI Consumer Energy Co - Campbell (9/2009) liquid 2

MI Consumer Energy Co - Campbell (9/2009) liquid 3

OH Smart Papers Holdings LLC (10/2005) Solid/Coal 1 5/29 120 84.8 265 7.3 0.1 2.3

OH Smart Papers Holdings LLC (10/2005) Solid/Coal 2 5/29 120 83.2 260 9.6 0.1 1.2

OH Smart Papers Holdings LLC (10/2005) Solid/Coal 3 5/29 120 86.0 261 10 2.35 1

SC GP Chem Russellville (8/2009) liquid/liquid 1 26A 120 104.2 250 10.3 1.1 1.3

SC GP Chem Russellville (8/2009) liquid/liquid 2 26A 120 102.2 250 10.8 1.1 0.7

SC GP Chem Russellville (8/2009) liquid/liquid 3 26A 120 81.8 248 10.6 0.4 1

SC Marlboro Paper (7/2009) Solid/Biomass 1 5/29 180 142.3 256 20.7 4.6 4.6

SC Marlboro Paper (7/2009) Solid/Biomass 2 5/29 180 136.0 252 19.8 6.1 3.9

SC Marlboro Paper (7/2009) Solid/Biomass 3 5/29 180 146.6 252 20.4 5.7 2.5

TN Eastman NO CBI DATA Solid/Coal 1 5/29 225 162.4 260 13.8 14.7 9.9

TN Eastman NO CBI DATA Solid/Coal 2 5/29 225 163.7 260 13.5 4.7 4.5

TN Eastman NO CBI DATA Solid/Coal 3 5/29 225 165.4 260 12.6 2.9 4.7

VADukeEnergyNarrows Boiler 2 Solid/Coal 1 5/26A 60 57.2 3.2 0.6 2.6

VADukeEnergyNarrows Boiler 2 Solid/Coal 2 5/26A 60 45.0 2.6 0.1 2.3

VADukeEnergyNarrows Boiler 2 Solid/Coal 3 5/26A 60 57.1 5 0.7 3.8

VADukeEnergyNarrows Boiler 3 Solid/Coal 1 5/26A 60 42.8 268 7.6 0.1 1.8

VADukeEnergyNarrows Boiler 3 Solid/Coal 2 5/26A 60 45.7 270 7.1 0.1 5.3

VADukeEnergyNarrows Boiler 3 Solid/Coal 3 5/26A 60 43.5 270 8.3 0.6 7.5

VA University of Virginia 7103-1-01R (12/2007) Solid/Coal 1 5/202 60 35.2 257 9.44 0.1 0.9

VA University of Virginia 7103-1-01R (12/2007) Solid/Coal 2 60 35.4 257 9.74 0.3 0.2 1

VA University of Virginia 7103-1-01R (12/2007) Solid/Coal 3 60 33.4 257 8.92 0.1 0.3 1

VA University of Virginia 7103-1-01R Solid/Coal 1 5/29 240 263

VA University of Virginia 7103-1-01R Solid/Coal 2 5/29 240 260

VA University of Virginia 7103-1-01R Solid/Coal 3 5/29 240 264

VA University of Virginia 7103-1-02R Solid/Coal 1 5/202 60 42.7 255 8.9 0.7 4.1

VA University of Virginia 7103-1-02R Solid/Coal 2 5/202 60 41.6 258 8.8 0.1 1.8

VA University of Virginia 7103-1-02R Solid/Coal 3 5/202 60 41.6 258 8.4 0.5 1.6

VA University of Virginia 7103-1-05

Solid/Coal 1 5/202 60 42.4 253 10

0.5 1.86

VA University of Virginia 7103-1-05 Solid/Coal 2 5/202 60 42.7 255 9.4 0.5 1.76

VA University of Virginia 7103-1-05 Solid/Coal 3 5/202 60 42.4 255 10.3 1.9 8.58

WA Grays Harbor Paper (6/2006)

Solid/Biomass 1 5/202 60 36.6 245 21.9

175 44.1

WA Grays Harbor Paper (6/2006) Solid/Biomass 2 5/202 60 38.1 250 21.09 179.6 37.5

WA Grays Harbor Paper (6/2006) Solid/Biomass 3 5/202 60 36.7 248 20.54 172 43.5
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit Category/ sub-category Run #

Method 

used (5, 

17, 26A, 

29,)

Sample time 

(min.)

Sample 

volume 

(dscf)

Filter 

temperature 

(avg. deg. f)

Percent 

H2O (Bws)

Mass - Filter 

(mg)

Mass - Rinse 

(mg)

Re-calculated Based 

on zero filter for 

negative values

Revised Catch 

based on 64 FR 

53028

AR Potlatch Forest Warren (8/2006) Solid/Biomass 1 5/26A 60 46.3 250 22 1.5 0.5

AR Potlatch Forest Warren (8/2006) Solid/Biomass 2 5/26A 60 45.4 253 20.97 1.2 0

AR Potlatch Forest Warren (8/2006) Solid/Biomass 3 5/26A 60 47.0 250 22.61 1.1 0

AR Potlatch Forest Warren (9/2009) Solid/Biomass 1 5/29 240 204.3 248 21.06 227 19.2

AR Potlatch Forest Warren (9/2009) Solid/Biomass 2 5/29 240 214.1 248 20.23 34.3 4.5

AR Potlatch Forest Warren (9/2009) Solid/Biomass 3 5/29 240 213.8 245 21.47 24.4 2.6

AR Weyerhaeuser Dierks Mill/ Unit 7 (12/2002) Solid/Biomass 1 5 60 45.2 245 20.65 4.8 1.2

AR Weyerhaeuser Dierks Mill/ Unit 7 (12/2002) Solid/Biomass 2 5 60 44.7 243 18.9 4.3 1.1

AR Weyerhaeuser Dierks Mill/ Unit 7 (12/2002) Solid/Biomass 3 5 60 43.8 240 18.93 4.8 0.1

AR Weyerhaeuser Dierks Mill/ Unit 7 (2/2009) Solid/Biomass 1 5/29 240 193.6 255 17.99 .

AR Weyerhaeuser Dierks Mill/ Unit 7 (2/2009) Solid/Biomass 2 5/29 240 178.9 252 18.99

AR Weyerhaeuser Dierks Mill/ Unit 7 (2/2009) Solid/Biomass 3 5/29 240 176.5 250 18.79

IA Archers Daniels Midland Des Moines Boiler 1 (6/2008) Solid/Coal 1 5 100 75.5 12.48 0.2 1.6625

IA Archers Daniels Midland Des Moines Boiler 1 (6/2008) Solid/Coal 2 5 100 78.6 11.42 0.1 1.3625

IA Archers Daniels Midland Des Moines Boiler 1 (6/2008) Solid/Coal 3 5 100 77.9 12.97 0.1 1.3

IA Archers Daniels Midland Des Moines Boiler 1 (8/2009) Solid/Coal 1 5/29 240 218.3 250 11.8 0.55 1.4

IA Archers Daniels Midland Des Moines Boiler 1 (8/2009) Solid/Coal 2 5/29 240 214.8 250 12.1 0.4 1.2

IA Archers Daniels Midland Des Moines Boiler 1 (8/2009) Solid/Coal 3 5/29 240 217.4 250 12 0.4 0.95

ID Potlatch (7/2009) Solid/Biomass 1 5/29 240 159.5 260 9.5 6 2.03

ID Potlatch (7/2009) Solid/Biomass 2 5/29 240 170.7 264 9.4 4.7 1.21

ID Potlatch (7/2009) Solid/Biomass 3 5/29 240 161.1 260 9.5 5 1.72

ME New Page-Rumford Cogen #6 and #7(12/2009) Solid/Biomass 1 5/29 240 189.2 250 11.71 2.9 3.1

ME New Page-Rumford Cogen #6 and #7(12/2009) Solid/Biomass 2 5/29 240 185.7 251 11.28 3.5 3

ME New Page-Rumford Cogen #6 and #7(12/2009) Solid/Biomass 3 5/29 240 187.8 250 11.7 4.6 3

MSWeyerhaeuserBruce Boiler 2 (8/2009) Solid/Biomass 1 5/29 180 171.1 255 24.6 24.4 12.8

MSWeyerhaeuserBruce Boiler 2 (8/2009) Solid/Biomass 2 5/29 180 176.4 250 25.5 22.5 23.8

MSWeyerhaeuserBruce Boiler 2 (8/2009) Solid/Biomass 3 5/29 180 174.7 252 25.1 11.7 11.6

ID Riley Creek Lumber Boiler 1/Solid Biomass 1 5 60 40.9 250 0.171 1.6 4.4

ID Riley Creek Lumber Boiler 1/Solid Biomass 2 5 60 40.6 256 0.161 1.1 2.7

ID Riley Creek Lumber Boiler 1/Solid Biomass 3 5 60 40.3 253.5 0.171 0.1 2.8

ID Riley Creek Lumber Boiler 2/Solid Biomass 1 5 60 not reported not reported not reported 78.6 38.4

ID Riley Creek Lumber Boiler 2/Solid Biomass 2 5 60 not reported not reported not reported 49 29.4

ID Riley Creek Lumber Boiler 2/Solid Biomass 3 5 60 not reported not reported not reported 23.5 12.7

ID Tasco Nampa, Riley Boiler Solid/Coal 1 5/26A 60 44.7 260 0.077 6.8 5.5

ID Tasco Nampa, Riley Boiler Solid/Coal 2 5/26A 60 45.9 260 0.0756 6.4 6.4/-0.4 ?

ID Tasco Nampa, Riley Boiler Solid/Coal 3 5/26A 60 46.3 258 0.0767 4.9 6.7

ID Tasco Nampa Solid/Coal 1 5 120 89.9 260 0.081 11.3 4.9

ID Tasco Nampa Solid/Coal 2 5 120 94.1 262 0.793 13.4 3.8

ID Tasco Nampa Solid/Coal 3 5 120 94.0 260 0.0396 9.5 3.8

IN Purdue Univ. Unit 5 Solid/Coal (Nov 2006) 1 5 64 45.6 258 0.1113 0.7 7.7

IN Purdue Univ. Unit 5 Solid/Coal (Nov 2006) 2 5 70 45.1 252 0.1108 1.1 1.5

IN Purdue Univ. Unit 5 Solid/Coal (Nov 2006) 3 5 75 45.0 255 0.1153 0.8 0.7

IN Purdue Univ. Unit 5 Solid/Coal (Nov 2008) 1 5 64 42.7 253 0.0572 5.7 9.9

IN Purdue Univ. Unit 5 Solid/Coal (Nov 2008) 2 5 63 44.7 253 0.076 1.8 10.7

IN Purdue Univ. Unit 5 Solid/Coal (Nov 2008) 3 5 63 44.8 253 0.082 1.3 11.1

IN Purdue Univ. Unit 5 Solid/Coal (July 2009) 1 5 287 210.6 0.0605

IN Purdue Univ. Unit 5 Solid/Coal (July 2009) 2 5 259 210.4 0.0645

IN Purdue Univ. Unit 5 Solid/Coal (July 2009) 3 5 250 201.6 0.0619

IN SABIC Plastics Solid/Coal Boiler House 1 (Apr 2005) 1 5/29 121 91.4 265 0.088 540.8 428.1

IN SABIC Plastics Solid/Coal Boiler House 1 (Apr 2005) 2 5/29 121 91.4 267 0.077 672.9 324.7

IN SABIC Plastics Solid/Coal Boiler House 1 (Apr 2005) 3 5/29 121 92.0 261 0.077 669.7 341.3

IN SABIC Plastics Solid/Coal Boiler House 2 (Apr 2005) 1 5/29 123 88.8 256 0.081 0 3.8

IN SABIC Plastics Solid/Coal Boiler House 2 (Apr 2005) 2 5/29 123 92.4 257 0.076 0 2.4

IN SABIC Plastics Solid/Coal Boiler House 2 (Apr 2005) 3 5/29 123 91.3 254 0.085 0 5.9
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit Category/ sub-category Run #

Method 

used (5, 

17, 26A, 

29,)

Sample time 

(min.)

Sample 

volume 

(dscf)

Filter 

temperature 

(avg. deg. f)

Percent 

H2O (Bws)

Mass - Filter 

(mg)

Mass - Rinse 

(mg)

Re-calculated Based 

on zero filter for 

negative values

Revised Catch 

based on 64 FR 

53028

IN SABIC Plastics Solid/Coal Boiler House 2 (Jun 2006) 1 5/29 125 91.7 259 0.063 0.1 4.2

IN SABIC Plastics Solid/Coal Boiler House 2 (Jun 2006) 2 5/29 125 89.7 260 0.068 0.1 2.2

IN SABIC Plastics Solid/Coal Boiler House 2 (Jun 2006) 3 5/29 125 86.6 258 0.072 6.8 0.7

LA Port Hudson

100% MCR Biomass/Dry scrubber on 

(Condition 1) 1 5 64 48.2 253 0.1276 4.1 4.9

LA Port Hudson 100% MCR Biomass/Dry scrubber on 2 5 62 47.5 253 0.1217 11.3 6.2

LA Port Hudson 100% MCR Biomass/Dry scrubber on 3 5 64 47.1 255 0.1239 54 23.4

LA Port Hudson

100% MCP Pet Coke/Dry scrubber on 

(Condition 4) 1 5 70 41.5 250 0.0816 0.5 3.1

LA Port Hudson 100% MCP Pet Coke/Dry scrubber on 2 5 70 41.7 248 0.081 0.3 2.1

LA Port Hudson 100% MCP Pet Coke/Dry scrubber on 3 5 70 42.0 246 0.0778 0.2 2.6

MI City of Escanaba Solid/Coal Boiler #1 4 5/26A 60 42.7 ? 0.071 34.8 12.3

MI City of Escanaba Solid/Coal Boiler #1 5 5/26A 60 43.3 ? 0.07 39.6 10.9

MI City of Escanaba Solid/Coal Boiler #1 6 5/26A 60 43.8 ? 0.067 36.7 12.8

MN Andersen Corp Bayport Boiler 11 Solid/Biomass (wood fuel) 4/2008 1 5 60 42.9 263 0.099 -2.5 5.7 5.7

MN Andersen Corp Bayport Boiler 11 Solid/Biomass (wood fuel) 4/2008 2 5 60 43.1 262 0.1056 -2.8 3.6 3.6

MN Andersen Corp Bayport Boiler 11 Solid/Biomass (wood fuel) 4/2008 3 5 60 42.4 263 0.0955 -1.2 3.3 3.3

MN Andersen Corp Bayport Boiler 12 Solid/Biomass (wood fuel) 4/2008 1 5 60 40.0 268 0.1065 -4.5 5.3 5.3

MN Andersen Corp Bayport Boiler 12 Solid/Biomass (wood fuel) 4/2008 2 5 60 39.6 263 0.1035 -3.3 4.3 4.3

MN Andersen Corp Bayport Boiler 12 Solid/Biomass (wood fuel) 4/2008 3 5 60 39.0 262 0.1087 -1.8 2.3 2.3

MN Boise Paper 1212 Boiler #2 6/2005 (TPM) 1 5/202 60 36.2 255 0.211 -1.4 25.9 25.9

MN Boise Paper 1212 Boiler #2 6/2005 (TPM) 2 5/202 60 35.1 255 0.224 -0.7 20.5 20.5

MN Boise Paper 1212 Boiler #2 6/2005 (TPM) 3 5/202 60 34.5 257 0.203 -2.1 28.9 28.9

WA Grays Harbor Paper Boiler #6 Solid/Biomass 1 5 240 181.4 256 0.1134 457.8 49.33

WA Grays Harbor Paper Boiler #6 Solid/Biomass 2 5 240 144.1 252 0.1301 369 41.01

WA Grays Harbor Paper Boiler #6 Solid/Biomass 3 5 240 188.8 252 0.1056 627 55.72

WA Weyerhaeuser Co. Solid/Biomass 1 5 60 43.4 259 0.1866 -2.7 2.4

WA Weyerhaeuser Co. Solid/Biomass 2 5 60 42.9 255 0.1769 1.6 2.36

WA Weyerhaeuser Co. Solid/Biomass 3 5 60 38.7 258 0.1836 0.6 3.08

WI Domtar 2814 Solid/Biomass 1 5/202 60 37.1 250 0.176 0.7 <1.06 1

WI Domtar 2814 Solid/Biomass 2 5/202 60 36.9 250 0.195 0.3 1.4

WI Domtar 2814 Solid/Biomass 3 5/202 60 34.6 250 0.161 0.5 3

WI GPGreenBay 2818 Boiler #10 Solid/Biomass (1999) 1 5/202 120 60.5 250 0.253 not found ?

WI GPGreenBay 2818 Boiler #10 Solid/Biomass (1999) 2 5/202 120 63.6 250 only impinger weights are recorded 0.252 ?

WI GPGreenBay 2818 Boiler #10 Solid/Biomass (1999) 3 5/202 120 64.5 250 0.248 ?

WI GPGreenBay 2818 Boiler #10 Solid/Biomass (2007) 1 5 60 50.2 263 0.0611 11.8 3.3

WI GPGreenBay 2818 Boiler #10 Solid/Biomass (2007) 2 5 60 56.1 263 0.0667 11 13.3

WI GPGreenBay 2818 Boiler #10 Solid/Biomass (2007) 3 5 60 57.7 264 0.0512 1.7 6.7

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1992) 1 5 120 100.8 336 0.0696 not found not found

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1992) 2 5 120 102.8 322 0.0673 not found not found

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1992) 3 5 120 106.1 328 0.0688 not found not found

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1999) 1

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1999) 2

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1999) 3

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2000) 1 5/202 60 35.2 249 0.028 1.4 1.9

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2000) 2 5/202 60 35.6 251 0.0311 1.2 3.1

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2000) 3 5/202 60 36.2 252 0.0299 2.2 2.3
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit Category/ sub-category Run #

Method 

used (5, 

17, 26A, 

29,)

Sample time 

(min.)

Sample 

volume 

(dscf)

Filter 

temperature 

(avg. deg. f)

Percent 

H2O (Bws)

Mass - Filter 

(mg)

Mass - Rinse 

(mg)

Re-calculated Based 

on zero filter for 

negative values

Revised Catch 

based on 64 FR 

53028

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2000) Stack 11 1 5/202 60 47.7 247 0.0381 0.9 3.1

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2000) Stack 11 2 5/202 60 32.8 251 0.0542 0 2.4

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2000) Stack 11 3 5/202 60 33.3 249 0.0427 0.2 6.2

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1998) Stack 11 1 5 60 49.4 307 0.0408 2.3 5.8

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1998) Stack 11 2 5 60 50.7 312 0.0408 1.4 0.7

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1998) Stack 11 3 5 60 49.8 313 0.0408 1.1 2.2

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2004) Stack 11 1 5/202 60 38.7 318 0.0465 15 12

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2004) Stack 11 2 5/202 60 37.5 317 0.0404 13.5 26.2

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2004) Stack 11 3 5/202 60 39.6 318 0.0407 15.4 30.9

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2002) Stack 11 1 5/202 60 50.4 323 0.0458 2 8.8

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2002) Stack 11 2 5/202 60 50.1 323 0.0469 4.1 1.9

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2002) Stack 11 3 5/202 60 50.4 323 0.0466 9.5 1.8

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2000) Stack 11 1 5/202 60 37.7 248 0.0488 1.7 6

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2000) Stack 11 2 5/202 60 38.0 250 0.0452 3.1 17.3

WI GPGreenBay 2818 Boiler #9 Solid/Coal (2000) Stack 11 3 5/202 60 38.1 250 0.0512 0 1.3

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1994) Stack 11 1 5 120 74.3 ?? 0.0531 2.7 6

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1994) Stack 11 2 5 120 72.8 ? 0.0498 1.5 7.9

WI GPGreenBay 2818 Boiler #9 Solid/Coal (1994) Stack 11 3 5 120 73.3 ? 0.0468 0 9.8

WIGreenBayPackagingMillDivision Boiler B26/Coal fired (2006) 1 5 120 85.1 258 0.063 2.8 0

WIGreenBayPackagingMillDivision Boiler B26/Coal fired (2006) 2 5 120 84.7 249 0.054 0 0.1 1

WIGreenBayPackagingMillDivision Boiler B26/Coal fired (2006) 3 5 120 84.7 250 0.073 1.1 1

WI New Page Biron Boiler 5 Solid/Coal (Sept, 12 2007) 1 5 60 59.2 249 0.058 7.1 0.9

WI New Page Biron Boiler 5 Solid/Coal (Sept, 12 2007) 2 5 60 39.3 254 0.069 3.4 0.1

WI New Page Biron Boiler 5 Solid/Coal (Sept, 12 2007) 3 5 60 36.7 251 0.084 2.9 1

SC Milliken Dewey Plant D30 Liquid/Liquid (2009) 1 29 180 164.1 250 0.12 8 3.3

SC Milliken Dewey Plant D30 Liquid/Liquid (2009) 2 29 180 146.0 249 0.123 1.8 1.6

SC Milliken Dewey Plant D30 Liquid/Liquid (2009) 3 29 180 150.9 250 0.122 1.6 0.9

TN Milan Army Ammunition Plant Boiler D88-L1 Liquid/Liquid (2009) 1 5 216 166.7 247 0.085 0.8 3.9

TN Milan Army Ammunition Plant Boiler D88-L1 Liquid/Liquid (2009) 2 5 216 167.3 244 0.1 0.7 2

TN Milan Army Ammunition Plant Boiler D88-L1 Liquid/Liquid (2009) 3 5 216 168.6 244 0.09 <0.30 2.2

VA GP Big Island 2703 Solid/Coal Boiler 4 (2007) 1 5/29 120 82.3 254 0.076 4.4 6.3

VA GP Big Island 2703 Solid/Coal Boiler 4 (2007) 2 5/29 120 71.6 253 0.089 3.2 4.7

VA GP Big Island 2703 Solid/Coal Boiler 4 (2007) 3 5/29 120 65.7 254 0.098 2.1 5

WA Weyerhaeuser Raymond Solid/Biomass (2009) 1 29 240 not reported not reported 0.1245 not reported not reported

WA Weyerhaeuser Raymond Solid/Biomass (2009) 2 29 240 not reported not reported 0.1438 not reported not reported

WA Weyerhaeuser Raymond Solid/Biomass (2009) 3 29 240 not reported not reported 0.1434 not reported not reported

WI GPGreenBay 2818 Boiler #10 Solid/Biomass (2009) 1 5/29 240 155.6 263 0.2894

WI GPGreenBay 2818 Boiler #10 Solid/Biomass (2009) 2 5/29 240 155.1 263 0.2683

WI GPGreenBay 2818 Boiler #10 Solid/Biomass (2009) 3 5/29 240 147.7 262 0.2965

WI New Page Biron Solid/Coal B24 (2009) 1 5 240 167.0 252 0.095 1.5 2.6

WI New Page Biron Solid/Coal B24 (2009) 2 5 240 149.0 254 0.12 3.1 4.3

WI New Page Biron Solid/Coal B24 (2009) 3 5 240 150.0 254 0.117 3.1 2.6

WI Wausau

Solid/Coal (boiler 5) 1 5 60 35.9 250 0.11

<0.3 <1.06 ?

WI Wausau

Solid/Coal (boiler 5) 2 5 60 35.8 251 0.075

1.5 1.3

WI Wausau Solid/Coal (boiler 5) 3 5 60 36.8 249 0.089 <0.3 1.6 ?

WV Mountain State Carbon Follansbee S1 Process Gas/ Process Gas 1 5 240 144.3 246 0.201 26 3.8

WV Mountain State Carbon Follansbee S1 Process Gas/ Process Gas 2 5 240 130.9 247 0.207 26.1 0.4

WV Mountain State Carbon Follansbee S1 Process Gas/ Process Gas 3 5 240 131.0 249 0.208 24.1 2.5
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit Category/ sub-category Run #

Method 

used (5, 

17, 26A, 

29,)

Sample time 

(min.)

Sample 

volume 

(dscf)

Filter 

temperature 

(avg. deg. f)

Percent 

H2O (Bws)

Mass - Filter 

(mg)

Mass - Rinse 

(mg)

Re-calculated Based 

on zero filter for 

negative values

Revised Catch 

based on 64 FR 

53028

TN Eastman NO CBI DATA Solid/Coal (11/9/2004) Condition 1 1 5 120 111.2 0.062

TN Eastman NO CBI DATA Solid/Coal (11/9/2004) Condition 1 2 5 120 107.8 0.064

TN Eastman NO CBI DATA Solid/Coal (11/9/2004) Condition 1 3 5 120 101.6 0.065

TN Eastman NO CBI DATA Solid/Coal (11/9/2004) Condition 2 1 5 120 107.2 0.06

TN Eastman NO CBI DATA Solid/Coal (11/9/2004) Condition 2 2 5 120 111.2 0.065

TN Eastman NO CBI DATA Solid/Coal (11/9/2004) Condition 2 3 5 120 103.0 0.067

TN Eastman NO CBI DATA Solid/Coal (6/2004) Voided 5

TN Eastman NO CBI DATA Solid/Coal (6/2004) 2 5 60 33.12 250 0.071 1.2 19.8

TN Eastman NO CBI DATA Solid/Coal (6/2004) 3 5 60 33.31 250 0.073 1.3 2.1

TN Eastman NO CBI DATA Solid/Coal (7/2008) 1 5 60 37.9 225 0.076 0.9 5.1

TN Eastman NO CBI DATA Solid/Coal (7/2008) 3 5 60 38.3 225 0.0761 3.4 4

TN Eastman NO CBI DATA Solid/Coal (7/2008) 4 5 60 39.3 226 0.0708 1 9.8

TN Eastman NO CBI DATA Solid/Coal (8/1996) 1 5 64 37.0 mislabeled Run 2 (p60)0.0744 10.1 10.3

TN Eastman NO CBI DATA Solid/Coal (8/1996) 2 5 64 37.9 255 0.0761 10.6 3.6

TN Eastman NO CBI DATA Solid/Coal (8/1996) 3 5 64 37.4 256 0.0807 47.5 15.5

TN Eastman NO CBI DATA Solid/Coal (8/2000) 2 5 64 38.9 248 0.0847 7.1 65

TN Eastman NO CBI DATA Solid/Coal (8/2000) 3 5 64 41.5 248 0.085 11.1 16.7

TN Eastman NO CBI DATA Solid/Coal (8/2000) 4 5 64 41.7 248 0.0813 8.9 7.2

TN Eastman NO CBI DATA Solid/Coal (3/2005) 1 5 120

TN Eastman NO CBI DATA Solid/Coal (3/2005) 2 5 120

TN Eastman NO CBI DATA Solid/Coal (3/2005) 3 5 120

TN Eastman NO CBI DATA Solid/Coal (5/2005) 1 5 60 38.9 255 0.0688 0 4

TN Eastman NO CBI DATA Solid/Coal (5/2005) 2 5 60 38.9 255 0.0718 0 7.5

TN Eastman NO CBI DATA Solid/Coal (5/2005) 3 5 60 38.3 260 0.0614 0 3.4

TN Eastman NO CBI DATA Solid/Coal (7/1993) 1 5 64 54.2 255 0.0731 3.3 18.7

TN Eastman NO CBI DATA Solid/Coal (7/1993) 2 5 64 54.1 255 0.0703 2.4 12.3

TN Eastman NO CBI DATA Solid/Coal (7/1993) 3 5 64 53.0 255 0.0725 0 15.2

TN Eastman NO CBI DATA Solid/Coal (8/2001) 1 5 60 39.9 254 0.084 5.1 10.7

TN Eastman NO CBI DATA Solid/Coal (8/2001) 2 5 60 40.9 251 0.0808 1.1 3.9

TN Eastman NO CBI DATA Solid/Coal (8/2001) 3 5 60 39.5 253 0.0845 0.5 5.5

TN Eastman NO CBI DATA Solid/Coal (9/1997) 1 5 64 41.5 251 0.0705 0 15.4

TN Eastman NO CBI DATA Solid/Coal (9/1997) 2 5 64 43.0 248 0.076 2.6 5

TN Eastman NO CBI DATA Solid/Coal (9/1997) 3 5 64 40.3 250 0.0726 0 4.9

TN Eastman NO CBI DATA Solid/Coal (11/8/1994) 1 5 75 50.3 251 0.0905 1.3 15.9

TN Eastman NO CBI DATA Solid/Coal (11/8/1994) 2 5 75 50.9 247 0.0943 3.2 11.2

TN Eastman NO CBI DATA Solid/Coal (11/8/1994) 4 5 75 47.6 250 0.1024 2.8 10.8

TN Eastman NO CBI DATA Solid/Coal (9/2002) 1 5 60 36.5 237 0.125 0.8 6.3

TN Eastman NO CBI DATA Solid/Coal (9/2002) 2 5 60 34.7 227 0.13 0.9 3.8

TN Eastman NO CBI DATA Solid/Coal (9/2002) 4 5 60 34.3 256 0.11 0.5 6.6

TN Eastman NO CBI DATA

Solid/Coal (9/2006) 1 5 60 35.9 250 0.1088

0.7 11.2

TN Eastman NO CBI DATA Solid/Coal (9/2006) 2 5 60 35.1 251 0.1076 0.7 14.8

TN Eastman NO CBI DATA Solid/Coal (9/2006) 3 5 60 35.1 254 0.1131 0.5 10.4

TN Eastman NO CBI DATA Solid/Coal (12/1994) 1 5 125 87.3 259 0.1192 17.1 10

TN Eastman NO CBI DATA Solid/Coal (12/1994) 2 5 125 83.5 244 0.1179 0.1 8.8

TN Eastman NO CBI DATA Solid/Coal (12/1994) 3 5 125 83.3 254 0.1142 0 19.3

TN Eastman NO CBI DATA Solid/Coal (12/2006) 1 5 125 94.8 255 0.1102 8.5 6.5

TN Eastman NO CBI DATA Solid/Coal (12/2006) 2 5 125 93.3 256 0.1108 0 8.9

TN Eastman NO CBI DATA Solid/Coal (12/2006) 3 5 125 94.2 257 0.1138 1.9 8.9

TN Eastman NO CBI DATA Solid/Coal (7/2006) 2 5 125 77.6 255 0.128 135.4 34.2

TN Eastman NO CBI DATA Solid/Coal (7/2006) 3 5 125 79.6 263 0.129 31.3 30.8

TN Eastman NO CBI DATA Solid/Coal (7/2006) 4 5 125 81.1 261 0.127 82.9 35.9
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit Category/ sub-category Run #

Method 

used (5, 

17, 26A, 

29,)

Sample time 

(min.)

Sample 

volume 

(dscf)

Filter 

temperature 

(avg. deg. f)

Percent 

H2O (Bws)

Mass - Filter 

(mg)

Mass - Rinse 

(mg)

Re-calculated Based 

on zero filter for 

negative values

Revised Catch 

based on 64 FR 

53028

TN Eastman NO CBI DATA Solid/Coal (8/2006) 1 5 125 73.9 260 0.1283 63.1 44.3

TN Eastman NO CBI DATA Solid/Coal (8/2006) 2 5 125 78.6 255 0.1312 74.5 51

TN Eastman NO CBI DATA Solid/Coal (8/2006) 3 5 125 77.9 252 0.1333 114.1 31.4

TN Eastman NO CBI DATA Solid/Coal (8/1994) 1 5 125 101.8 252 0.1005 0.7 8.6

TN Eastman NO CBI DATA Solid/Coal (8/1994) 2 5 125 97.7 247 0.1104 3.9 4.3

TN Eastman NO CBI DATA Solid/Coal (8/1994) 3 5 125 119.4 230 0.1168 2.3 14.8

TN Eastman NO CBI DATA Solid/Coal (9/1998) 1 5 125 62.7 250 0.1162 10.3 14.6

TN Eastman NO CBI DATA Solid/Coal (9/1998) 2 5 125 64.9 250 0.1192 0 13.6

TN Eastman NO CBI DATA Solid/Coal (9/1998) 3 5 125 66.3 251 0.1186 0 20.7

VA Duke Energy Narrows

Solid/Coal (Boiler 3) 1 5/26A 60 45.6 250 0.072

9.7 40.1

VA Duke Energy Narrows Solid/Coal (Boiler 3) 2 5/26A 60 47.0 250 0.075 10.1 20.4

VA Duke Energy Narrows Solid/Coal (Boiler 3) 3 5/26A 60 48.1 249 0.075

VA Duke Energy Narrows Solid/Coal (Boiler 3) 4 5/26A 60 47.3 251 0.067 11.1 23.3

VA Duke Energy Narrows Solid/Coal (Boiler 7) 1 5/26A 60 60.8 251 0.075 38.6 26

VA Duke Energy Narrows Solid/Coal (Boiler 7) 2 5/26A 60 47.3 250 0.077 31.9 37.1

VA Duke Energy Narrows Solid/Coal (Boiler 7) 3 5/26A 60 38.4 251 0.093 33.1 24.8

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (2/2004) 1 5 60 49.1 250 0.122 6.9 3.9

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (2/2004) 2 5 60 52.1 250 0.106 6.4 1.7

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (2/2004) 3 5 60 50.2 2500 0.103 7.7 2.1

VA Georgia Pacific Big Island Solid/Woodwaste Boiler 5 (2/2004) 1 5 60 43.7 257 0.139 7.3 10.4

VA Georgia Pacific Big Island Solid/Woodwaste Boiler 5 (2/2004) 2 5 60 45.3 251 0.14 9.7 14.4

VA Georgia Pacific Big Island Solid/Woodwaste Boiler 5 (2/2004) 3 5 60 48.2 250 0.123 12 13.2

VA Georgia Pacific Big Island Solid/Woodwaste Boiler 5 (3/2009) 1 5 60

VA Georgia Pacific Big Island Solid/Woodwaste Boiler 5 (3/2009) 2 5 60

VA Georgia Pacific Big Island Solid/Woodwaste Boiler 5 (3/2009) 3 5 60

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (3/2009) 1 5 60 55.9 252 0.39 107.7 49.7

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (3/2009) 2 5 60 54.2 252 0.047 94.2 40.6

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (3/2009) 3 5 60 59.7 252 0.04 129.6 46.1

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (4/2009) 1 5 60 22.8 257 0.093 10.6 3.4

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (4/2009) 2 5 60 22.8 253 0.081 2.9 5

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (4/2009) 3 5 60 21.7 254 0.097 2.6 3.8

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (5/2005) 1 5 60 39.6 not found 0.133 11.6 7.1

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (5/2005) 2 5 60 38.1 not found 0.098 9.5 5.2

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (5/2005) 3 5 60 37.7 not found 0.127 9.2 7.4

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (7/2006) 1 5 120 81.3 257 0.078 2.3 8.8

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (7/2006) 2 5 120 78.9 258 0.081 0 7.9

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (7/2006) 3 5 120 79.1 258 0.077 2.3 2.5

VA Georgia Pacific Big Island

Solid/Coal Boiler 4 (9/2008) 1 5 48 46.3 258 0.103

16.8 2.5

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (9/2008) 2 5 48 38.0 256 0.123 10 3.6

VA Georgia Pacific Big Island Solid/Coal Boiler 4 (9/2008) 3 5 48 38.3 256 0.095 10 4

Solid/Coal 4 5 48 42.6 253 0.093 10.2 1.4

Solid/Coal 5 5 48 34.4 255 0.073 45 13.7

Solid/Coal 6 5 48 34.6 264 0.071 37.1 18.5

Solid/Coal 1 5 48 37.8 254 0.067 32.3 12.6

Solid/Coal 2 5 48 37.1 253 0.059 28.2 13.2

Solid/Coal 1 5 48 33.5 255 0.061 39.6 15.5

Solid/Coal 2 5 48 32.6 255 0.066 33.5 11.1

WI Thilmany Paper Solid Coal 2/22/2006 1 5 60 51.4 223-273 0.061 2.9 3.6

WI Thilmany Paper Solid Coal 2/22/2006 2 5 60 52.2 223-273 0.063 2.3 0

WI Thilmany Paper Solid Coal 2/22/2006 3 5 60 51.2 223-273 0.057 2.2 1

WI Thilmany Paper Solid Coal 2/23/2006 1 5 60 51.2 223-273 0.06 3.7 1.7

WI Thilmany Paper Solid Coal 2/23/2006 2 5 60 51.8 223-273 0.064 4.2 2.7

WI Thilmany Paper Solid Coal 2/23/2006 3 5 60 52.6 223-273 0.065 3.3 0.7

WA Weyerhaeuser Raymond (11/2004) Solid/Biomass - Fuel Cell 1 5/202 60 60.3 265 15.52 0 1.3

WA Weyerhaeuser Raymond (11/2004) Solid/Biomass - Fuel Cell 2 5/202 60 60.4 262 15.93 0.1 1
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit Category/ sub-category Run #

Method 

used (5, 

17, 26A, 

29,)

Sample time 

(min.)

Sample 

volume 

(dscf)

Filter 

temperature 

(avg. deg. f)

Percent 

H2O (Bws)

Mass - Filter 

(mg)

Mass - Rinse 

(mg)

Re-calculated Based 

on zero filter for 

negative values

Revised Catch 

based on 64 FR 

53028

WA Weyerhaeuser Raymond (11/2004) Solid/Biomass - Fuel Cell 3 5/202 60 41.6 16.52 0 6 1

WA Weyerhaeuser Raymond (9/1996) Solid/Biomass - Fuel Cell 1 5 120 90.0 316 15.27 0 4.6

WA Weyerhaeuser Raymond (9/1996) Solid/Biomass - Fuel Cell 2 5 120 87.3 318 16.16 0 3.3

WA Weyerhaeuser Raymond (9/1996) Solid/Biomass - Fuel Cell 3 5 120 78.7 318 14.99 0 4.5

FL US Sugar Corp Boiler 8 (12/2009) Solid/Biomass - Suspension/ Grate 1 5 60 43.9 234 30 7 8.7

FL US Sugar Corp Boiler 8 (12/2009) Solid/Biomass - Suspension/ Grate 2 5 60 42.9 230 29 7.5 4.9

FL US Sugar Corp Boiler 8 (12/2009) Solid/Biomass - Suspension/ Grate 3 5 60 41.4 230 30.2 3.1 3.5

FL US Sugar Corp Boiler 8 (6/2006)

Solid/Biomass - Suspension/ Grate 1 5 60 29.1 255 26.73

0.5 3

FL US Sugar Corp Boiler 8 (6/2006) Solid/Biomass - Suspension/ Grate 2 5 60 25.7 253 24.13 0.4 1.5

FL US Sugar Corp Boiler 8 (6/2006) Solid/Biomass - Suspension/ Grate 3 5 60 32.0 255 21.61 0.5 1.1

FL US Sugar Corp Boiler 8 (6/2006) Solid/Biomass - Suspension/ Grate 4 5 60 29.4 255 21.65 0.6 1.2

FL US Sugar Corp Boiler 8 (6/2006) Solid/Biomass - Suspension/ Grate 5 5 60 26.1 253 20.04 0.6 0.9

FL US Sugar Corp Boiler 8 (8/2006)

Solid/Biomass - Suspension/ Grate 1 5 64 32.8 254 21.33

2.4 4.4

FL US Sugar Corp Boiler 8 (8/2006) Solid/Biomass - Suspension/ Grate 2 5 64 33.6 253 21.12 7.8 5

FL US Sugar Corp Boiler 8 (8/2006) Solid/Biomass - Suspension/ Grate 3 5 64 33.7 255 20.86 7.6 4.2

FL US Sugar Corp Boiler 8 (1/2007)

Solid/Biomass - Suspension/ Grate 1 5 60 52.2 258 24.23

4.7 11.3

FL US Sugar Corp Boiler 8 (1/2007) Solid/Biomass - Suspension/ Grate 2 5 60 53.7 258 23.85 6.6 6.9

FL US Sugar Corp Boiler 8 (1/2007) Solid/Biomass - Suspension/ Grate 3 5 60 53.3 258 24.35 9.9 7.8

FL US Sugar Corp Boiler 8 (1/2007)

Solid/Biomass - Suspension/ Grate 1 5 60 55.4 265 26.36

3.6 3.9

FL US Sugar Corp Boiler 8 (1/2007) Solid/Biomass - Suspension/ Grate 2 5 60 51.7 263 27.44 2.3 3

FL US Sugar Corp Boiler 8 (1/2007) Solid/Biomass - Suspension/ Grate 3 5 60 25.4 263 41.86 2.6 3.8

FL US Sugar Corp Boiler 8 (1/2007) Solid/Biomass - Suspension/ Grate 4 5 60 52.4 264 27.33 4.5 2.3

GA GP Madison Ply (10/2004) Solid/Biomass - Stoker/Other 1 5 60 40.4 250 15.11 -0.5 3.1 3.1

GA GP Madison Ply (10/2004) Solid/Biomass - Stoker/Other 2 5 60 39.9 250 15.96 -0.1 3.8 3.8

GA GP Madison Ply (10/2004) Solid/Biomass - Stoker/Other 3 5 60 40.8 253 15.82 -0.4 2.3 2.3

GA GP Madison Ply (6/2006) Solid/Biomass - Stoker/Other 1 5 60 51.7 260 12.26 1.3 4

GA GP Madison Ply (6/2006) Solid/Biomass - Stoker/Other 2 5 60 56.0 258 13.68 2 4.9

GA GP Madison Ply (6/2006) Solid/Biomass - Stoker/Other 3 5 60 57.0 260 13.83 1.9 3.2

GA GP Madison Ply (9/2007) Solid/Biomass - Stoker/Other 1 5 60 39.1 252 14.68 12.5 14.2

GA GP Madison Ply (9/2007) Solid/Biomass - Stoker/Other 2 5 60 35.9 252 10.65 5.9 2.6

GA GP Madison Ply (9/2007) Solid/Biomass - Stoker/Other 3 5 60 37.1 253 14.64 14.9 4.1

GA GP Madison Ply (6/2003) Solid/Biomass - Stoker/Other 1 5 120 84.0 250 15.2 2.5 6.1

GA GP Madison Ply (6/2003) Solid/Biomass - Stoker/Other 2 5 120 80.1 248 15.1 1.3 2.3

GA GP Madison Ply (6/2003) Solid/Biomass - Stoker/Other 3 5 120 72.9 240 15.64 1.1 2.3

GA GP Madison Ply (8/2009) Solid/Biomass - Stoker/Other 1 5/29 240 156.9 252 12.85 4.5 5.4

GA GP Madison Ply (8/2009) Solid/Biomass - Stoker/Other 2 5/29 240 154.1 252 14 0 0.1 1

GA GP Madison Ply (8/2009) Solid/Biomass - Stoker/Other 3 5/29 240 159.9 253 3.77 0.4 5.4

IL Abbott Abbott Park Solid/Coal - Stoker/Other 1 5 60 33.7 255 6.5 9 18.9

IL Abbott Abbott Park Solid/Coal - Stoker/Other 2 5 60 34.0 255 7.6 4.2 11.7

IL Abbott Abbott Park Solid/Coal - Stoker/Other 3 5 60 35.1 255 7.7 3 6.8

MN American Crystal Crookston Boiler 1 (10/2005) Solid/Coal - Stoker/Other 1 5 60 47.3 252 8.4 1.8 1.8

MN American Crystal Crookston Boiler 1 (10/2005) Solid/Coal - Stoker/Other 2 5 60 46.9 252 8.2 1.4 0.9

MN American Crystal Crookston Boiler 1 (10/2005) Solid/Coal - Stoker/Other 3 5 60 45.5 250 8.1 1.9 2.8

OH U of Cincinnati B108 (4/2006) Solid/Coal - Stoker/Other 1 5

OH U of Cincinnati B108 (4/2006) Solid/Coal - Stoker/Other 2 5

OH U of Cincinnati B108 (4/2006) Solid/Coal - Stoker/Other 3 5

SC International Paper Eastover Boiler 1(10/2004) Solid/Coal - PC 1 5 60 37.9 270 10.6 7.6 10

SC International Paper Eastover Boiler 1(10/2004) Solid/Coal - PC 2 5 60 37.7 268 11.5 3.2 3.1
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit Category/ sub-category Run #

Method 

used (5, 

17, 26A, 

29,)

Sample time 

(min.)

Sample 

volume 

(dscf)

Filter 

temperature 

(avg. deg. f)

Percent 

H2O (Bws)

Mass - Filter 

(mg)

Mass - Rinse 

(mg)

Re-calculated Based 

on zero filter for 

negative values

Revised Catch 

based on 64 FR 

53028

SC International Paper Eastover Boiler 1(10/2004) Solid/Coal - PC 3 5 60 39.4 270 11.3 1.4 2.5

SC International Paper Eastover Boiler 1(10/2000) Solid/Coal - PC 1 5 60 38.2 250 8.3 29.7 44.3

SC International Paper Eastover Boiler 1(10/2000) Solid/Coal - PC 2 5 60 38.2 248 12.3 15.1 12.6

SC International Paper Eastover Boiler 1(10/2000) Solid/Coal - PC 3 5 60 39.2 245 13.5 37.1 20.6

SC International Paper Eastover Boiler 1(10/2006) Solid/Coal - PC 1 5 60 39.8 252 10.4 2.2 3

SC International Paper Eastover Boiler 1(10/2006) Solid/Coal - PC 2 5 60 39.9 254 11.3 2.7 3.8

SC International Paper Eastover Boiler 1(10/2006) Solid/Coal - PC 3 5 60 38.9 252 10.2 1.2 0.5

SC International Paper Eastover Boiler 1(10/2002) Solid/Coal - PC 1 5 60 38.6 250 10.4 36.3 8.7

SC International Paper Eastover Boiler 1(10/2002) Solid/Coal - PC 2 5 60 38.2 252 11.6 43.1 12.4

SC International Paper Eastover Boiler 1(10/2002) Solid/Coal - PC 3 5 60 36.9 250 12.1 40.1 2.5

SC International Paper Eastover Boiler 2(10/2002) Solid/Biomass - Stoker/Other 1 5 125 78.4 255 14.8 6.5 5.9

SC International Paper Eastover Boiler 2(10/2002) Solid/Biomass - Stoker/Other 2 5 125 81.0 258 15.6 5.3 3.3

SC International Paper Eastover Boiler 2(10/2002) Solid/Biomass - Stoker/Other 3 5 125 79.9 256 16.4 7 2.7

SC International Paper Eastover Boiler 2(3/2008) Solid/Biomass - Stoker/Other 1 5 125 79.4 244 16 13.2 10.1

SC International Paper Eastover Boiler 2(3/2008) Solid/Biomass - Stoker/Other 2 5 125 82.2 248 16 7 17.3

SC International Paper Eastover Boiler 2(3/2008) Solid/Biomass - Stoker/Other 3 5 125 80.9 246 16 4.6 3.1

SC International Paper Eastover Boiler 2(3/2004) Solid/Biomass - Stoker/Other 1 5 125 82.1 315 20 16 2.6

SC International Paper Eastover Boiler 2(3/2004) Solid/Biomass - Stoker/Other 2 5 125 77.3 315 18 12.1 4.2

SC International Paper Eastover Boiler 2(3/2004) Solid/Biomass - Stoker/Other 3 5 125 75.0 315 20 20.5 5.4

SC International Paper Eastover Boiler 2(6/1999) Solid/Biomass - Stoker/Other 1 5 125 67.9 326 21 1.5 1.8

SC International Paper Eastover Boiler 2(6/1999) Solid/Biomass - Stoker/Other 2 5 125 65.4 325 20 3.9 4.8

SC International Paper Eastover Boiler 2(6/1999) Solid/Biomass - Stoker/Other 3 5 125 66.8 328 20 0.4 5.7

SC International Paper Eastover Boiler 2(6/2003) Solid/Biomass - Stoker/Other 1 5 125 76.2 310 17.1 15.3 10.2

SC International Paper Eastover Boiler 2(6/2003) Solid/Biomass - Stoker/Other 2 5 125 76.9 320 16.4 5.4 9.3

SC International Paper Eastover Boiler 2(6/2003) Solid/Biomass - Stoker/Other 3 5 125 79.2 300 17.9 1 10.6

SC International Paper Eastover Boiler 2(8/1997) Solid/Biomass - Stoker/Other 1 5 125 72.1 22.04 6.7 34.1

SC International Paper Eastover Boiler 2(8/1997) Solid/Biomass - Stoker/Other 2 5 125 23.81 4.8 19.2

SC International Paper Eastover Boiler 2(8/1997) Solid/Biomass - Stoker/Other 3 5 125 24.1 20.3 41

SC International Paper Eastover Boiler 2(8/1995) Solid/Biomass - Stoker/Other 1 5 120 66.2 250 20.6 3.75 7.7

SC International Paper Eastover Boiler 2(8/1995) Solid/Biomass - Stoker/Other 2 5 120 65.1 251 21.4 1.85 7

SC International Paper Eastover Boiler 2(8/1995) Solid/Biomass - Stoker/Other 3 5 120 66.7 255 22 3.6 3.65

SC International Paper Eastover Boiler 2(8/1993)

Solid/Biomass - Stoker/Other 1 5 90 46.9 262 20.4

3.9 104.1

SC International Paper Eastover Boiler 2(8/1993) Solid/Biomass - Stoker/Other 2 5 90 52.6 268 21.1 6.6 50.8

SC International Paper Eastover Boiler 2(8/1993) Solid/Biomass - Stoker/Other 3 5 90 47.0 266 20.3 1.95 40.95

TN Cargill Memphis Boiler 8001(8/2009) Solid/Coal - Stoker/Other 1 5/29 240 169.4 6.7 0.5 2.2

TN Cargill Memphis Boiler 8001(8/2009) Solid/Coal - Stoker/Other 2 5/29 240 172.5 7.2 0.5 2.5

TN Cargill Memphis Boiler 8001(8/2009) Solid/Coal - Stoker/Other 3 5/29 240 158.7 7.4 0.5 1.9

TN Cargill Memphis Boiler 8001(7/2007) Solid/Coal - Stoker/Other 1 5 60 53.1 255 5.5 9.8 11.1

TN Cargill Memphis Boiler 8001(7/2007) Solid/Coal - Stoker/Other 2 5 60 52.4 251 5.5 8.3 9.6

TN Cargill Memphis Boiler 8001(7/2007) Solid/Coal - Stoker/Other 3 5 60 52.5 253 5.7 6.7 7.1
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

AK Doyon Utilities/ Unit 4

AK Doyon Utilities/ Unit 4

AK Doyon Utilities/ Unit 4

AK Doyon Utilities/ Unit 7

AK Doyon Utilities/ Unit 7

AK Doyon Utilities/ Unit 7

AR Weyerhaeuser Dierks Mill / Unit 5 (1997) 

AR Weyerhaeuser Dierks Mill / Unit 5 (1997) 

AR Weyerhaeuser Dierks Mill / Unit 5 (1997) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (1997) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (1997) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (1997) 

FL Smurfit-Stone

FL Smurfit-Stone

FL Smurfit-Stone

GA GP Monticello Plywood (2/21/08)

GA GP Monticello Plywood (2/21/08)

GA GP Monticello Plywood (2/21/08)

GA GP Monticello Plywood (2/7/07)

GA GP Monticello Plywood (2/7/07)

GA GP Monticello Plywood (2/7/07)

IA ADM Corn Processing Cedar Rapids

IA ADM Corn Processing Cedar Rapids

IA ADM Corn Processing Cedar Rapids

IA Iowa State University B1

IA Iowa State University B1

IA Iowa State University B1

IA Iowa State University B2

IA Iowa State University B2

IA Iowa State University B2

IA Monsanto Muscatine #8 Cond. 1 (5/2007)

IA Monsanto Muscatine #8 Cond. 1 (5/2007)

IA Monsanto Muscatine #8 Cond. 1 (5/2007)

IA Monsanto Muscatine #8 Cond. 3 (5/2007)

IA Monsanto Muscatine #8 Cond. 3 (5/2007)

IA Monsanto Muscatine #8 Cond. 3 (5/2007)

IA Monsano Muscatine #8 Cond. 1 (8/2007)

IA Monsano Muscatine #8 Cond. 1 (8/2007)

IA Monsano Muscatine #8 Cond. 1 (8/2007)

ID Amalgamated Suger Co. Twin Falls

ID Amalgamated Suger Co. Twin Falls

ID Amalgamated Suger Co. Twin Falls

Mass Total (mg) Diluent correction (7% 

O2? 12% CO2?)

Reagent 

blank value 

(mg/ml)

Total 

reagent 

used (ml)

Blank 

correction 

value

Reported 

Gr/dscf

Reported 

Mass/Unit 

(lbs/mmbtu)

Meter cal 

y/n

Leak check 

y/n

Iso Check 

y/n

Nozzle 

check y/n

3.6

7 % O2, 12.8% CO2 100 0.3 0.0020 y y 96.6 y

4.5 6.67 %O2, 13.13%CO2 100 0.3 0.0023 y y 97.5 y

5.1 6.6% O2, 13.2%CO2 100 0.3 0.0027 y y 96.6 y

5.8 7.6% o2, 12.2% CO2 100 0.3 0.0033 y y 95.4 y

7.2 7.93% O2, 12.0% CO2 100 0.3 0.0042 y y 95.5 y

6.5 8.0% O2, 12.0% CO2 100 0.3 0.0040 y y 95.4 y

24.6 9% O2, 10% CO2 100 0.7 7.200E-03 y y 69.89

19.9 9% O2, 10% CO2 100 0.7 5.400E-03 y y 99.73

10.4 9% O2, 10% CO2 100 0.7 3.200E-03 y y 100.11

60.5 6.7% O2, 13.9%CO2 100 0.7 1.200E-02 0.0243 y y 100.68

25 6.4%O2, 14.0% CO2 100 0.7 6.500E-03 0.0128 y y 102.23

25.4 6.4% O2, 13.9% CO2 100 0.7 4.900E-03 0.0097 y y 100.47

4 7.05% O2, 12.5% CO2 100 0.8 1.360E-03 0.0029 y 93.43 y

2.1 7.29% O2, 12.17% CO2 100 0.8 7.010E-04 0.0015 y 95.25 y

7.1 7.41% O2, 12.10% CO2 100 0.8 2.470E-03 0.0054 y 93.01 y

3.8 10.71% O2, 9.42% CO2 131 1 6.000E-04 0.0017 y 96.3 y

2.9 10.73% O2, 9.83% CO2 122 1 4.000E-04 0.0012 y 95.92 y

1.6 11.35% O2, 8.88% CO2 118 0.9 3.000E-04 0.0008 y 96.91 y

15 5.89% O2, 14.0% CO2 198 1.5 2.500E-03 0.0050 101.63 y

21.7 6.80% O2, 13.54% CO2 140 1.1 3.800E-03 0.0070 101.13 y

15.9 6.44% O2, 14.04% CO2 162 1.2 2.600E-03 0.0050 99.71 y

4.3 4.5% O2, 15.0% CO2 130 0 1.000E-03 0.0017 y y 1.04 y

8.6 4.5% O2, 15.0% CO2 170 0 2.100E-03 0.0038 y y 1.01 y

2.2 4.5% O2, 15.0% CO2 130 0 5.000E-04 0.0009 y y 1.02 y

0.7 4.3, 14.6 50 0 0.000E+00 0.0010 y y 95.6

0.9 3.9, 15.0 65 0 0.000E+00 0.0010 y y 98.8

1.6 4.4, 14.5 50 0 1.000E-03 0.0010 y y 97.2

0.6

4.0, 14.9 50 0 0.000E+00 0.0000 y y 98.2

0.7 3.9, 15.0 65 0 0.000E+00 0.0010 y y 101.2

0.4

3.7, 15.1 50 0 0.000E+00 0.0000 y y 97

8.55 8.3, 11.8 400 0 3.300E-03 0.0077 y y 98.1

7.55 7.9, 11.6 400 0 2.900E-03 0.0065 y y 99

11 8.3, 11.4 425 0 4.300E-03 0.0102 y y 97.3

7.6

8.3, 11.4 450 0 2.900E-03 0.0067 y y 95.9

6.25 8.1, 11.1 500 0 2.400E-03 0.0055 y y 96.1

11.4 8.3, 11.5 500 0 4.300E-03 0.0099 y y 101.7

8.55 9.3, 11.5 450 0 3.200E-03 0.0080 99.3

10.7 9.0, 11.3 450 0 4.100E-03 0.0101 99.9

7.1 9.0, 11.0 500 0 2.700E-03 0.0067 99.4

5.6 6.9, 9.6 50 0 1.100E-03 y y 103

8.9 6.9, 9.5 55 0 1.800E-03 y y 102

11.1 6.0, 13.5 70 0 2.200E-03 y y 103
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

IA Monsano Muscatine #8 Cond. 1 (10/2009)

IA Monsano Muscatine #8 Cond. 1 (10/2009)

IA Monsano Muscatine #8 Cond. 1 (10/2009)

IA U of Northern Iowa #3 (10/2009)

IA U of Northern Iowa #3 (10/2009)

IA U of Northern Iowa #3 (10/2009)

IL PilyOne Boiler 1 (9/2009)

IL PilyOne Boiler 1 (9/2009)

IL PilyOne Boiler 1 (9/2009)

IN Purdue University Boiler 5 (7/2009)

IN Purdue University Boiler 5 (7/2009)

IN Purdue University Boiler 5 (7/2009)

ME Boralex Stratton Boiler 1 (10/2009)

ME Boralex Stratton Boiler 1 (10/2009)

ME Boralex Stratton Boiler 1 (10/2009)

MI Consumer Energy Co - Campbell (9/2009)

MI Consumer Energy Co - Campbell (9/2009)

MI Consumer Energy Co - Campbell (9/2009)

OH Smart Papers Holdings LLC (10/2005)

OH Smart Papers Holdings LLC (10/2005)

OH Smart Papers Holdings LLC (10/2005)

SC GP Chem Russellville (8/2009)

SC GP Chem Russellville (8/2009)

SC GP Chem Russellville (8/2009)

SC Marlboro Paper (7/2009)

SC Marlboro Paper (7/2009)

SC Marlboro Paper (7/2009)

TN Eastman NO CBI DATA 

TN Eastman NO CBI DATA 

TN Eastman NO CBI DATA 

VADukeEnergyNarrows Boiler 2

VADukeEnergyNarrows Boiler 2

VADukeEnergyNarrows Boiler 2

VADukeEnergyNarrows Boiler 3

VADukeEnergyNarrows Boiler 3

VADukeEnergyNarrows Boiler 3

VA University of Virginia 7103-1-01R (12/2007)

VA University of Virginia 7103-1-01R (12/2007)

VA University of Virginia 7103-1-01R (12/2007)

VA University of Virginia 7103-1-01R

VA University of Virginia 7103-1-01R

VA University of Virginia 7103-1-01R

VA University of Virginia 7103-1-02R

VA University of Virginia 7103-1-02R

VA University of Virginia 7103-1-02R

VA University of Virginia 7103-1-05

VA University of Virginia 7103-1-05

VA University of Virginia 7103-1-05

WA Grays Harbor Paper (6/2006)

WA Grays Harbor Paper (6/2006)

WA Grays Harbor Paper (6/2006)

Mass Total (mg) Diluent correction (7% 

O2? 12% CO2?)

Reagent 

blank value 

(mg/ml)

Total 

reagent 

used (ml)

Blank 

correction 

value

Reported 

Gr/dscf

Reported 

Mass/Unit 

(lbs/mmbtu)

Meter cal 

y/n

Leak check 

y/n

Iso Check 

y/n

Nozzle 

check y/n

1.65 7.00, 11.90 1.510E-04 0.0003 y y 99.9

3.45 6.80, 12.00 3.010E-04 0.0007 y y 101

2.15 6.90, 11.80 1.960E-04 0.0004 y y 100.3

4.2 5.80, 13.40 78 0 4.000E-04 0.0008 y y 97.3 y

3.3 5.30, 13.80 108 0 3.000E-04 0.0006 y y 97.8 y

2 6.00, 12.30 95 0 2.000E-04 0.0004 y y 98.9 y

20.4 8.4, 11.2 0.0046 y 101.9 y

27.1 8.1, 11.5 0.0053 y 102.6 y

61.2 8.3, 11.4 0.0126 y 101.2 y

21.3

4.4, 15 1.590E-03 0.0030 y y 102.2 y

21.1 4.4, 15 1.590E-03 0.0030 y y 102 y

20.2 4.3, 15 1.550E-03 0.0030 y y 102.2 y

0.65 6.3, 14.6 0.000E+00 0.0010 y y 107.9 y

2.9 5.9, 14.8 0.000E+00 0.0030 y y 97 y

3.8 5.9, 15.0 0.000E+00 0.0040 y y 92 y

2.4 7.9, 11.7 4.370E-04 0.0011 y 94.6 y

1.3 7.8, 11.9 2.410E-04 0.0005 y 96.1 y

3.4 7.8, 11.9 6.010E-04 0.0014 y 96.9 y

2.4 8.06, 9.86 85.3 -0.1 4.000E-04 0.0008 y y 99.9 y

1.8 7.26, 10.43 84.6 -0.1 3.000E-04 0.0005 y y 100.6 y

1.4 7.31, 10.31 84 -0.1 3.000E-04 0.0005 y y 100.4 y

9.3 9.74, 11.42 84.36 0.1 1.000E-03 0.0025 y 98.2 y

10 9.38, 11.73 88.61 0.1 1.100E-03 0.0027 y 97.3 y

8.2 9.11, 11.97 86.22 0.1 9.000E-03 0.0020 y 97.4 y

24.6 6.3, 13.2 64 0.0047 y y 99.4 y

9.2 6.3, 13.4 71 0.0017 y y 100.2 y

7.6 6.3, 13.3 83 0.0014 y y 100.1 y

3.2 14.10, 5.60 138 0.1 9.000E-04 0.0040 y y 95 y

2.4 12.53, 6.77 135.99 0.1 8.000E-04 0.0030 y y 96.9 y

4.5 13.03, 6.63 136.38 0.1 1.200E-03 0.0040 y y 96.3 y

1.9 7.73, 11.47 139.13 0.1 7.000E-04 0.0020 y y 102.3 y

5.4 7.07, 12.17 140.11 0.1 1.800E-03 0.0040 y y 106.1 y

8.1 9.63, 9.80 130.98 0.1 2.900E-03 0.0070 y y 102 y

1 7.07, 12.21 140 0 4.000E-04 0.0009 y y 101 y

0.5 7.03, 12.34 140 0 2.000E-04 0.0005 y y 103.1 y

0.4 6.98, 12.54 140 0 2.000E-04 0.0004 y y 96.5 y

4.8 6.64, 12.62 100 0 2.000E-03 0.0040 y y 102 y

1.9 6.96, 12.36 100 0 1.000E-03 0.0010 y y 102.1 y

3.1 6.74, 12.57 110 0 1.000E-03 0.0020 y y 101.9 y

2.36

6.8, 12.8 120 0.94 9.000E-04 0.0018 y y 102 y

1.26 7.5, 11.9 120 0.94 8.000E-04 0.0018 y y 102.3 y

10.48 8.5, 11.0 130 1.02 3.800E-03 0.0090 y y 103.2 y

219.1

6.3, 14.5 0.5 120 0.1 9.200E-02 0.1950 y

217.1 6.9, 13.9 0.5 95 0 9.000E-02 0.1940 y

215.5 7.4, 13.3 0.5 110 0.1 9.400E-02 0.1960 y
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

AR Potlatch Forest Warren (8/2006)

AR Potlatch Forest Warren (8/2006)

AR Potlatch Forest Warren (8/2006)

AR Potlatch Forest Warren (9/2009)

AR Potlatch Forest Warren (9/2009)

AR Potlatch Forest Warren (9/2009)

AR Weyerhaeuser Dierks Mill/ Unit 7 (12/2002) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (12/2002) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (12/2002) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (2/2009) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (2/2009) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (2/2009) 

IA Archers Daniels Midland Des Moines Boiler 1 (6/2008)

IA Archers Daniels Midland Des Moines Boiler 1 (6/2008)

IA Archers Daniels Midland Des Moines Boiler 1 (6/2008)

IA Archers Daniels Midland Des Moines Boiler 1 (8/2009)

IA Archers Daniels Midland Des Moines Boiler 1 (8/2009)

IA Archers Daniels Midland Des Moines Boiler 1 (8/2009)

ID Potlatch (7/2009)

ID Potlatch (7/2009)

ID Potlatch (7/2009)

ME New Page-Rumford Cogen #6 and #7(12/2009)

ME New Page-Rumford Cogen #6 and #7(12/2009)

ME New Page-Rumford Cogen #6 and #7(12/2009)

MSWeyerhaeuserBruce Boiler 2 (8/2009)

MSWeyerhaeuserBruce Boiler 2 (8/2009)

MSWeyerhaeuserBruce Boiler 2 (8/2009)

ID Riley Creek Lumber

ID Riley Creek Lumber

ID Riley Creek Lumber

ID Riley Creek Lumber

ID Riley Creek Lumber

ID Riley Creek Lumber

ID Tasco Nampa, Riley Boiler

ID Tasco Nampa, Riley Boiler

ID Tasco Nampa, Riley Boiler

ID Tasco Nampa

ID Tasco Nampa

ID Tasco Nampa

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN SABIC Plastics

IN SABIC Plastics

IN SABIC Plastics

IN SABIC Plastics

IN SABIC Plastics

IN SABIC Plastics

Mass Total (mg) Diluent correction (7% 

O2? 12% CO2?)

Reagent 

blank value 

(mg/ml)

Total 

reagent 

used (ml)

Blank 

correction 

value

Reported 

Gr/dscf

Reported 

Mass/Unit 

(lbs/mmbtu)

Meter cal 

y/n

Leak check 

y/n

Iso Check 

y/n

Nozzle 

check y/n

2 16.00, 22.00 121 0 7.000E-04 0.0011 y y 100.06 y

1.2 15.50, 20.97 148 0 4.000E-04 0.0007 y y 98.24 y

1.1 16.00, 22.61 103 0 4.000E-04 0.0006 y y 103.78 y

246 4.22, 15.81 0 0.0355 y y 91.37 y

38.8 4.90, 15.12 0 0.0048 y y 96.17 y

27 4.39, 15.60 0 0.0033 y y 93.67 y

5.9 8.07, 12.45 0.001 118 0.1 6.000E-04 y 100.85

4.2 7.84, 12.50 0.001 158 0.2 7.000E-04 y 99.86

4.7 7.84, 12.41 0.001 166 0.2 6.000E-04 y 99.29

17 9.18, 11.79 0.0032 y y 97.62 y

19 9.23, 11.58 0.0039 y y 98.69 y

20 9.33, 11.53 0.0042 y y 98.94 y

1.8625 6.90, 13.00 0.0015 225 0.3375 4.000E-04 0.0007 y 101.7 y

1.4625 7.90, 12.00 0.0015 225 0.3375 3.000E-04 0.0006 y 100.5 y

1.4 7.90, 12.00 0.0015 200 0.3 3.000E-04 0.0005 y 104.1 y

1.95 5.58, 14.24 0 100 0 <.0001 <.00025 y y 100.2 y

1.6 5.56, 14.11 0 100 0 <.0001 <.00021 y y 96.7 y

1.35 5.66, 14.29 0 100 0 <.0001 <.00017 y y 103.6 y

8.03 13.2, 7.1 0.0031 86 0.27 8.000E-04 0.0028 y y 97 y

5.91 13.8, 6.7 0.0031 92 0.29 5.000E-04 0.0021 y y 100 y

6.72 13.0, 7.5 0.0031 91 0.28 6.000E-04 0.0023 y y 98 y

6 7.5, 12.2 0 36 0 5.000E-04 0.0010 y y 102.3 y

6.5 7.6, 12.2 0 68 0 5.000E-04 0.0010 y y 99.6 y

7.6 7.7, 12.0 0 95 0 6.000E-04 0.0020 y y 101.5 y

37.2 8.06, 12.51 0.0008 85.5 -0.1 3.300E-03 0.0074 y y 99.6 y

46.3 7.25, 13.24 0.0008 86.7 -0.1 4.000E-03 0.0084 y y 102.4 y

23.3 7.63, 12.80 0.0008 84.9 -0.1 2.100E-03 0.0044 y y 100.7 y

6 8% O2 0.001 150 0.2 2.700E-03 0.2200 Y N Y N

3.8 8% O2 0.001 150 0.2 1.600E-03 0.1400 Y N Y N

2.9 8% O2 0.001 150 0.2 1.300E-03 0.1100 Y N Y N

117 8% O2 0.001 150 0.2 5.370E-02 5.3900 Y N Y N

78.4 8% O2 0.001 150 0.2 3.940E-02 4.0000 Y N Y N

36.2 8% O2 0.001 150 0.2 1.800E-02 1.8200 Y N Y N

12.3 8% O2 0 75 0 3.800E-03 2.1200 Y N Y N

6.4 8% O2 0 100/75 0 1.900E-03 1.0900 Y Y

11.6 8% O2 0 95 0 3.200E-03 1.9900 Y Y

16.2 8% O2 0 100 0 2.400E-03 1.4000 Y Y

17.2 8% O2 0 100 0 2.400E-03 1.4300 Y Y

13.3 8% O2 0 100 0 1.800E-03 1.1600 Y Y

8.2 not reported 0.001 150 0.2 2.780E-03 1.4200 Y N y Y

2.5 not reported 0.001 130 0.1 8.570E-04 0.4300 Y N y Y

1.4 not reported 0.001 55 0.1 4.810E-04 0.2400 Y N y Y

15.3 not reported 0.002 128.3 0.3 5.530E-03 2.7800 Y y

12.3 not reported 0.002 113.5 0.2 4.250E-03 2.2100 y

12.1 not reported 0.002 115.8 0.2 4.170E-03 2.1400 y

1.590E-03 0.8900 y

1.590E-03 0.8800 y

1.550E-03 0.8400 y

968.9 0.07 170 0 1.637E-01 130.4150 y y

997.6 0.07 155 0 1.684E-01 134.9410 y y

1011 0.07 165 0 1.697E-01 137.0540 y y

3.8 0.07 100 0 7.000E-04 0.7010 y y

2.4 0.07 84 0 4.000E-04 0.4450 y y

5.9 0.07 69 0 1.000E-03 1.0930 y y
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

IN SABIC Plastics

IN SABIC Plastics

IN SABIC Plastics

LA Port Hudson

LA Port Hudson

LA Port Hudson

LA Port Hudson

LA Port Hudson

LA Port Hudson

MI City of Escanaba

MI City of Escanaba

MI City of Escanaba

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Boise Paper 1212

MN Boise Paper 1212

MN Boise Paper 1212

WA Grays Harbor Paper 

WA Grays Harbor Paper 

WA Grays Harbor Paper 

WA Weyerhaeuser Co.

WA Weyerhaeuser Co.

WA Weyerhaeuser Co.

WI Domtar 2814

WI Domtar 2814

WI Domtar 2814

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

Mass Total (mg) Diluent correction (7% 

O2? 12% CO2?)

Reagent 

blank value 

(mg/ml)

Total 

reagent 

used (ml)

Blank 

correction 

value

Reported 

Gr/dscf

Reported 

Mass/Unit 

(lbs/mmbtu)

Meter cal 

y/n

Leak check 

y/n

Iso Check 

y/n

Nozzle 

check y/n

4.1 ? 0.003333333 60 0.2 7.000E-04 0.8310 y y y

2.2 ? 0.002702703 37 0.1 4.000E-04 0.4440 y y y

7.2 ? 0.003921569 51 0.2 1.300E-03 1.4700 y y y

9

0.07 0 414 0 2.500E-03 6.8000 y y y

17.5 0.07 0 392 0 4.900E-03 14.1000 y y y

77.4 0.07 0 396 0 1.970E-02 57.2000 y y y

3.6 0.07 0 323 0 1.200E-03 3.1960 y y y

2.4 0.07 0 311 0 1.200E-03 3.2170 y y y

2.8 0.07 0 314 0 1.200E-03 3.2540 y y y

47.1 ? 0 ? 0 1.700E-02 7.3800 y y y

50.5 ? 0 ? 0 1.800E-02 7.8700 y y y

49.5 ? 0 ? 0 1.740E-02 7.7700 y y y

5.7 0 65 0 1.150E-03 0.1360 y y y

3.6 0 70 0 2.900E-04 0.0330 y y y

3.3 0 60 0 7.600E-04 0.0890 y y y

5.3 0 60 0 3.100E-04 0.0330 y y y

4.3 0 60 0 3.900E-04 0.0420 y y y

2.3 0 50 0 2.000E-04 0.0210 y y y

24.5 0.0002380950.1+0.1 (organic + inorganic condensibles) 840 0.0098 (0.0003) 6.6 (0.2) y y y

19.8 0.0002352940.1+0.1 (organic + inorganic condensibles) 850 0.0112 (0.0009) 6.4 (0.6) y y y

26.8 0.0002366860.1+0.1 (organic + inorganic condensibles) 845 0.012 (0.0015) 7.5 (1.0) y y y

507 0.07 0.00135 123 0.17 ALT-009 was used - Meter box 8 didn't pass. Meter box 3 was used here. 9.520E-02 20.8000 y

409.84 0.07 0.00135 103 0.17 ALT-009 was used - Meter box 8 didn't pass. Meter box 3 was used here. 8.240E-02 16.7000 y

682.55 0.07 0.00135 200 0.17 ALT-009 was used - Meter box 8 didn't pass. Meter box 3 was used here. 1.292E-01 27.8000 y

2.4 0.07 0 85 0 9.000E-04 1.5400 y y

0.4 0.07 0 94 0 1.500E-03 2.4800 y y

3.7 0.07 0 95 0 1.500E-03 2.3300 y y

0.7 7% 12% 0 125 0 8.300E-03 2.8000 y y

1.7 7% 12% 0 150 0 7.800E-03 2.5000 y y

3.5 7% 12% 0 150 0 1.100E-02 3.5000 y y

both, so there are two 

sets of results. ? ? ? 0.00047, 0.00041 0.0900 y y

(7% O2, 12%CO2) ? ? ? 0.00063, 0.00054 0.1200 y y

(7% O2, 12%CO2) ? ? ? 0.00046, 0.00039 0.0800 y y

15.1 ? 0.006666667 30 0.2 4.900E-03 13.0300 y y y y

23.3 ? 0.008064516 62 0.5 6.800E-03 20.8700 y y y y

8.4 ? 0.008064516 62 0.5 2.300E-03 7.1400 y y y y

not found not found not found not found not found 5.000E-03 5.1200 y not found not found not found

not found not found not found not found not found 7.000E-03 6.4000 y not found not found not found

not found not found not found not found not found 7.000E-03 6.6100 y not found not found not found

3.3 both 0.001 100 0.1 1.700E-03 1.7500 y two points during run 1 were <90% y

4.3 both 0.0008 125 0.1 2.150E-03 2.2300 y y y

4.5 both 0.001 100 0.1 2.100E-03 2.2100 y y y
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WIGreenBayPackagingMillDivision

WIGreenBayPackagingMillDivision

WIGreenBayPackagingMillDivision

WI New Page Biron

WI New Page Biron

WI New Page Biron

SC Milliken Dewey Plant

SC Milliken Dewey Plant

SC Milliken Dewey Plant

TN Milan Army Ammunition Plant

TN Milan Army Ammunition Plant

TN Milan Army Ammunition Plant

VA GP Big Island 2703

VA GP Big Island 2703

VA GP Big Island 2703

WA Weyerhaeuser Raymond

WA Weyerhaeuser Raymond

WA Weyerhaeuser Raymond

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI New Page Biron

WI New Page Biron

WI New Page Biron

WI Wausau

WI Wausau

WI Wausau

WV Mountain State Carbon Follansbee

WV Mountain State Carbon Follansbee

WV Mountain State Carbon Follansbee

Mass Total (mg) Diluent correction (7% 

O2? 12% CO2?)

Reagent 

blank value 

(mg/ml)

Total 

reagent 

used (ml)

Blank 

correction 

value

Reported 

Gr/dscf

Reported 

Mass/Unit 

(lbs/mmbtu)

Meter cal 

y/n

Leak check 

y/n

Iso Check 

y/n

Nozzle 

check y/n

4 both 0.0024 125 0.3 1.300E-03 1.6300 y no way to tell b'c of bad sample calcs y

2.4 both 0.0024 125 0.3 1.100E-03 1.4000 y no way to tell b'c of bad sample calcs y

6.4 both 0.0024 125 0.3 3.000E-03 3.7400 y no way to tell b'c of bad sample calcs y

8.1 not found 0.008421053 190 1.6 1.500E-03 1.4900 y y

2.1 not found 0.008247423 194 1.6 2.400E-03 2.4200 y y

3.3 not found 0.008695652 184 1.6 3.800E-03 3.9000 y y

28.3 6% and 12.46%? (pg 95) 0.000877193 114 0.1 1.182E-02 9.0460 y not found

39.4 6% and 12.46%? 0.001 200 0.2 1.686E-02 12.8480 y not found

46.8 6% and 12.46%? 0.000851064 235 0.2 1.902E-02 14.8990 y not found

10.3 not found 0 158 0 3.000E-03 3.2500 0.967 y

9.6 not found 0 120 0 3.000E-03 3.0500 0.967 y

14.4 not found 0 154 0 4.000E-03 4.6100 0.967 y

7.7 both 0.001 100 0.1 3.100E-03 4.4200 y y

20.4 both 0.001 100 0.1 8.300E-03 11.7000 y y

1.3 both 0.001 100 0.1 5.000E-04 0.7400 y y

8.7 ? 0 90 0 6.600E-03 6.8000 y n y

9.4 ? 0 70 0 5.600E-03 5.5600 y n y

9.8 ? 0 100 0 1.290E-02 13.1300 y n y

2.8 ? 0 90 0 5.000E-04 0.2000 y y

0.1 ? 0 75 0 2.000E-05 0.0070 y y

2.1 ? 0 55 0 4.000E-04 0.1510 y y

8 y 0 95 0 2.100E-03 2.2890 y y y

3.5 y 0 55 0 1.400E-03 1.4740 y y y

3.9 y 0 76 0 1.600E-03 1.6990 y y y

11.3 ? not found 0 1.100E-03 0.0139 y y y

3.4 ? not found 0 4.000E-04 0.0051 y y y

2.4 ? not found 0.1 3.000E-04 0.0037 y y y

4.7 0 72.8 0 ? 0.0007 y y y

2.7 0 33.8 0 ? 0.0004 y y y

2.2 0 57 0 ? 0.0004 y y y

10.7 0 96 0 2.000E-03 1.2040 y y

7.9 0 96 0 1.700E-03 0.8800 y y

7.1 0 90 0 1.700E-03 0.7990 y y

not reported 7% O2 not reported not reportednot reported 7.300E-04 0.0900 not reported y not reported

not reported 7% O2 not reported not reportednot reported 8.500E-04 0.1090 not reported y not reported

not reported 7% O2 not reported not reportednot reported 2.700E-04 0.0370 not reported y not reported

4.2 7% O2 not found not found not found 4.200E-04 0.0910 y y

5.8 7% O2 not found not found not found 5.800E-04 0.1280 y y

5.4 7% O2 not found not found not found 5.600E-04 0.1200 y y

4.1 not found not found, assume 0 54 not found, assume 0.000E+00 0.4049 not found y

7.4 not found not found, assume 0 63 not found, assume 01.000E-03 0.7338 not found y

5.7 not found not found, assume 0 79 not found, assume 01.000E-03 0.5657 not found y

<1.06

0 50 0 <0.000456 0.0008 y y

2.8

0 75 0 1.210E-03 0.0016 y y

1.6 0 50 0.3 was treated as 0.6.700E-04 0.0013 y y

29.8 ? 0 265 0 3.180E-03 0.4120 y y

26.5 ? 0 260 0 3.120E-03 0.3680 y y

26.6 ? 0 255 0 3.130E-03 0.3730 y y
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

Mass Total (mg) Diluent correction (7% 

O2? 12% CO2?)

Reagent 

blank value 

(mg/ml)

Total 

reagent 

used (ml)

Blank 

correction 

value

Reported 

Gr/dscf

Reported 

Mass/Unit 

(lbs/mmbtu)

Meter cal 

y/n

Leak check 

y/n

Iso Check 

y/n

Nozzle 

check y/n

6.000E-04 0.8800 y

1.100E+01 1.5500 y

9.000E-04 1.2200 y

4.000E-04 0.5200 y

7.000E-04 0.9600 y

2.000E-04 0.2600 y

2.210E-02 22.2400

21 0.07 0.003 200 0.6 9.800E-03 11.3000 y y y

3.4 0.07 0.003 200 0.6 1.600E-03 1.7800 y y y

6 0.07 0.0005 200 0.1 2.300E-03 2.5800 y y y

7.4 0.07 0.0005 200 0.1 2.800E-03 3.1600 y y y

10.8 0.07 0.0005 200 0.1 4.100E-03 4.6300 y y y

20.4 both 0 250 0 8.000E-03 10.0900 y y y

14.2 both 0 250 0 5.300E-03 6.8000 y y y

63 both 0 250 0 2.350E-02 30.5900 y y y

72.1 0.07 0 200 0 2.820E-02 35.4100 y y y

27.8 0.07 0 200 0 1.030E-02 13.6500 y y y

16.1 0.07 0 200 0 6.000E-03 7.9200 y y y

0.74 cond. 1 average

1.07 cond. 2 average

4 0.07 0.0005 200 0.1 1.600E-03 1.6800 y y y

7.5 0.07 0.0005 200 0.1 3.000E-03 3.1000 y y y

3.4 0.07 0.0005 200 0.1 1.400E-03 1.4500 y y y

22.3 0.07 0 100 0 8.500E-03 8.9100 y y y

14.7 0.07 0 100 0 4.300E-03 5.7900 y y y

18.2 0.07 0 100 0 6.700E-03 7.2300 y y y

15.8 0.07 0.0005 200 0.1 6.100E-03 6.4600 y y y

5 0.07 0.0005 200 0.1 1.900E-03 2.0300 y y y

6 0.07 0.0005 200 0.1 2.200E-03 2.4300 y y y

15.4 0.07 0 200 0 5.730E-03 5.8400 y y y

7.6 0.07 0 200 0 2.730E-03 2.9400 y y y

4.9 0.07 0 200 0 1.880E-03 1.9300 y y y

13.4 0.07 0.038 100 3.8 3.900E-03 7.2300 y y y

10.6 0.07 0.038 100 3.8 3.000E-03 5.6300 y y y

10 0.07 0.036 100 3.6 3.200E-03 5.5100 y y y

7.1 0.07 0 200 0 3.000E-03 4.3100 y y y

4.7 0.07 0 200 0 2.100E-03 2.9500 y y y

7.1 0.07 0 200 0 3.200E-03 4.5400 y y y

11.9

0.07 0 200 0 4.900E-03 7.8500 y y y

15.5 0.07 0 200 0 6.600E-03 10.4700 y y y

10.9 0.07 0 200 0 4.600E-03 7.2400 y y y

27.1 0.07 0 155 0 4.100E-03 6.2700 y y y

8.9 0.07 0 100 0 1.400E-03 2.1500 y y y

19.3 0.07 0 100 0 3.100E-03 4.7200 y y y

15 0.07 0.002 200 0.4 2.100E-03 3.1900 y y y

8.9 0.07 0.002 200 0.4 1.300E-03 1.9200 y y y

10.8 0.07 0.002 200 0.4 1.600E-03 2.3200 y y y

169.6 0.07 0 200 0 3.370E-02 45.3800 y y y

62.1 0.07 0 200 0 3.120E-01 16.1600 y y y

118.8 0.07 0 200 0 2.260E-02 30.8500 y y y
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

WI Thilmany Paper

WI Thilmany Paper

WI Thilmany Paper

WI Thilmany Paper

WI Thilmany Paper

WI Thilmany Paper

WA Weyerhaeuser Raymond (11/2004)

WA Weyerhaeuser Raymond (11/2004)

Mass Total (mg) Diluent correction (7% 

O2? 12% CO2?)

Reagent 

blank value 

(mg/ml)

Total 

reagent 

used (ml)

Blank 

correction 

value

Reported 

Gr/dscf

Reported 

Mass/Unit 

(lbs/mmbtu)

Meter cal 

y/n

Leak check 

y/n

Iso Check 

y/n

Nozzle 

check y/n

107.4 0.07 0 200 0 2.090E-02 29.8700 y y y

125.5 0.07 0 200 0 2.280E-02 33.2400 y y y

145.5 0.07 0 200 0 2.710E-02 38.8500 y y y

8.9 0.07 0.002666667 150 0.4 1.300E-03 4.7100 y y y

7.8 0.07 0.002666667 150 0.4 1.200E-03 4.1100 y y y

17.5 0.07 0.002666667 150 0.4 2.300E-03 8.9800 y y y

24.9 0.07 0 200 0 6.130E-03 5.8600 y y y

13.6 0.07 0 200 0 3.240E-03 3.1600 y y y

20.7 0.07 0 200 0 4.820E-03 4.8200 y y y

49.8

not found 0 150 0 1.680E-02 6.1600 y y y y

30.5 not found 0 150 0 1.000E-02 3.9100 y y y y

- not found - - y y y y

34.4 not found 0 150 0 1.120E-02 4.3600 y y y y

64.6 not found 0 150 0 1.640E-02 12.8000 y y y y

69 not found 0 150 0 2.240E-02 21.4500 y y y y

57.9 not found 0 150 0 2.320E-02 17.7400 y y y y

10.7 not found 0.013333333 30 0.4 3.400E-03 2.0760 not found y y

8.1 not found 0.0125 40 0.5 2.400E-03 1.5180 not found y y

9.8 not found 0.013333333 30 0.4 3.000E-03 1.8860 not found y y

17.7 not found 0.015 20 0.3 6.300E-03 4.5560 not found y y

24.1 not found 0.013333333 30 0.4 8.200E-03 5.8600 not found n y

25.2 not found 0.0125 40 0.5 8.100E-03 5.8860 not found n y

157.3 not found 0.002083333 48 0.1 4.340E-02 25.4460 y y

134.8 not found 0.003225806 62 0.2 3.840E-02 23.9720 y y

175.7 not found 0.003076923 65 0.2 4.540E-02 28.4080 y y

14 not found 0.008333333 48 0.4 5.700E-03 3.0820 y y

7.9 not found 0.00952381 42 0.4 3.400E-03 1.4750 y y

6.5 not found 0.009259259 54 0.5 2.800E-03 1.2060 y y

18.7 not found 0 200 0 7.290E-03 4.0900 y y

14.7 not found 0 200 0 5.960E-03 3.4200 y y

16.7 not found 0 210 0 6.830E-03 3.7500 y y

11.1 not found not reported not reportednot reported 2.100E-03 0.9860 y y y

7.9 not found not reported not reportednot reported 1.500E-03 0.7040 y y y

4.8 not found not reported not reportednot reported 9.000E-04 0.4250 y y y

19.3

not found 0.00952381 42 0.4 6.400E-03 4.5030 y y y

13.6 not found 0.009302326 43 0.4 5.500E-03 3.7510 y y y

14 not found 0.01 40 0.4 5.600E-03 3.7220 y y y

11.5 not found 0.009756098 41 0.4 4.200E-03 2.8400 y y y

58.7 not found 0.009090909 44 0.4 2.630E-02 15.8010 y y y

55.5 not found 0.00952381 42 0.4 2.470E-02 16.1250 y y n

44.9 not found 0.00952381 42 0.4 1.830E-02 11.9420 y y y

41.4 not found 0.009302326 43 0.4 1.720E-02 11.3380 y y y

55.1 not found 0.00952381 42 0.4 2.530E-02 12.2110 y y y

44.6 not found 0.009302326 43 0.4 2.110E-02 9.9600 y y y

6.5 not found 0 30 0 not reported 0.8134 y y y

2.3 not found 0 30 0 not reported 0.2884 y y y

3.2 not found 0 38 0 not reported 0.4033 y y y

5.4 not found 0 18 0 not reported 0.6797 y y y

6.9 not found 0 23 0 not reported 0.8644 y y y

4 not found 0 38 0 not reported 0.5000 y y y

1.3 9.5, 11.4 0 120 0 3.000E-04 0.0100 y y 97

1.1 9.3, 11.4 0 120 0 3.000E-04 0.0030 y y 98
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

WA Weyerhaeuser Raymond (11/2004)

WA Weyerhaeuser Raymond (9/1996)

WA Weyerhaeuser Raymond (9/1996)

WA Weyerhaeuser Raymond (9/1996)

FL US Sugar Corp Boiler 8 (12/2009)

FL US Sugar Corp Boiler 8 (12/2009)

FL US Sugar Corp Boiler 8 (12/2009)

FL US Sugar Corp Boiler 8 (6/2006)

FL US Sugar Corp Boiler 8 (6/2006)

FL US Sugar Corp Boiler 8 (6/2006)

FL US Sugar Corp Boiler 8 (6/2006)

FL US Sugar Corp Boiler 8 (6/2006)

FL US Sugar Corp Boiler 8 (8/2006)

FL US Sugar Corp Boiler 8 (8/2006)

FL US Sugar Corp Boiler 8 (8/2006)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

GA GP Madison Ply (10/2004)

GA GP Madison Ply (10/2004)

GA GP Madison Ply (10/2004)

GA GP Madison Ply (6/2006)

GA GP Madison Ply (6/2006)

GA GP Madison Ply (6/2006)

GA GP Madison Ply (9/2007)

GA GP Madison Ply (9/2007)

GA GP Madison Ply (9/2007)

GA GP Madison Ply (6/2003)

GA GP Madison Ply (6/2003)

GA GP Madison Ply (6/2003)

GA GP Madison Ply (8/2009)

GA GP Madison Ply (8/2009)

GA GP Madison Ply (8/2009)

IL Abbott Abbott Park

IL Abbott Abbott Park

IL Abbott Abbott Park

MN American Crystal Crookston Boiler 1 (10/2005)

MN American Crystal Crookston Boiler 1 (10/2005)

MN American Crystal Crookston Boiler 1 (10/2005)

OH U of Cincinnati B108 (4/2006)

OH U of Cincinnati B108 (4/2006)

OH U of Cincinnati B108 (4/2006)

SC International Paper Eastover Boiler 1(10/2004)

SC International Paper Eastover Boiler 1(10/2004)

Mass Total (mg) Diluent correction (7% 

O2? 12% CO2?)

Reagent 

blank value 

(mg/ml)

Total 

reagent 

used (ml)

Blank 

correction 

value

Reported 

Gr/dscf

Reported 

Mass/Unit 

(lbs/mmbtu)

Meter cal 

y/n

Leak check 

y/n

Iso Check 

y/n

Nozzle 

check y/n

0.6 8.7, 11.9 0 110 0 2.000E-04 0.0040 101

4.6 10.7, 10.2 0 140 0 8.000E-04 0.0040 y y 106

3.3 10.6, 10.3 0 118 0 9.000E-04 0.0030 y y 103

4.5 9.4, 11.4 0 130 0 9.000E-04 0.0030 y y 101

15.6 6.4, 14.4 0 0 5.000E-03 0.0100 y y 104.5 y

12.4 7.0, 13.5 0 0 4.000E-03 0.0080 y y 100.7 y

6.6 5.6, 14.9 0 0 2.000E-03 0.0040 y y 100.7 y

3.5

7.58, 13.18 0.0053 160 0 1.900E-03 0.0041 y y 109.95

1.9 7.99, 12.67 0.0053 175 0 1.100E-03 0.0025 y y 104.1

1.6 9.22, 11.23 0.0053 165 0 8.000E-04 0.0019 y y 98.27

1.8 9.84, 10.63 0.0053 190 0 9.000E-04 0.0026 y y 94.96

1.5 9.10, 11.40 0.0053 150 0 9.000E-04 0.0022 y y 102.7

6.8

10.36, 10.03 0.015 100 0 3.200E-03 0.0101 y 93.17

12.8 10.43, 10.03 0.015 100 0 5.900E-03 0.0193 y 96.79

11.8 10.3, 9.89 0.015 100 0 5.400E-03 0.0167 y 95.71

15

7.73, 12.78 0.014 110 0 4.700E-03 0.0117 y 100.02

13.5 7.65, 12.71 0.014 95 0 3.900E-03 0.0094 y 99.95

17.7 7.25, 13.17 0.014 125 0 5.100E-03 0.0122 y 101.98

7.5

6.52, 14.44 0.004 130 0 0.0040 y y 102.27 y

5.3 6.96, 14.09 0.004 120 0 0.0030 y y 103.02 y

6.4 0.004 140 0 y y y

6.8 6.53, 14.57 0.004 110 0 0.0040 y y 104.6 y

2.6 8.82, 11.68 177 0 1.000E-03 0.0020 y y 96.45 y

3.7 8.76, 11.83 165 0 1.500E-03 0.0030 y y 100.52 y

1.9 9.06, 11.42 175 0 7.000E-04 0.0020 y y 100.8 y

5.3 7.75, 12.59 160 0 1.600E-03 0.0033 y y 100.37 y

6.9 8.13, 12.38 120 0 1.900E-03 0.0042 y y 102.18 y

5.1 8.46, 12.10 130 0 1.400E-03 0.0032 y y 102.05 y

26.7 7.35, 12.0 150 0 1.050E-02 0.0215 y y 99.3 y

8.5 6.60, 12.5 125 0 3.600E-03 0.0071 y y 97.85 y

19 7.51, 12.0 125 0 7.900E-03 0.0164 y y 95.96 y

8.6 9.78, 10.85 350 0 1.600E-03 0.0040 y y 95.27 y

3.6 9.55, 11.06 275 0 7.000E-04 0.0020 y y 95.44 y

3.4 7.91, 12.64 275 0 7.000E-04 0.0020 y y 97.39 y

9.9 8.88, 11.52 100 0 y y 98.3

0.1 8.21, 12.04 100 0 y y 102.9

5.8 7.21, 12.79 100 0 y y 92.1

27.9 9.93, 10.90 4.9 0 1.270E-02 0.0340 y y 100.2 y

15.9 9.77, 9.34 4.9 0 7.200E-03 0.0190 y y 101.4 y

9.8 9.61, 10.04 4.9 0 4.300E-03 0.0110 y y 102.5 y

3.6 11.5, 9.0 150 0 1.200E-03 0.0037 y y 100.5

2.3 11.5, 9.0 150 0 8.000E-04 0.0024 y y 101

4.7 11.5, 9.0 150 0 1.600E-03 0.0050 y y 99.6

17.6 5.60, 13.50 0 7.200E-03 0.0137 y y 99.9 y

6.3 5.90, 13.20 0 2.600E-03 0.0051 y y 100.7 y
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

SC International Paper Eastover Boiler 1(10/2004)

SC International Paper Eastover Boiler 1(10/2000)

SC International Paper Eastover Boiler 1(10/2000)

SC International Paper Eastover Boiler 1(10/2000)

SC International Paper Eastover Boiler 1(10/2006)

SC International Paper Eastover Boiler 1(10/2006)

SC International Paper Eastover Boiler 1(10/2006)

SC International Paper Eastover Boiler 1(10/2002)

SC International Paper Eastover Boiler 1(10/2002)

SC International Paper Eastover Boiler 1(10/2002)

SC International Paper Eastover Boiler 2(10/2002)

SC International Paper Eastover Boiler 2(10/2002)

SC International Paper Eastover Boiler 2(10/2002)

SC International Paper Eastover Boiler 2(3/2008)

SC International Paper Eastover Boiler 2(3/2008)

SC International Paper Eastover Boiler 2(3/2008)

SC International Paper Eastover Boiler 2(3/2004)

SC International Paper Eastover Boiler 2(3/2004)

SC International Paper Eastover Boiler 2(3/2004)

SC International Paper Eastover Boiler 2(6/1999)

SC International Paper Eastover Boiler 2(6/1999)

SC International Paper Eastover Boiler 2(6/1999)

SC International Paper Eastover Boiler 2(6/2003)

SC International Paper Eastover Boiler 2(6/2003)

SC International Paper Eastover Boiler 2(6/2003)

SC International Paper Eastover Boiler 2(8/1997)

SC International Paper Eastover Boiler 2(8/1997)

SC International Paper Eastover Boiler 2(8/1997)

SC International Paper Eastover Boiler 2(8/1995)

SC International Paper Eastover Boiler 2(8/1995)

SC International Paper Eastover Boiler 2(8/1995)

SC International Paper Eastover Boiler 2(8/1993)

SC International Paper Eastover Boiler 2(8/1993)

SC International Paper Eastover Boiler 2(8/1993)

TN Cargill Memphis Boiler 8001(8/2009)

TN Cargill Memphis Boiler 8001(8/2009)

TN Cargill Memphis Boiler 8001(8/2009)

TN Cargill Memphis Boiler 8001(7/2007)

TN Cargill Memphis Boiler 8001(7/2007)

TN Cargill Memphis Boiler 8001(7/2007)

Mass Total (mg) Diluent correction (7% 

O2? 12% CO2?)

Reagent 

blank value 

(mg/ml)

Total 

reagent 

used (ml)

Blank 

correction 

value

Reported 

Gr/dscf

Reported 

Mass/Unit 

(lbs/mmbtu)

Meter cal 

y/n

Leak check 

y/n

Iso Check 

y/n

Nozzle 

check y/n

3.9 5.40, 13.70 0 1.500E-03 0.0028 y y 100.7 y

74 6.0, 13.0 152 0.3 3.000E-02 0.0590 y y 99 y

27.7 6.1, 13.0 111 0.2 1.100E-02 0.0220 y y 105 y

57.7 5.9, 13.2 94 0.2 2.300E-02 0.0440 y y 106 y

5.2 3.2, 15.1 0 2.000E-03 0.0033 y y 100.3 y

6.5 3.6, 17.0 0 2.500E-03 0.0042 y y 101.6 y

1.7 3.8, 17.1 0 7.000E-04 0.0012 y y 100.6 y

45 6.1, 13.3 0.0044 68 0.6 1.800E-02 0.0360 y y 99 y

55.5 3.1, 13.3 0.0044 74 0.6 2.200E-02 0.0440 y y 98 y

42.6 5.8, 13.4 0.0044 38 0.5 1.800E-02 0.0340 y y 99 y

12.4 7.66, 12.62 0.0052 88.2 0.5 2.500E-03 0.0053 y y 97.7 y

8.6 7.67, 12.61 0.0052 102.3 0.5 1.600E-03 0.0034 y y 100.6 y

9.7 7.48, 13.26 0.0052 78.6 0.5 1.900E-03 0.0040 y y 101.2 y

23.3 10.1, 10.3 0.0005 130 -0.1 4.500E-03 0.0118 y y 100 y

24.4 9.8, 10.0 0.0005 125 -0.1 4.600E-03 0.0117 y y 100 y

7.8 10.1, 10.2 0.0005 98 0 1.500E-03 0.0039 y y 99 y

18.6 7.5, 12.8 0.0011 84 1.2 3.500E-03 0.0074 y y 100 y

16.3 7.3, 12.9 0.0011 92 1.2 3.300E-03 0.0068 y y 101 y

25.9 6.8, 12.5 0.0011 64 1 5.300E-03 0.0107 y y 101 y

3.3 6.5, 12.9 0.0027 125 0.3 2.000E-03 0.0014 y 107 y

8.7 6.3, 13.1 0.0027 154 0.4 3.000E-03 0.0039 y 105 y

6.1 6.1, 13.9 0.0027 140 0.4 3.000E-03 0.0026 y 104 y

25.5 8.7, 11.4 0.0019 74 1.4 5.000E-03 0.0117 y y 93.4 y

14.7 8.3, 11.8 0.0019 72 1.4 3.000E-03 0.0065 y y 94 y

11.6 8.4, 11.8 0.0019 74 1.4 2.000E-03 0.0050 y y 98.7 y

40.8 3.60, 11.70 0.00078 200 0.1 8.700E-03 0.0140 109.85

24 3.30, 12.30 0.00078 140 0.1 5.800E-03 0.0090 102.96

61.3 3.10, 13.70 0.00078 200 0.1 1.480E-02 0.0230 103.83

11.4 8.3, 10.8 137 2.15 2.700E-03 0.0058 y y 113 y

8.8 7.1, 12.3 134 2.15 2.100E-03 0.0042 y y 112 y

7.25 6.3, 13.1 132 2.15 1.700E-03 0.0032 y y 113 y

108

7.1, 13.1 0.55 0.2 3.550E-02 0.0710 y y 102 y

57.4 7.1, 13.0 0.19 0.2 1.650E-02 0.0336 y y 103 y

42.9 7.5, 12.7 0.97 0.2 1.400E-02 0.0289 y y 102 y

2.7 10.84, 8.98 2.000E-04 0.0007 y y 101 y

3 10.31, 9.35 3.000E-04 0.0007 y y 100 y

2.4 10.25, 9.39 2.000E-04 0.0006 y y 101 y

20.9 12.4, 7.5 0.001 65 0.6 6.100E-03 0.0210 y y 106.7

17.9 12.2, 7.8 0.001 60 0.5 5.300E-03 0.0178 y y 105.9

13.9 11.9, 8.0 0.001 45 0.4 4.100E-03 0.0133 y y 105.6
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

AK Doyon Utilities/ Unit 4

AK Doyon Utilities/ Unit 4

AK Doyon Utilities/ Unit 4

AK Doyon Utilities/ Unit 7

AK Doyon Utilities/ Unit 7

AK Doyon Utilities/ Unit 7

AR Weyerhaeuser Dierks Mill / Unit 5 (1997) 

AR Weyerhaeuser Dierks Mill / Unit 5 (1997) 

AR Weyerhaeuser Dierks Mill / Unit 5 (1997) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (1997) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (1997) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (1997) 

FL Smurfit-Stone

FL Smurfit-Stone

FL Smurfit-Stone

GA GP Monticello Plywood (2/21/08)

GA GP Monticello Plywood (2/21/08)

GA GP Monticello Plywood (2/21/08)

GA GP Monticello Plywood (2/7/07)

GA GP Monticello Plywood (2/7/07)

GA GP Monticello Plywood (2/7/07)

IA ADM Corn Processing Cedar Rapids

IA ADM Corn Processing Cedar Rapids

IA ADM Corn Processing Cedar Rapids

IA Iowa State University B1

IA Iowa State University B1

IA Iowa State University B1

IA Iowa State University B2

IA Iowa State University B2

IA Iowa State University B2

IA Monsanto Muscatine #8 Cond. 1 (5/2007)

IA Monsanto Muscatine #8 Cond. 1 (5/2007)

IA Monsanto Muscatine #8 Cond. 1 (5/2007)

IA Monsanto Muscatine #8 Cond. 3 (5/2007)

IA Monsanto Muscatine #8 Cond. 3 (5/2007)

IA Monsanto Muscatine #8 Cond. 3 (5/2007)

IA Monsano Muscatine #8 Cond. 1 (8/2007)

IA Monsano Muscatine #8 Cond. 1 (8/2007)

IA Monsano Muscatine #8 Cond. 1 (8/2007)

ID Amalgamated Suger Co. Twin Falls

ID Amalgamated Suger Co. Twin Falls

ID Amalgamated Suger Co. Twin Falls

Notes: Action

In calculating the PM a 0.05 mg was added to the final value after the 

acetone blank raw data does not support this, it is listed as .3 mg in raw data 

but .25 mg in final spreadsheet. 

Individual water vapor percents were calculated based upon weights of the 

water recovered. Reported Values are in lbs/dscf 

Run 1 very high probe rinse component.

For this value they had 25.0 mg reported

values kept as is, resultant lb/mmBtu value ok

values kept as is, resultant lb/mmBtu value ok

The values for gr/dscf and lbs/MMBtu went below the number of significant 

figures carried throughout the calculations the lb/dscf was (3.74, 4.23, 

2.50)e-8 respectively

Database updated, see A-2 for calcs.

values kept as is, resultant lb/mmBtu value ok

The values for gr/dscf and lbs/MMBtu went below the number of significant 

figures carried throughout the calculations the lb/dscf was (3.74, 4.23, 

2.50)e-8 respectively

Database updated, see A-2 for calcs.

This is the lowest polluting of the two permited operating conditions.

Lowest of the runs even though this situation was not used for compliance. 

This was a combination of coal/corn which was not typical according to the 

report
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

IA Monsano Muscatine #8 Cond. 1 (10/2009)

IA Monsano Muscatine #8 Cond. 1 (10/2009)

IA Monsano Muscatine #8 Cond. 1 (10/2009)

IA U of Northern Iowa #3 (10/2009)

IA U of Northern Iowa #3 (10/2009)

IA U of Northern Iowa #3 (10/2009)

IL PilyOne Boiler 1 (9/2009)

IL PilyOne Boiler 1 (9/2009)

IL PilyOne Boiler 1 (9/2009)

IN Purdue University Boiler 5 (7/2009)

IN Purdue University Boiler 5 (7/2009)

IN Purdue University Boiler 5 (7/2009)

ME Boralex Stratton Boiler 1 (10/2009)

ME Boralex Stratton Boiler 1 (10/2009)

ME Boralex Stratton Boiler 1 (10/2009)

MI Consumer Energy Co - Campbell (9/2009)

MI Consumer Energy Co - Campbell (9/2009)

MI Consumer Energy Co - Campbell (9/2009)

OH Smart Papers Holdings LLC (10/2005)

OH Smart Papers Holdings LLC (10/2005)

OH Smart Papers Holdings LLC (10/2005)

SC GP Chem Russellville (8/2009)

SC GP Chem Russellville (8/2009)

SC GP Chem Russellville (8/2009)

SC Marlboro Paper (7/2009)

SC Marlboro Paper (7/2009)

SC Marlboro Paper (7/2009)

TN Eastman NO CBI DATA 

TN Eastman NO CBI DATA 

TN Eastman NO CBI DATA 

VADukeEnergyNarrows Boiler 2

VADukeEnergyNarrows Boiler 2

VADukeEnergyNarrows Boiler 2

VADukeEnergyNarrows Boiler 3

VADukeEnergyNarrows Boiler 3

VADukeEnergyNarrows Boiler 3

VA University of Virginia 7103-1-01R (12/2007)

VA University of Virginia 7103-1-01R (12/2007)

VA University of Virginia 7103-1-01R (12/2007)

VA University of Virginia 7103-1-01R

VA University of Virginia 7103-1-01R

VA University of Virginia 7103-1-01R

VA University of Virginia 7103-1-02R

VA University of Virginia 7103-1-02R

VA University of Virginia 7103-1-02R

VA University of Virginia 7103-1-05

VA University of Virginia 7103-1-05

VA University of Virginia 7103-1-05

WA Grays Harbor Paper (6/2006)

WA Grays Harbor Paper (6/2006)

WA Grays Harbor Paper (6/2006)

Notes: Action

There was no Rinse value associated with this test. All of the mass came 

from filter weight.

No filter temp.

Could not find supporting documents for lab analysis. Only had summary 

tables with weight gain of the method 5 runs. No determination based upon 

filter or rinse.

No information regarding analytical rinse. Data was only seperated 

between filterable and condensable.

Database updated, see A-2 for calcs.

Boiler is an Auxilary boiler and was run not at full load. The boiler also does 

not have any controls on the stack.

No statement on the calculation of the analytical rinse

Run 1 much higher than 2,3

Blank values for the acetone rinse were high.

Low sample mass / volume

Low sample mass / volume Database updated, see A-2 for calcs.

Low sample mass / volume Database updated, see A-2 for calcs.

PM data not presented

PM data not presented

PM data not presented

For Run 1, 2 they got an acetone blank of 1.48 mg but then used the 

maximum allowable blank of .94 in the calculations. For run 3 they got an 

acetone blank of 1.6 mg and used 1.02

These values are very high in comparison to the other tests. This is a dutch 

oven and the emissions values are from the stack and not the stack/duct 

combination (which would likely lower emissions concentration numbers 

reported from the unit).
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

AR Potlatch Forest Warren (8/2006)

AR Potlatch Forest Warren (8/2006)

AR Potlatch Forest Warren (8/2006)

AR Potlatch Forest Warren (9/2009)

AR Potlatch Forest Warren (9/2009)

AR Potlatch Forest Warren (9/2009)

AR Weyerhaeuser Dierks Mill/ Unit 7 (12/2002) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (12/2002) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (12/2002) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (2/2009) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (2/2009) 

AR Weyerhaeuser Dierks Mill/ Unit 7 (2/2009) 

IA Archers Daniels Midland Des Moines Boiler 1 (6/2008)

IA Archers Daniels Midland Des Moines Boiler 1 (6/2008)

IA Archers Daniels Midland Des Moines Boiler 1 (6/2008)

IA Archers Daniels Midland Des Moines Boiler 1 (8/2009)

IA Archers Daniels Midland Des Moines Boiler 1 (8/2009)

IA Archers Daniels Midland Des Moines Boiler 1 (8/2009)

ID Potlatch (7/2009)

ID Potlatch (7/2009)

ID Potlatch (7/2009)

ME New Page-Rumford Cogen #6 and #7(12/2009)

ME New Page-Rumford Cogen #6 and #7(12/2009)

ME New Page-Rumford Cogen #6 and #7(12/2009)

MSWeyerhaeuserBruce Boiler 2 (8/2009)

MSWeyerhaeuserBruce Boiler 2 (8/2009)

MSWeyerhaeuserBruce Boiler 2 (8/2009)

ID Riley Creek Lumber

ID Riley Creek Lumber

ID Riley Creek Lumber

ID Riley Creek Lumber

ID Riley Creek Lumber

ID Riley Creek Lumber

ID Tasco Nampa, Riley Boiler

ID Tasco Nampa, Riley Boiler

ID Tasco Nampa, Riley Boiler

ID Tasco Nampa

ID Tasco Nampa

ID Tasco Nampa

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN Purdue Univ.

IN SABIC Plastics

IN SABIC Plastics

IN SABIC Plastics

IN SABIC Plastics

IN SABIC Plastics

IN SABIC Plastics

Notes: Action

No gr/dscf but mg/dscm were 49.13, 6.40, 4.46 respectively 

No description of acetone rinse and or filter/rinse components. 

Less signs were used in the report.

discrepancy between field data sheet and results page Database updated, see A-2 for calcs.

discrepancy between field data sheet and results page Database updated, see A-2 for calcs.

discrepancy between field data sheet and results page Database updated, see A-2 for calcs.

they did a nozzle calc, but I don’t know if it passed

not very complete

not a full report, only results, no example calcs, filter or rinse masses, etc
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

IN SABIC Plastics

IN SABIC Plastics

IN SABIC Plastics

LA Port Hudson

LA Port Hudson

LA Port Hudson

LA Port Hudson

LA Port Hudson

LA Port Hudson

MI City of Escanaba

MI City of Escanaba

MI City of Escanaba

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Boise Paper 1212

MN Boise Paper 1212

MN Boise Paper 1212

WA Grays Harbor Paper 

WA Grays Harbor Paper 

WA Grays Harbor Paper 

WA Weyerhaeuser Co.

WA Weyerhaeuser Co.

WA Weyerhaeuser Co.

WI Domtar 2814

WI Domtar 2814

WI Domtar 2814

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

Notes: Action

Database updated, see A-2 for calcs.

Database updated, see A-2 for calcs.

Database updated, see A-2 for calcs.

Database updated, see A-2 for calcs.

Database updated, see A-2 for calcs.

Database updated, see A-2 for calcs.

Mass is reported as TPM (dry catch + organic condensibles + aqueous phase 

condensibles) filterable is in ()s

Database updated, see A-2 for calcs.

Mass is reported as TPM (dry catch + organic condensibles + aqueous phase 

condensibles) filterable is in ()s

Database updated, see A-2 for calcs.

Mass is reported as TPM (dry catch + organic condensibles + aqueous phase 

condensibles) filterable is in ()s

Database updated, see A-2 for calcs.

OTM 28 and M29 were done simultaneously. 

OTM 28 and M29 were done simultaneously. Only run 1 shows the blank 

correction.

OTM 28 and M29 were done simultaneously. Only run 1 shows the blank 

correction.

ok, calcs in report are correct

A soot blow, which typically occurs 3xs/day, happened in run 2. Database updated, see A-2 for calcs.

the total pm results include M202 data.

the total pm results include M202 data.

Masses are front half only. I didn't include back half which was much 

greater.

No actual sample calcs, just equations

missing data: filter weight, rinse weight, volume of reagent, sample calc

filter blank of 0.1mg

filter blank of 0.1mg

filter blank of 0.1mg

Left side of page is missing in first ~20 pages. Filter temp is too high

Filter temp is too high

Filter temp is too high

Boiler #9 goes through stack 11

no actual values in the sample calcs, just formulas

no actual values in the sample calcs, just formulas
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WIGreenBayPackagingMillDivision

WIGreenBayPackagingMillDivision

WIGreenBayPackagingMillDivision

WI New Page Biron

WI New Page Biron

WI New Page Biron

SC Milliken Dewey Plant

SC Milliken Dewey Plant

SC Milliken Dewey Plant

TN Milan Army Ammunition Plant

TN Milan Army Ammunition Plant

TN Milan Army Ammunition Plant

VA GP Big Island 2703

VA GP Big Island 2703

VA GP Big Island 2703

WA Weyerhaeuser Raymond

WA Weyerhaeuser Raymond

WA Weyerhaeuser Raymond

WI GPGreenBay 2818

WI GPGreenBay 2818

WI GPGreenBay 2818

WI New Page Biron

WI New Page Biron

WI New Page Biron

WI Wausau

WI Wausau

WI Wausau

WV Mountain State Carbon Follansbee

WV Mountain State Carbon Follansbee

WV Mountain State Carbon Follansbee

Notes: Action

no way to tell b'c of bad sample calcs

no way to tell b'c of bad sample calcs

no way to tell b'c of bad sample calcs

high temp to prevent sulfate from forming on the filter. Actual rinse wgt was 

7.4mg (1.6 was subtracted).

net weight of rinse was -0.1. corrected wt = 0.0mg

backup filter was 1.3mg.

backup filter was -0.3mg.

backup filter was 0.5mg.

high temp to prevent sulfate from forming on the filter

Highlighted areas are totals (front and back half), not just filterable

No field data sheets.

Run 2 much lower than other two runs (1 and 3). Removing this test, broken 

vacuum suspected and no final leadk detection in report.

Database updated, see A-2 for calcs.

No controls

lab said moisture was on filters so they were baked at 105C until dry. 

ok, calcs in report are correct

Mass fractions for which the lab results was 0 were assigned the DL of 

0.1mg.

highlighted areas are values that had BDL fractions

no actual values in the sample calcs, just formulas

no actual values in the sample calcs, just formulas

Boiler #5 has two IK soot blowers that operate once, for 5 minutes each, per 

8-hour shift and a third IK soot blower that is operated for 5 minutes once 

every 24 hours.

Database updated, see A-2 for calcs.

During Run 2 on Boiler #5 all three soot blowers will be operated, one after 

the other, for a total soot blow duration of 15 minutes. For all Boiler #5 

particulate test runs

CleanAir performed 2.5 minute points yielding 6 points (50%) of the duct 

traversed during the soot blow.

Database updated, see A-2 for calcs.

Reports states that filterable front-half emissions are also PM2.5 emissions 

(p 11)
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

Notes: Action

Two conditions were tested: 1. non-ozone season and 2. low-NOx mode 

inside the ozone season.

NO FIELD DATA, FILTER/RINSE DATA, OR M5 RESULTS. VERY INCOMPLETE

NO FIELD DATA, FILTER/RINSE DATA, OR M5 RESULTS. VERY INCOMPLETE

The leak check of run 1 failed. Due to time constraints the TDAPC contact 

allowed test certification on the basis of runs 2 and 3 only.

Soot blowing was conducted during run 3.

Run 2 was void after the 2nd port change due to a broken impinger

Run 1 was voided b'c a probe liner broke. Soot blowing was performed 

during Run 4.

Two conditions were tested: 1. non-ozone season and 2. low-NOx mode 

inside the ozone season.

NO FIELD DATA, FILTER/RINSE DATA, OR M5 RESULTS. VERY INCOMPLETE

Run 3 was voided due to an operational upset Database updated, see A-2 for calcs.

Database updated, see A-2 for calcs.

Database updated, see A-2 for calcs.

Leak check failed on Run 3, so it was voided.

The pm catch was less than the DL of 6mg, so 4.7mg was used. 

Small shards of glass were found in the filter housing of runs 2 and 3, but the 

observer from TDAPC said it was ok and the shards were removed before 

weighing.

Soot blow during run 1

During run 1 a glass connector between the filter and impinger 1 broke, so 

the run was terminated.
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Duke Energy Narrows

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

VA Georgia Pacific Big Island

WI Thilmany Paper

WI Thilmany Paper

WI Thilmany Paper

WI Thilmany Paper

WI Thilmany Paper

WI Thilmany Paper

WA Weyerhaeuser Raymond (11/2004)

WA Weyerhaeuser Raymond (11/2004)

Notes: Action

Soot blow during run 3

17.5mg is erroneous. It should be 16.7

soot blowing during run 3

4 runs were done but the test report doesn't document why. There is no 

front half data for run 3, so I assume there was an issue. The lab only reports 

data for 3 runs, so I'm assuming those samples are from runs 1,2, and 4.

Sample volume is <30dscf

Sample volume is <30dscf

Sample volume is <30dscf

The test location is only 1.4 and 1.7 equivalent diameters up and 

downstream from disturbances.

this is not well documented. They did 6 runs plus two sets of two but no 

discussion of why. Runs were 48 minutes each but the report states they 

were 60 minutes.

Isokinetics ~88%, void this run.

Soot blowing occurred during run 2 for thirty minutes

Soot blowing occurs three times per day for 30 minutes each.

Soot blowing occurred during run 2 for thirty minutes

Soot blowing occurs three times per day for 30 minutes each.
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

WA Weyerhaeuser Raymond (11/2004)

WA Weyerhaeuser Raymond (9/1996)

WA Weyerhaeuser Raymond (9/1996)

WA Weyerhaeuser Raymond (9/1996)

FL US Sugar Corp Boiler 8 (12/2009)

FL US Sugar Corp Boiler 8 (12/2009)

FL US Sugar Corp Boiler 8 (12/2009)

FL US Sugar Corp Boiler 8 (6/2006)

FL US Sugar Corp Boiler 8 (6/2006)

FL US Sugar Corp Boiler 8 (6/2006)

FL US Sugar Corp Boiler 8 (6/2006)

FL US Sugar Corp Boiler 8 (6/2006)

FL US Sugar Corp Boiler 8 (8/2006)

FL US Sugar Corp Boiler 8 (8/2006)

FL US Sugar Corp Boiler 8 (8/2006)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

FL US Sugar Corp Boiler 8 (1/2007)

GA GP Madison Ply (10/2004)

GA GP Madison Ply (10/2004)

GA GP Madison Ply (10/2004)

GA GP Madison Ply (6/2006)

GA GP Madison Ply (6/2006)

GA GP Madison Ply (6/2006)

GA GP Madison Ply (9/2007)

GA GP Madison Ply (9/2007)

GA GP Madison Ply (9/2007)

GA GP Madison Ply (6/2003)

GA GP Madison Ply (6/2003)

GA GP Madison Ply (6/2003)

GA GP Madison Ply (8/2009)

GA GP Madison Ply (8/2009)

GA GP Madison Ply (8/2009)

IL Abbott Abbott Park

IL Abbott Abbott Park

IL Abbott Abbott Park

MN American Crystal Crookston Boiler 1 (10/2005)

MN American Crystal Crookston Boiler 1 (10/2005)

MN American Crystal Crookston Boiler 1 (10/2005)

OH U of Cincinnati B108 (4/2006)

OH U of Cincinnati B108 (4/2006)

OH U of Cincinnati B108 (4/2006)

SC International Paper Eastover Boiler 1(10/2004)

SC International Paper Eastover Boiler 1(10/2004)

Notes: Action

lb/MMBtu includes condesnable. Run 3 does not have supporting material in 

the report

Database updated, see A-2 for calcs.

lb/MMBtu includes condensable

Volume of Acetone used was not recorded for all runs. Only run 1 which 

used 71.6595 g

Runs 3,4,5 were used for compliace. Acetone Blank was not used to correct 

wash values. There was only one blank weighed but I noted it for each run. 

The boiler was also only running at 50% load which is "normal" for non-peak 

season load. Only Bagasse was used for firing.

The boiler was firing only wood chips this test. There was only one blank 

weighed but I noted it for each run. No blank correction was made

The boiler was firing only Bagasse this test. There was only one blank 

weighed but I noted it for each run. No blank correction was made

The boiler was firing only on Bagasse this test. Run 3 was aborted due to 

plant malfunction. There was only one blank weighed but I noted it for each 

run. No blank correction was made

Subtracted a negative filter weight from the Acetone Wash values. Database updated, see A-2 for calcs.

Subtracted a negative filter weight from the Acetone Wash values. Database updated, see A-2 for calcs.

Subtracted a negative filter weight from the Acetone Wash values. Database updated, see A-2 for calcs.

No blanks

The grates were raked during run 3. No blanks were reported

No Blanks

No blanks and the report did not have gr/dscf or lbs/MMBtu

Database updated, see A-2 for calcs.

The summary for the boiler does not match the supporting data.

No blanks

Weight of Acetone wash was only recorded not the volume of the wash. A 

blank was done and no correction was recorded.
Appendix A-1 - PM Tracking Sheet for Boiler Data Review

Facility/Unit

SC International Paper Eastover Boiler 1(10/2004)

SC International Paper Eastover Boiler 1(10/2000)

SC International Paper Eastover Boiler 1(10/2000)

SC International Paper Eastover Boiler 1(10/2000)

SC International Paper Eastover Boiler 1(10/2006)

SC International Paper Eastover Boiler 1(10/2006)

SC International Paper Eastover Boiler 1(10/2006)

SC International Paper Eastover Boiler 1(10/2002)

SC International Paper Eastover Boiler 1(10/2002)

SC International Paper Eastover Boiler 1(10/2002)

SC International Paper Eastover Boiler 2(10/2002)

SC International Paper Eastover Boiler 2(10/2002)

SC International Paper Eastover Boiler 2(10/2002)

SC International Paper Eastover Boiler 2(3/2008)

SC International Paper Eastover Boiler 2(3/2008)

SC International Paper Eastover Boiler 2(3/2008)

SC International Paper Eastover Boiler 2(3/2004)

SC International Paper Eastover Boiler 2(3/2004)

SC International Paper Eastover Boiler 2(3/2004)

SC International Paper Eastover Boiler 2(6/1999)

SC International Paper Eastover Boiler 2(6/1999)

SC International Paper Eastover Boiler 2(6/1999)

SC International Paper Eastover Boiler 2(6/2003)

SC International Paper Eastover Boiler 2(6/2003)

SC International Paper Eastover Boiler 2(6/2003)

SC International Paper Eastover Boiler 2(8/1997)

SC International Paper Eastover Boiler 2(8/1997)

SC International Paper Eastover Boiler 2(8/1997)

SC International Paper Eastover Boiler 2(8/1995)

SC International Paper Eastover Boiler 2(8/1995)

SC International Paper Eastover Boiler 2(8/1995)

SC International Paper Eastover Boiler 2(8/1993)

SC International Paper Eastover Boiler 2(8/1993)

SC International Paper Eastover Boiler 2(8/1993)

TN Cargill Memphis Boiler 8001(8/2009)

TN Cargill Memphis Boiler 8001(8/2009)

TN Cargill Memphis Boiler 8001(8/2009)

TN Cargill Memphis Boiler 8001(7/2007)

TN Cargill Memphis Boiler 8001(7/2007)

TN Cargill Memphis Boiler 8001(7/2007)

Notes: Action

Weight of Acetone wash was only recorded not the volume of the wash. A 

blank was done and no correction was recorded.

The blank correction values include .3 mg for the filter blank.

Negative Acetone blanks

High temperatures. The blank correction value includes a .5 mg correction 

for the filter blank

High temperatures. A filter blank of .5 mg was found but was not applied to 

the samples

High temperatures

No flow data for runs 2 and 3

Volume of rinse was calculated based upon the mass and a density of .79 

provided by the report

A note was made about the Acetone wash values that it was suspected to be 

high because of contamination but it will still be used because it biases the 

values high. Also the rinse mL seem to be low but were calculated base 

upon weight and a report density of .79.

The filterable pm values were reported as .5 because that seemed to be the 

detection level of the instrument making the reading. 
Appendix A-2 - Calculations for PM Data Revisions

Facility/Unit Category/ sub-category Run ID FacilityID Unit ID Test Date Run ID Data Source Source Tab Oxygen% F-Factor

WIGreenBayPackagingMillDivi

sion Boiler B26/Coal fired (2006) 2

WIGreenBayPackagingMillDi

vision

Boiler B26- Coal Fired 

Boiler 5/16/2006 ALL ICR Phase I PM and Metals{PM & HgB26} 10.75 9780

IA Iowa State University B2 solid/coal 1 IAIAStateUnivPowerPlant B2 3/27/2008 Sample #1 ICR Phase I PM and Metals (2) 4 9780

IA Iowa State University B2 solid/coal 3 IAIAStateUnivPowerPlant B2 3/27/2008 Sample #3 ICR Phase I PM and Metals (2) 3.7 9780

ME Boralex Stratton Boiler 1 

(10/2009) solid/biomass 1 MEBoralexStratton Boiler #1 10/21/2009 Sample #1 ICR Phase II - Templates

PM Additions from Test 

Report

6.3 9600

VA University of Virginia 7103-

1-01R (12/2007) solid/coal 2 VAUniversityofVirginia 7103-1-01R 12/6/2007 Sample #2 ICR Phase I PM and Metals 7.03 9780

VA University of Virginia 7103-

1-01R (12/2007) solid/coal 3 VAUniversityofVirginia 7103-1-01R 12/6/2007 Sample #3 ICR Phase I PM and Metals 6.98 9780

WI Domtar 2814 Solid/Biomass 1 WIDomtar2814 B11, S11 8/29/2007 Sample #1 ICR Phase I PM and Metals (B11) 9.4 13680

GA GP Madison Ply (8/2009) solid/biomass 2 GAGPMadisonPly 800 Wood Waste Boiler 8/12/2009 2 ICR Phase II - ERT ERT 8.21 9600

WI Wausau Solid/Coal (boiler 5) 1 WIWausau # 5 Power Boiler (B24) 7/24/2007 Sample #1 ICR Phase I PM (B24) 11 9780

WI Wausau Solid/Coal (boiler 5) 3 WIWausau # 5 Power Boiler (B24) 7/24/2007 Sample #3 ICR Phase I PM (B24) 11.2 9780

ID Tasco Nampa Solid/Coal 1 IDTASCONampa Riley Boiler 1/12/2004 Sample #1 ICR Phase I PM and Metals (3) 6.3 9780

ID Tasco Nampa Solid/Coal 2 IDTASCONampa Riley Boiler 1/12/2004 Sample #2 ICR Phase I PM and Metals (3) 6.4 9780

ID Tasco Nampa Solid/Coal 3 IDTASCONampa Riley Boiler 1/12/2004 Sample #3 ICR Phase I PM and Metals (3) 6.4 9780

MN Boise Paper 1212 Boiler #2 6/2005 (PM10) 1 MNBoisePaper1212 EU 430 Boiler #2 6/7/2005 Sample #1 ICR Phase I PM and Metals #2 Boiler 

2005 5.6 9585

MN Boise Paper 1212 Boiler #2 6/2005 (PM10) 2 MNBoisePaper1212 EU 430 Boiler #2 6/7/2005 Sample #2 ICR Phase I PM and Metals #2 Boiler 

2005 5.4 9585

MN Boise Paper 1212 Boiler #2 6/2005 (PM10) 3 MNBoisePaper1212 EU 430 Boiler #2 6/7/2005 Sample #3 ICR Phase I PM and Metals #2 Boiler 

2005 6.8 9585

GA GP Madison Ply (10/2004) solid/biomass 1 GAGPMadisonPly 800 Wood Waste Boiler 10/14/2004 Sample #1 ICR Phase II - 

Comments

Additional PM from 

Comments - 2004

8.82 9280

GA GP Madison Ply (10/2004) solid/biomass 2 GAGPMadisonPly 800 Wood Waste Boiler 10/14/2004 Sample #2 ICR Phase II - 

Comments

Additional PM from 

Comments - 2004

8.76 9280

GA GP Madison Ply (10/2004) solid/biomass 3 GAGPMadisonPly 800 Wood Waste Boiler 10/14/2004 Sample #3 ICR Phase II - 

Comments

Additional PM from 

Comments - 2004

9.06 9280

From Sheet A-1 From Database
Appendix A-2 - Calculations for PM Data Revisions

Facility/Unit Category/ sub-category Run ID FacilityID Unit ID Test Date Run ID Data Source Source Tab Oxygen% F-Factor

From Sheet A-1 From Database

WA Weyerhaeuser Raymond 

(11/2004) Solid/Biomass 3 WAWeyerhaeuser_Raymond Hog Fuel Boiler EU1 11/10/2004 Sample #3 ICR Phase I PM and Metals 8.7 11300

TN Eastman NO CBI DATA Solid/Coal (11/8/1994) 1 TNEastman_NO_CBIDATA Boiler 30 11/8/1994 Sample #1 ICR Phase I PM and Metals (UDBlr30) (2)11.6 1800

TN Eastman NO CBI DATA Solid/Coal (11/8/1994) 2 TNEastman_NO_CBIDATA Boiler 30 11/8/1994 Sample #2 ICR Phase I PM and Metals (UDBlr30) (2)12.6 1800

TN Eastman NO CBI DATA Solid/Coal (11/8/1994) 4 TNEastman_NO_CBIDATA Boiler 30 11/8/1994 Sample #3 ICR Phase I PM and Metals (UDBlr30) (2)11.8 1800

MN Andersen Corp Bayport Boiler 11 Solid/Biomass (wood 

fuel) 4/2008 1 MNAndersonCorpBayport Boiler 11 EU620 4/22/2008 Sample #1 ICR Phase I PM and Metals

MN Andersen Corp Bayport Boiler 11 Solid/Biomass (wood 

fuel) 4/2008 2 MNAndersonCorpBayport Boiler 11 EU620 4/22/2008 Sample #2 ICR Phase I PM and Metals

MN Andersen Corp Bayport Boiler 11 Solid/Biomass (wood 

fuel) 4/2008 3 MNAndersonCorpBayport Boiler 11 EU620 4/22/2008 Sample #3 ICR Phase I PM and Metals

MN Andersen Corp Bayport Boiler 12 Solid/Biomass (wood 

fuel) 4/2008 1 MNAndersonCorpBayport Boiler 12 EU621 4/22/2008 Sample #1 ICR Phase I PM and Metals (5)

MN Andersen Corp Bayport Boiler 12 Solid/Biomass (wood 

fuel) 4/2008 2 MNAndersonCorpBayport Boiler 12 EU621 4/22/2008 Sample #2 ICR Phase I PM and Metals (5)

MN Andersen Corp Bayport Boiler 12 Solid/Biomass (wood 

fuel) 4/2008 3 MNAndersonCorpBayport Boiler 12 EU621 4/22/2008 Sample #3 ICR Phase I PM and Metals (5)
Appendix A-2 - Calculations for PM Data Revisions

Facility/Unit

WIGreenBayPackagingMillDivi

sion

IA Iowa State University B2

IA Iowa State University B2

ME Boralex Stratton Boiler 1 

(10/2009)

VA University of Virginia 7103-

1-01R (12/2007)

VA University of Virginia 7103-

1-01R (12/2007)

WI Domtar 2814

GA GP Madison Ply (8/2009)

WI Wausau

WI Wausau

ID Tasco Nampa

ID Tasco Nampa

ID Tasco Nampa

MN Boise Paper 1212

MN Boise Paper 1212

MN Boise Paper 1212

GA GP Madison Ply (10/2004)

GA GP Madison Ply (10/2004)

GA GP Madison Ply (10/2004)

From Sheet A-1

Fuel 1

Sample 

volume 

(dscf)

Mass - 

Filter (mg)

Mass - 

Rinse (mg)

Re-calculated 

Based on zero 

filter for negative 

values

Revised 

Catch based 

on 64 FR 

53028

Mass Total 

(mg)

Reported 

Mass/Unit 

(lbs/mmbtu)

Reported Total 

Mass (based on 

negative filter 

weight)

Revised 

lb/mmBtu value 

using site 

specific factor

Coal-100% bituminous 84.67 0 0.1 1 1 0.007 5.23E-04

Coal-100% bituminous 35.40 0.3 0.3 1 1 0 1.00E-03

Coal-100% bituminous 35.29 0.4 0.1 1 1 0 1.00E-03

Wet biomass-100% Wood: 

Bark/Wood: Unadulterated 

Timber

20.20 n/a n/a 1 1 0.001 1.50E-03

Coal-100% bituminous 35.36 0.3 0.2 1 1 0.0005 9.18E-04

Coal-100% bituminous 33.44 0.1 0.3 1 1 0.0004 9.67E-04

Wet biomass-100% /Wood: 

Unadulterated Timber/ 37.13 0.7 <1.06 ? 1.76 2.8 2.59E-03

Wet biomass-82%; Dry 

biomass 18% (Wood: 

Bark/Wood: Plywood, 

Particleboard (containing 

glues or resins)/Wood: 

Unadulterated Lumber)

154.06 0 0.1 1 1 2.26E-04

Bituminous coal 35.90 <0.3 <1.06 ? 1.36 0.000835 1.72E-03

Bituminous coal 36.84 <0.3 1.6 ? 1.9 0.00125 2.39E-03

Coal-100% subbituminous 31.12 1.5 4.4 ? 5.9 1.09 5.85E-03

Coal-100% subbituminous 29.29 1.1 3.9 5 5.30E-03

Coal-100% subbituminous 31.51 1 3.8 4.8 4.73E-03

Wet biomass-87.6%; Heavy 

liquid-12.04% (Industrial 

Sludge - Primary/Industrial 

Sludge - Secondary/Natural 

gas/Wood: Bark)

36.19 -5.8 6.4 6.4 6.4 5.10E-03

Wet biomass-87.6%; Heavy 

liquid-12.04% (Industrial 

Sludge - Primary/Industrial 

Sludge - Secondary/Natural 

gas/Wood: Bark)

35.06 -1.3 3.3 3.3 3.3 2.68E-03

Wet biomass-87.6%; Heavy 

liquid-12.04% (Industrial 

Sludge - Primary/Industrial 

Sludge - Secondary/Natural 

gas/Wood: Bark)

34.46 -2.5 5.8 5.8 5.8 5.27E-03

Wet biomass-100% Bark 40.38 -0.5 3.1 3.1 3.1 0.002 2.72E-03

Wet biomass-100% Bark 39.91 -0.1 3.8 3.8 3.8 0.003 3.35E-03

Wet biomass-100% Bark 40.78 -0.4 2.3 2.3 2.3 0.002 2.04E-03
Appendix A-2 - Calculations for PM Data Revisions

Facility/Unit

From Sheet A-1

WA Weyerhaeuser Raymond 

(11/2004)

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

Fuel 1

Sample 

volume 

(dscf)

Mass - 

Filter (mg)

Mass - 

Rinse (mg)

Re-calculated 

Based on zero 

filter for negative 

values

Revised 

Catch based 

on 64 FR 

53028

Mass Total 

(mg)

Reported 

Mass/Unit 

(lbs/mmbtu)

Reported Total 

Mass (based on 

negative filter 

weight)

Revised 

lb/mmBtu value 

using site 

specific factor

Dry Biomass-100% hog fuel 41.58 0 0.6 1 1 0.004 1.03E-03

Coal: Bituminous 50.29 1.3 15.9 16.4 1.12E-02

Coal: Bituminous 50.90 3.2 11.2 13.6 8.41E-03

Coal: Bituminous 47.57 2.8 10.8 12.8 9.05E-03

/Natural gas/Wood: 

Unadulterated Lumber/ 42.89 -2.5 5.7 5.7 5.7 0.002 3.2 3.56E-03

/Natural gas/Wood: 

Unadulterated Lumber/ 43.14 -2.8 3.6 3.6 3.6 0.001 0.8 4.50E-03

/Natural gas/Wood: 

Unadulterated Lumber/ 42.44 -1.2 3.3 3.3 3.3 0.002 2.1 3.14E-03

/Natural gas/Wood: 

Unadulterated Lumber/ 39.95 -4.5 5.3 5.3 5.3 0.006 0.8 3.98E-02

/Natural gas/Wood: 

Unadulterated Lumber/ 39.63 -3.3 4.3 4.3 4.3 0.008 1 3.44E-02

/Natural gas/Wood: 

Unadulterated Lumber/ 39.04 -1.8 2.3 2.3 2.3 0.004 0.5 1.84E-02
Appendix A-2 - Calculations for PM Data Revisions

Facility/Unit

WIGreenBayPackagingMillDivi

sion

IA Iowa State University B2

IA Iowa State University B2

ME Boralex Stratton Boiler 1 

(10/2009)

VA University of Virginia 7103-

1-01R (12/2007)

VA University of Virginia 7103-

1-01R (12/2007)

WI Domtar 2814

GA GP Madison Ply (8/2009)

WI Wausau

WI Wausau

ID Tasco Nampa

ID Tasco Nampa

ID Tasco Nampa

MN Boise Paper 1212

MN Boise Paper 1212

MN Boise Paper 1212

GA GP Madison Ply (10/2004)

GA GP Madison Ply (10/2004)

GA GP Madison Ply (10/2004)

From Sheet A-1

Notes:

Removing this entire test, broken vacuum 

suspected and no final leak detection in report. 

Run 2 much lower than other two runs (1 and 3).

No information regarding analytical rinse. Data 

was only seperated between filterable and 

condensable.

discrepancy between field data sheet and results 

page

Subtracted a negative filter weight from the 

Acetone Wash values.

Subtracted a negative filter weight from the 

Acetone Wash values.

Subtracted a negative filter weight from the 

Acetone Wash values.
Appendix A-2 - Calculations for PM Data Revisions

Facility/Unit

From Sheet A-1

WA Weyerhaeuser Raymond 

(11/2004)

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

TN Eastman NO CBI DATA

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

MN Andersen Corp Bayport

Notes:

lb/MMBtu includes condesnable. Run 3 does not 

have supporting material in the report? Total 

mass <1 mg. Did a back calc using gr/dscf 

number.

adjusted as report subtracted too much for 

blank, added 2.8mg.

adjusted as report subtracted too much for 

blank, added 3mg.

adjusted as report subtracted too much for 

blank, added 3mg.

Corrected lb/mmBtu based on a ratio of catches

Corrected lb/mmBtu based on a ratio of catches

Corrected lb/mmBtu based on a ratio of catches

Corrected lb/mmBtu based on a ratio of catches

Corrected lb/mmBtu based on a ratio of catches

Corrected lb/mmBtu based on a ratio of catches