This spreadsheet is adapted from the Sargent and Lundy cost algorithms documentation for a 

DSI installation, as incorporated in version 5.13 of the IPM model. The "Source" tab lists the 

origination of these cost algorithms and other information used in this spreadsheet. The 

facilities tabs (i.e., BB 1) replicates the cost algorithms present in the documentation. In 

addition, the facilities tabs annualize the costs and calculate a $/ton figure. Emissions data 

are included in the remaining tabs as an aid in choosing some input values.

User must have "show objects" selected in Excel's options for the drop down menus to work:
IPM Model – Updates to Cost and Performance for APC Technologies, Dry Sorbent Injection for 

SO2 Control Cost Development Methodology, Final March 2013, Project 12847-002, Systems 

Research and Applications Corporation, Prepared by Sargent and Lundy. 

Documentation for v.5.13: Chapter 5: Emission Control Technologies, Attachment 5-5: DSI Cost 

Methodology, downloaded from http://www.epa.gov/airmarkets/progsregs/epaipm/docs/v513/attachment5_5.pdf on 12-18-13

Emissions data were downloaded from EPA CAMD's website: http://ampd.epa.gov/ampd/
Facility Unit

DSI 

Control 

(%)

DSI SO2 

Reduction 

(tpy)

DSI Capital 

Cost

DSI 

Annualized 

Capital Cost

DSI Variable 

Operating 

Cost

DSI Fixed 

Operating 

Cost

DSI Total 

Annualized 

Cost

Big Brown 1 50.00 15,334 $19,096,000 $1,538,878 $32,128,615 $419,378 $34,086,871

90.00 27,600 $33,357,000 $2,688,121 $79,452,946 $543,175 $82,684,241

2 50.00 15,407 $19,035,000 $1,533,962 $31,959,458 $416,402 $33,909,822

90.00 27,733 $32,965,000 $2,656,531 $78,456,412 $536,643 $81,649,586

Coleto Creek 1 50.00 8,030 $15,888,000 $1,280,357 $20,731,452 $404,410 $22,416,218

90.00 14,453 $21,863,000 $1,761,861 $47,781,846 $457,979 $50,001,685

Monticello 1 50.00 8,933 $17,137,000 $1,381,009 $22,609,610 $374,199 $24,364,819

90.00 16,079 $23,580,000 $1,900,227 $52,664,972 $426,218 $54,991,417

2 50.00 8,215 $17,057,000 $1,374,562 $23,585,904 $390,904 $25,351,370

90.00 14,786 $23,468,000 $1,891,202 $54,514,200 $445,087 $56,850,489

Tolk 171B 50.00 5,016 $13,938,000 $1,123,213 $13,968,324 $374,040 $15,465,578

90.00 9,028 $19,179,000 $1,545,567 $30,461,398 $419,465 $32,426,429

172B 50.00 5,517 $13,873,000 $1,117,975 $14,115,709 $366,470 $15,600,155

90.00 9,931 $19,090,000 $1,538,394 $30,036,649 $410,837 $31,985,880

W A Parish WAP5 50.00 7,079 $15,227,000 $1,227,089 $16,546,703 $338,198 $18,111,990

90.00 12,741 $20,953,000 $1,688,527 $36,091,083 $381,772 $38,161,382

WAP6 50.00 7,654 $15,934,000 $1,284,064 $19,027,337 $349,036 $20,660,436

90.00 13,776 $21,924,000 $1,766,776 $42,315,954 $395,356 $44,478,086

WAP7 50.00 6,168 $14,641,000 $1,179,866 $15,752,870 $368,792 $17,301,527

90.00 11,102 $20,145,000 $1,623,413 $34,555,902 $415,087 $36,594,402

Welsh 1 50.00 4,042 $14,888,000 $1,199,770 $13,501,650 $325,118 $15,026,538

80.00 6,467 $18,901,000 $1,523,164 $24,115,114 $354,687 $25,992,966

2 50.00 4,128 $14,775,000 $1,190,664 $13,390,807 $325,342 $14,906,814

80.00 6,605 $18,758,000 $1,511,640 $23,755,748 $354,778 $25,622,166

3 50.00 4,305 $15,023,000 $1,210,650 $14,337,927 $336,087 $15,884,663

80.00 6,887 $19,071,000 $1,536,863 $25,628,127 $366,841 $27,531,831
DSI Cost 

Effectiveness 

($/ton)

$2,223

$2,996

$2,201

$2,944

$2,792

$3,460

$2,728

$3,420

$3,086

$3,845

$3,084

$3,592

$2,828

$3,221

$2,559

$2,995

$2,699

$3,229

$2,805

$3,296

$3,718

$4,019

$3,611

$3,879

$3,690

$3,998
 Facility Name Facility 

ID 

(ORISPL)

 Unit ID Year SO2 

(tons)

SO2 avg. 

(tons)

SO2 max 2009-

2012 (tons)

SO2 avg. 

2009-2012 

excluding 

Max and 

Min (tons)

Big Brown 3497 1 2009 28,929

Big Brown 3497 1 2010 31,131

Big Brown 3497 1 2011 30,070

Big Brown 3497 1 2012 32,100

Big Brown 3497 1 2013 30,801 30,606 32,100 30,667

Big Brown 3497 2 2009 26,619

Big Brown 3497 2 2010 32,169

Big Brown 3497 2 2011 34,127

Big Brown 3497 2 2012 28,581

Big Brown 3497 2 2013 31,693 30,638 34,127 30,814

Coleto Creek 6178 1 2009 21,453

Coleto Creek 6178 1 2010 17,616

Coleto Creek 6178 1 2011 13,694

Coleto Creek 6178 1 2012 16,218

Coleto Creek 6178 1 2013 14,344 16,665 21,453 16,059

Harrington Station 6193 061B 2009 6,941

Harrington Station 6193 061B 2010 6,327

Harrington Station 6193 061B 2011 5,006

Harrington Station 6193 061B 2012 4,791

Harrington Station 6193 061B 2013 4,310 5,475 6,941 5,375

Harrington Station 6193 062B 2009 8,203

Harrington Station 6193 062B 2010 5,565

Harrington Station 6193 062B 2011 4,557

Harrington Station 6193 062B 2012 6,034

Harrington Station 6193 062B 2013 5,010 5,874 8,203 5,536

Harrington Station 6193 063B 2009 7,006

Harrington Station 6193 063B 2010 8,424

Harrington Station 6193 063B 2011 5,542

Harrington Station 6193 063B 2012 4,559

Harrington Station 6193 063B 2013 4,989 6,104 8,424 5,846

J T Deely 6181 1 2009 8,419

J T Deely 6181 1 2010 9,671

J T Deely 6181 1 2011 11,010

J T Deely 6181 1 2012 3,661

J T Deely 6181 1 2013 5,973 7,747 11,010 8,021

J T Deely 6181 2 2009 8,624

J T Deely 6181 2 2010 11,539

J T Deely 6181 2 2011 9,670

J T Deely 6181 2 2012 5,352
J T Deely 6181

2 2013 5,540 8,145 11,539 7,945

Monticello 61471 2009 20,509

Monticello 61471 2010 19,160

Monticello 61471 2011 21,897

Monticello 61471 2012 13,925

Monticello 61471 2013 6,683 16,435 21,897 17,865

Monticello 61472 2009 20,930

Monticello 61472 2010 19,872

Monticello 61472 2011 18,436

Monticello 61472 2012 10,980

Monticello 61472 2013 7,072 15,458 20,930 16,429

Tolk Station 6194 171B 2009 10,681

Tolk Station 6194 171B 2010 12,412

Tolk Station 6194 171B 2011 10,546

Tolk Station 6194 171B 2012 8,613

Tolk Station 6194 171B 2013 8,868 10,224 12,412 10,031

Tolk Station 6194 172B 2009 11,960

Tolk Station 6194 172B 2010 12,062

Tolk Station 6194 172B 2011 9,285

Tolk Station 6194 172B 2012 10,555

Tolk Station 6194 172B 2013 10,586 10,889 12,062 11,034

W A Parish 3470 WAP5 2009 14,145

W A Parish 3470 WAP5 2010 16,232

W A Parish 3470 WAP5 2011 14,992

W A Parish 3470 WAP5 2012 12,774

W A Parish 3470 WAP5 2013 13,335 14,296 16,232 14,157

W A Parish 3470 WAP6 2009 13,206

W A Parish 3470 WAP6 2010 17,149

W A Parish 3470 WAP6 2011 18,267

W A Parish 3470 WAP6 2012 12,695

W A Parish 3470 WAP6 2013 15,565 15,376 18,267 15,307

W A Parish 3470 WAP7 2009 12,492

W A Parish 3470 WAP7 2010 13,200

W A Parish 3470 WAP7 2011 13,147

W A Parish 3470 WAP7 2012 10,391

W A Parish 3470 WAP7 2013 11,365 12,119 13,200 12,335

Welsh Power Plant 61391 2009 9,061

Welsh Power Plant 61391 2010 8,361

Welsh Power Plant 61391 2011 8,401

Welsh Power Plant 61391 2012 7,491

Welsh Power Plant 61391 2013 6,469 7,956 9,061 8,084

Welsh Power Plant 61392 2009 9,453

Welsh Power Plant 61392 2010 8,792

Welsh Power Plant 61392 2011 8,386
Welsh Power Plant 6139

2 2012 7,588

Welsh Power Plant 61392 2013 6,159 8,076 9,453 8,256

Welsh Power Plant 61393 2009 8,858

Welsh Power Plant 61393 2010 9,534

Welsh Power Plant 61393 2011 8,836

Welsh Power Plant 61393 2012 8,133

Welsh Power Plant 61393 2013 7,092 8,491 9,534 8,609
 Avg. 

NOx 

Rate 

(lb/MMB

tu)

 NOx 

(tons)

 Heat Input 

(MMBtu) Operating 

Time

 # of 

Months 

Reported

 Gross Load 

(MW-h)

 Gross Load 

avg. (MW-h)

 Gross Load 

Max 2009-

2012 (MWh)

0.136 2,941 42,834,120 8,188 12 4,346,661

0.1376 3,280 47,304,348 8,510 12 4,940,573

0.1401 2,754 39,607,495 7,924 12 4,082,531

0.1317 2,615 39,552,327 7,965 12 4,109,169

0.1318 2,863 43,543,406 8,163 12 4,437,808 4,383,348 4,940,573

0.1462 2,836 38,692,298 7,472 12 3,891,986

0.1437 3,473 48,238,106 8,368 12 4,921,894

0.1369 3,040 44,608,809 8,359 12 4,374,884

0.1303 2,429 36,596,309 7,346 12 3,674,361

0.1313 2,900 43,627,457 8,278 12 4,467,086 4,266,042 4,921,894

0.163 4,198 51,330,220 8,563 12 5,510,671

0.1485 3,234 43,496,800 7,249 12 4,687,042

0.1288 2,634 40,787,319 6,583 12 4,287,147

0.1274 3,367 52,727,119 8,707 12 5,618,820

0.1307 3,043 46,405,593 7,682 12 4,920,047 5,004,745 5,618,820

0.2589 3,360 25,196,015 8,353 12 2,633,831

0.2754 2,931 20,732,792 7,259 12 2,198,645

0.1641 1,587 19,310,303 7,296 12 2,182,413

0.1553 1,582 20,255,382 7,213 12 2,138,638

0.1471 1,374 18,471,939 6,513 12 1,790,174 2,188,740 2,633,831

0.1529 2,124 28,161,630 8,676 12 2,840,102

0.1545 1,609 19,849,928 7,002 12 2,015,934

0.1711 1,632 19,237,596 6,262 12 1,892,016

0.1577 2,091 26,262,270 7,784 12 2,418,813

0.1549 1,674 21,728,375 7,178 12 1,990,086 2,231,390 2,840,102

0.1566 2,041 25,866,341 7,585 12 2,435,752

0.157 2,171 27,548,347 8,709 12 2,800,894

0.1675 1,628 19,260,192 6,721 12 2,075,614

0.1579 1,543 19,914,016 6,595 12 2,045,828

0.1703 1,842 22,423,185 7,670 12 2,159,069 2,303,432 2,800,894

0.142 1,794 25,213,105 6,708 12 2,442,692

0.1372 1,945 28,292,203 7,049 12 2,626,845

0.1085 1,839 33,745,164 8,485 12 3,461,641

0.0889 641 14,998,743 4,956 12 1,465,888

0.0872 1,128 25,892,398 6,708 12 2,515,541 2,502,521 3,461,641

0.1441 1,863 25,754,618 6,533 12 2,414,722

0.1382 2,355 33,970,515 8,516 12 3,184,004

0.1068 1,581 29,761,382 7,877 12 3,091,197

0.0726 758 22,421,134 8,192 12 2,307,680
0.0655 782 24,169,385 6,459 12 2,296,076 2,658,736 3,184,004

0.1406 3,200 45,575,619 8,388 12 4,523,648

0.1294 2,608 40,192,358 7,625 12 3,943,992

0.1273 2,695 42,997,611 8,386 12 4,204,096

0.1462 1,785 25,523,453 6,402 12 2,499,516

0.1285 930 14,441,879 2,804 12 1,402,219 3,314,694 4,523,648

0.1429 3,360 46,997,564 8,481 12 4,733,924

0.1315 2,812 42,634,585 8,424 12 4,323,536

0.1236 2,259 36,536,176 7,332 12 3,681,866

0.1244 1,306 20,863,170 4,969 12 2,037,435

0.1191 944 15,991,210 3,052 12 1,495,864 3,254,525 4,733,924

0.1942 3,332 33,875,149 7,462 12 3,711,397

0.1958 3,932 39,861,511 8,107 12 4,106,866

0.1971 3,916 39,534,830 8,669 12 4,598,970

0.1368 2,265 32,905,257 7,312 12 3,708,139

0.1308 2,425 36,830,341 8,059 12 4,137,347 4,052,544 4,598,970

0.1877 3,832 40,247,195 8,153 12 3,875,990

0.1756 3,603 40,513,042 8,042 12 4,023,326

0.1756 3,066 34,453,687 6,899 12 3,593,513

0.17 3,505 40,958,516 8,225 12 4,258,695

0.1572 3,417 43,394,897 8,743 12 4,596,449 4,069,594 4,596,449

0.0534 1,237 47,411,660 7,876 12 4,838,372

0.0519 1,230 47,829,753 8,568 12 4,804,743

0.049 1,048 43,129,418 7,687 12 4,449,991

0.0566 1,133 40,372,000 7,821 12 4,190,580

0.0687 1,421 41,668,238 8,381 12 4,496,507 4,556,039 4,838,372

0.0671 1,420 42,750,002 7,791 12 4,755,285

0.0511 1,154 45,639,410 8,493 12 4,730,968

0.0598 1,529 51,493,589 8,348 12 4,900,695

0.0475 945 40,434,487 7,003 12 3,792,960

0.0491 1,152 47,600,640 7,982 12 4,420,351 4,520,052 4,900,695

0.041 827 40,995,118 8,456 12 4,682,905

0.0543 993 36,564,428 7,996 12 4,294,370

0.0448 824 37,025,152 8,021 12 4,056,673

0.0424 648 30,705,810 7,006 12 3,221,631

0.0407 668 33,198,984 6,527 12 3,438,879 3,938,892 4,682,905

0.1827 3,475 37,607,897 7,898 12 3,753,300

0.1916 3,510 35,991,931 7,543 12 3,574,985

0.1929 3,730 38,381,651 7,953 12 3,827,597

0.1891 3,395 35,325,234 7,749 12 3,585,978

0.1793 2,771 30,115,547 7,588 12 3,093,867 3,567,145 3,827,597

0.1732 3,364 38,654,634 7,854 12 3,794,707

0.1709 3,334 38,826,022 7,909 12 3,827,532

0.1753 3,327 37,720,669 7,841 12 3,727,289
0.1663 3,015 35,568,873 7,493 12 3,480,946

0.1618 2,376 28,774,803 7,744 12 2,848,458 3,535,786 3,827,532

0.1837 3,307 35,673,601 7,554 12 3,581,040

0.1919 3,975 40,992,923 8,027 12 3,931,843

0.2061 4,039 38,998,372 7,836 12 3,855,378

0.1915 3,664 37,695,636 7,902 12 3,708,048

0.1847 3,110 33,029,365 7,925 12 3,286,816 3,672,625 3,931,843
 Gross Load 

avg. 2009-

2012 

excluding 

Max and 

Min (MW-h)

Gross 

Heat Rate 

(Btu/kWh)

Gross 

Heat Rate 

2009-

2012 Max 

(Btu/kWh)

Gross Heat 

Rate 2009-

2012 Avg. 

(Btu/kWh)

Gross Heat 

Rate avg. 

2009-2012 

excluding 

Max and 

Min (tons)

 County Facility 

Latitude

 Facility 

Longitud

e

 Owner

9,854 Freestone 31.8206 -96.056 Big Brown Power Com

9,575 Freestone 31.8206 -96.056 Big Brown Power Com

9,702 Freestone 31.8206 -96.056 Big Brown Power Com

9,625 Freestone 31.8206 -96.056 Big Brown Power Com

4,297,880 9,812 9,854 9,714 9,713 Freestone 31.8206 -96.056 Big Brown Power Com

9,942 Freestone 31.8206 -96.056 Big Brown Power Com

9,801 Freestone 31.8206 -96.056 Big Brown Power Com

10,197 Freestone 31.8206 -96.056 Big Brown Power Com

9,960 Freestone 31.8206 -96.056 Big Brown Power Com

4,244,652 9,766 10,197 9,933 9,901 Freestone 31.8206 -96.056 Big Brown Power Com

9,315 Goliad 28.7128 -97.214 Coleto Creek Power, L

9,280 Goliad 28.7128 -97.214 Coleto Creek Power, L

9,514 Goliad 28.7128 -97.214 Coleto Creek Power, L

9,384 Goliad 28.7128 -97.214 Coleto Creek Power, L

5,039,253 9,432 9,514 9,385 9,377 Goliad 28.7128 -97.214 Coleto Creek Power, L

9,566 Potter 35.2972 -101.75 Southwestern Public S

9,430 Potter 35.2972 -101.75 Southwestern Public S

8,848 Potter 35.2972 -101.75 Southwestern Public S

9,471 Potter 35.2972 -101.75 Southwestern Public S

2,173,232 10,319 10,319 9,527 9,489 Potter 35.2972 -101.75 Southwestern Public S

9,916 Potter 35.2972 -101.75 Southwestern Public S

9,847 Potter 35.2972 -101.75 Southwestern Public S

10,168 Potter 35.2972 -101.75 Southwestern Public S

10,858 Potter 35.2972 -101.75 Southwestern Public S

2,141,611 10,918 10,918 10,341 10,314 Potter 35.2972 -101.75 Southwestern Public S

10,619 Potter 35.2972 -101.75 Southwestern Public S

9,836 Potter 35.2972 -101.75 Southwestern Public S

9,279 Potter 35.2972 -101.75 Southwestern Public S

9,734 Potter 35.2972 -101.75 Southwestern Public S

2,223,479 10,386 10,619 9,971 9,985 Potter 35.2972 -101.75 Southwestern Public S

10,322 Bexar 29.3072 -98.323 City of San Antonio (O

10,770 Bexar 29.3072 -98.323 City of San Antonio (O

9,748 Bexar 29.3072 -98.323 City of San Antonio (O

10,232 Bexar 29.3072 -98.323 City of San Antonio (O

2,528,359 10,293 10,770 10,273 10,282 Bexar 29.3072 -98.323 City of San Antonio

10,666 Bexar 29.3072 -98.323 City of San Antonio (O

10,669 Bexar 29.3072 -98.323 City of San Antonio (O

9,628 Bexar 29.3072 -98.323 City of San Antonio (O

9,716 Bexar 29.3072 -98.323 City of San Antonio (O
2,604,533 10,526 10,669 10,241 10,303 Bexar 29.3072 -98.323 City of San Antonio

10,075 Titus 33.0917 -95.042 Luminant Generation C

10,191 Titus 33.0917 -95.042 Luminant Generation C

10,228 Titus 33.0917 -95.042 Luminant Generation C

10,211 Titus 33.0917 -95.042 Luminant Generation C

3,549,202 10,299 10,299 10,201 10,210 Titus 33.0917 -95.042 Luminant Generation C

9,928 Titus 33.0917 -95.042 Luminant Generation C

9,861 Titus 33.0917 -95.042 Luminant Generation C

9,923 Titus 33.0917 -95.042 Luminant Generation C

10,240 Titus 33.0917 -95.042 Luminant Generation C

3,347,612 10,690 10,690 10,128 10,030 Titus 33.0917 -95.042 Luminant Generation C

9,127 Lamb 34.1847 -102.57 Southwestern Public S

9,706 Lamb 34.1847 -102.57 Southwestern Public S

8,596 Lamb 34.1847 -102.57 Southwestern Public S

8,874 Lamb 34.1847 -102.57 Southwestern Public S

3,985,203 8,902 9,706 9,041 8,968 Lamb 34.1847 -102.57 Southwestern Public S

10,384 Lamb 34.1847 -102.57 Southwestern Public S

10,070 Lamb 34.1847 -102.57 Southwestern Public S

9,588 Lamb 34.1847 -102.57 Southwestern Public S

9,618 Lamb 34.1847 -102.57 Southwestern Public S

4,052,670 9,441 10,384 9,820 9,758 Lamb 34.1847 -102.57 Southwestern Public S

9,799 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

9,955 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

9,692 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

9,634 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

4,583,747 9,267 9,955 9,669 9,708 Fort Bend 29.4828 -95.631 NRG Energy, Inc

8,990 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

9,647 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

10,507 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

10,660 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

4,635,535 10,769 10,769 10,115 10,272 Fort Bend 29.4828 -95.631 NRG Energy, Inc

8,754 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

8,515 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

9,127 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

9,531 Fort Bend 29.4828 -95.631 NRG Energy, Inc (Own

3,929,974 9,654 9,654 9,116 9,137 Fort Bend 29.4828 -95.631 NRG Energy, Inc

10,020 Titus 33.0583 -94.844 Southwestern Electric 

10,068 Titus 33.0583 -94.844 Southwestern Electric 

10,028 Titus 33.0583 -94.844 Southwestern Electric 

9,851 Titus 33.0583 -94.844 Southwestern Electric 

3,638,088 9,734 10,068 9,940 9,966 Titus 33.0583 -94.844 Southwestern Electric 

10,186 Titus 33.0583 -94.844 Southwestern Electric 

10,144 Titus 33.0583 -94.844 Southwestern Electric 

10,120 Titus 33.0583 -94.844 Southwestern Electric 
10,218 Titus 33.0583 -94.844 Southwestern Electric 

3,667,647 10,102 10,218 10,154 10,150 Titus 33.0583 -94.844 Southwestern Electric 

9,962 Titus 33.0583 -94.844 Southwestern Electric 

10,426 Titus 33.0583 -94.844 Southwestern Electric 

10,115 Titus 33.0583 -94.844 Southwestern Electric 

10,166 Titus 33.0583 -94.844 Southwestern Electric 

3,714,822 10,049 10,426 10,144 10,110 Titus 33.0583 -94.844 Southwestern Electric 
Operator

 Fuel 

Type 

(Primary)

 Fuel 

Type 

(Seconda

ry)

 SO2 

Control(s

)

 NOx 

Control(s

)

 PM 

Control(s

)

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Coleto Creek Power, LP Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Coleto Creek Power, LP Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Coleto Creek Power, LP Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Coleto Creek Power, LP Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Coleto Creek Power, LP Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Southwestern Public Service Company Coal Overfire AirElectrostatic Precipitator

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Southwestern Public Service Company Coal Pipeline Natural GasLow NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Southwestern Public Service Company Coal Pipeline Natural GasLow NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Southwestern Public Service Company Coal Pipeline Natural GasLow NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Southwestern Public Service Company Coal Pipeline Natural GasLow NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Southwestern Public Service Company Coal Pipeline Natural GasLow NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

City of San Antonio Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

City of San Antonio Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

City of San Antonio Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

City of San Antonio Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

City of San Antonio Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

City of San Antonio Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

City of San Antonio Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

City of San Antonio Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

City of San Antonio Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse
City of San Antonio Coal Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Luminant Generation Company LLC Coal Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Southwestern Public Service Company Coal Overfire AirBaghouse

Southwestern Public Service Company Coal Overfire AirBaghouse

Southwestern Public Service Company Coal Overfire AirBaghouse

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Southwestern Public Service Company Coal Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Southwestern Public Service Company Coal Overfire AirBaghouse

Southwestern Public Service Company Coal Overfire AirBaghouse

Southwestern Public Service Company Coal Overfire AirBaghouse

Southwestern Public Service Company Coal Overfire AirBaghouse

Southwestern Public Service Company Coal Overfire AirBaghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

NRG Energy, Inc Coal Pipeline Natural GasSelective Catalytic Reduction Baghouse

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator
Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator

Southwestern Electric Power Company Coal Low NOx Burner Technology w/ Overfire Air Electrostatic Precipitator
 Facility Name

 Facility ID 

(ORISPL) Unit ID Year Month SO2 (tons)

 Avg. Monthly 

SO2 Rate 

(lb/MMBtu)

 2009-2012 

Max. Monthly 

SO2 Rate 

(lb/MMBtu)

Big Brown 3497 1 2009 1 2,799 1.32

Big Brown 3497 1 2009 2 2,315 1.27

Big Brown 3497 1 2009 3 2,458 1.29

Big Brown 3497 1 2009 4 1,678 1.22

Big Brown 3497 1 2009 5 1,821 1.35

Big Brown 3497 1 2009 6 2,809 1.44

Big Brown 3497 1 2009 7 2,423 1.26

Big Brown 3497 1 2009 8 2,496 1.48

Big Brown 3497 1 2009 9 2,559 1.35

Big Brown 3497 1 2009 10 2,502 1.46

Big Brown 3497 1 2009 11 2,597 1.46

Big Brown 3497 1 2009 12 2,473 1.31

Big Brown 3497 1 2010 1 2,458 1.23

Big Brown 3497 1 2010 2 2,520 1.28

Big Brown 3497 1 2010 3 2,045 1.31

Big Brown 3497 1 2010 4 2,308 1.24

Big Brown 3497 1 2010 5 2,654 1.34

Big Brown 3497 1 2010 6 2,722 1.33

Big Brown 3497 1 2010 7 2,996 1.39

Big Brown 3497 1 2010 8 2,978 1.40

Big Brown 3497 1 2010 9 2,852 1.43

Big Brown 3497 1 2010 10 2,711 1.39

Big Brown 3497 1 2010 11 2,381 1.23

Big Brown 3497 1 2010 12 2,508 1.22

Big Brown 3497 1 2011 1 2,049 1.07

Big Brown 3497 1 2011 2 1,924 1.09

Big Brown 3497 1 2011 3 2,337 1.38

Big Brown 3497 1 2011 4 63 1.39

Big Brown 3497 1 2011 5 2,418 1.44

Big Brown 3497 1 2011 6 2,690 1.41

Big Brown 3497 1 2011 7 2,962 1.44

Big Brown 3497 1 2011 8 2,872 1.59

Big Brown 3497 1 2011 9 3,542 1.80

Big Brown 3497 1 2011 10 3,765 2.00

Big Brown 3497 1 2011 11 3,027 1.90

Big Brown 3497 1 2011 12 2,421 1.64

Big Brown 3497 1 2012 1 1,381 1.54

Big Brown 3497 1 2012 2 2,821 1.93

Big Brown 3497 1 2012 3 2,810 1.68

Big Brown 3497 1 2012 4 2,983 1.68
Big Brown 3497

1 20125 2,398 1.57

Big Brown 34971 20126 2,672 1.58

Big Brown 34971 20127 2,883 1.52

Big Brown 34971 20128 2,778 1.45

Big Brown 34971 20129 2,866 1.55

Big Brown 34971 2012 10 3,424 1.65

Big Brown 34971 2012 11 1,910 1.63

Big Brown 34971 2012 12 3,174 1.71

Big Brown 34971 20131 2,633 1.60

Big Brown 34971 20132 2,599 1.50

Big Brown 34971 20133 3,065 1.47

Big Brown 34971 20134 2,007 1.39

Big Brown 34971 20135 2,428 1.45

Big Brown 34971 20136 2,309 1.35

Big Brown 34971 20137 3,067 1.50

Big Brown 34971 20138 2,783 1.38

Big Brown 34971 20139 2,112 1.27

Big Brown 34971 2013 10 2,671 1.43

Big Brown 34971 2013 11 2,426 1.33

Big Brown 34971 2013 12 2,700 1.31 2.00

Big Brown 34972 20091 2,468 1.33

Big Brown 34972 20092 2,090 1.26

Big Brown 34972 20093 1,664 1.29

Big Brown 34972 20094 2,074 1.22

Big Brown 34972 20095 N/A

Big Brown 34972 20096 1,724 1.41

Big Brown 34972 20097 2,596 1.30

Big Brown 34972 20098 2,963 1.54

Big Brown 34972 20099 2,612 1.42

Big Brown 34972 2009 10 2,833 1.47

Big Brown 34972 2009 11 2,834 1.51

Big Brown 34972 2009 12 2,761 1.35

Big Brown 34972 20101 2,398 1.22

Big Brown 34972 20102 2,625 1.27

Big Brown 34972 20103 2,811 1.28

Big Brown 34972 20104 2,707 1.25

Big Brown 34972 20105 2,770 1.35

Big Brown 34972 20106 2,940 1.38

Big Brown 34972 20107 3,017 1.46

Big Brown 34972 20108 3,232 1.45

Big Brown 34972 20109 2,893 1.40

Big Brown 34972 2010 10 1,880 1.43

Big Brown 34972 2010 11 2,264 1.27

Big Brown 34972 2010 12 2,634 1.27

Big Brown 34972 20111 2,229 1.06
Big Brown 3497

2 20112 1,791 1.06

Big Brown 34972 20113 2,654 1.41

Big Brown 34972 20114 2,630 1.40

Big Brown 34972 20115 3,145 1.54

Big Brown 34972 20116 2,745 1.48

Big Brown 34972 20117 3,148 1.51

Big Brown 34972 20118 3,448 1.73

Big Brown 34972 20119 3,877 1.87

Big Brown 34972 2011 10 2,627 1.91

Big Brown 34972 2011 11 3,186 1.88

Big Brown 34972 2011 12 2,648 1.62

Big Brown 34972 20121 2,652 1.79

Big Brown 34972 20122 1,242 1.63

Big Brown 34972 20123 2,955 1.59

Big Brown 34972 20124 2,817 1.56

Big Brown 34972 20125 2,988 1.68

Big Brown 34972 20126 2,624 1.51

Big Brown 34972 20127 2,646 1.36

Big Brown 34972 20128 2,695 1.38

Big Brown 34972 20129 2,961 1.58

Big Brown 34972 2012 10 1,135 1.69

Big Brown 34972 2012 11 1,096 1.56

Big Brown 34972 2012 12 2,771 1.61

Big Brown 34972 20131 2,899 1.53

Big Brown 34972 20132 2,305 1.55

Big Brown 34972 20133 2,678 1.43

Big Brown 34972 20134 2,748 1.42

Big Brown 34972 20135 2,814 1.51

Big Brown 34972 20136 2,297 1.42

Big Brown 34972 20137 3,115 1.56

Big Brown 34972 20138 2,826 1.43

Big Brown 34972 20139 2,914 1.49

Big Brown 34972 2013 10 2,667 1.42

Big Brown 34972 2013 11 1,728 1.32

Big Brown 34972 2013 12 2,702 1.32 1.91

Coleto Creek 61781 20091 1,744 0.78

Coleto Creek 61781 20092 1,831 0.88

Coleto Creek 61781 20093 1,922 0.92

Coleto Creek 61781 20094 1,937 0.89

Coleto Creek 61781 20095 1,867 0.82

Coleto Creek 61781 20096 1,840 0.82

Coleto Creek 61781 20097 1,533 0.80

Coleto Creek 61781 20098 1,725 0.81

Coleto Creek 61781 20099 1,721 0.82
Coleto Creek 6178

1 2009 10 1,812 0.81

Coleto Creek 61781 2009 11 1,874 0.90

Coleto Creek 61781 2009 12 1,648 0.78

Coleto Creek 61781 20101 1,890 0.83

Coleto Creek 61781 20102 1,312 0.79

Coleto Creek 61781 20103 N/A

Coleto Creek 61781 20104 316 0.71

Coleto Creek 61781 20105 1,685 0.87

Coleto Creek 61781 20106 1,735 0.76

Coleto Creek 61781 20107 1,954 0.83

Coleto Creek 61781 20108 1,839 0.86

Coleto Creek 61781 20109 1,769 0.79

Coleto Creek 61781 2010 10 1,916 0.84

Coleto Creek 61781 2010 11 1,737 0.79

Coleto Creek 61781 2010 12 1,462 0.75

Coleto Creek 61781 20111 1,685 0.73

Coleto Creek 61781 20112 1,251 0.61

Coleto Creek 61781 20113 1,375 0.66

Coleto Creek 61781 20114 1,417 0.69

Coleto Creek 61781 20115 1,423 0.69

Coleto Creek 61781 20116 1,493 0.65

Coleto Creek 61781 20117 1,613 0.66

Coleto Creek 61781 20118 1,722 0.73

Coleto Creek 61781 20119 1,454 0.66

Coleto Creek 61781 2011 10 N/A

Coleto Creek 61781 2011 11 N/A

Coleto Creek 61781 2011 12 262 0.54

Coleto Creek 61781 20121 1,400 0.63

Coleto Creek 61781 20122 1,299 0.62

Coleto Creek 61781 20123 1,476 0.66

Coleto Creek 61781 20124 1,186 0.60

Coleto Creek 61781 20125 1,431 0.64

Coleto Creek 61781 20126 1,222 0.59

Coleto Creek 61781 20127 1,380 0.62

Coleto Creek 61781 20128 1,380 0.60

Coleto Creek 61781 20129 1,570 0.71

Coleto Creek 61781 2012 10 1,344 0.59

Coleto Creek 61781 2012 11 1,257 0.57

Coleto Creek 61781 2012 12 1,274 0.56

Coleto Creek 61781 20131 1,043 0.58

Coleto Creek 61781 20132 1,193 0.60

Coleto Creek 61781 20133 1,382 0.63

Coleto Creek 61781 20134 1,099 0.59

Coleto Creek 61781 20135 911 0.56
Coleto Creek 6178

1 20136 1,457 0.67

Coleto Creek 61781 20137 1,319 0.56

Coleto Creek 61781 20138 1,641 0.71

Coleto Creek 61781 20139 1,469 0.65

Coleto Creek 61781 2013 10 1,081 0.59

Coleto Creek 61781 2013 11 367 0.59

Coleto Creek 61781 2013 12 1,381 0.63 0.92

Harrington Station 6193 061B 20091 506 0.47

Harrington Station 6193 061B 20092 587 0.52

Harrington Station 6193 061B 20093 487 0.45

Harrington Station 6193 061B 20094 428 0.63

Harrington Station 6193 061B 20095 593 0.57

Harrington Station 6193 061B 20096 584 0.58

Harrington Station 6193 061B 20097 549 0.56

Harrington Station 6193 061B 20098 689 0.57

Harrington Station 6193 061B 20099 673 0.59

Harrington Station 6193 061B 2009 10 651 0.58

Harrington Station 6193 061B 2009 11 580 0.55

Harrington Station 6193 061B 2009 12 615 0.57

Harrington Station 6193 061B 20101 533 0.61

Harrington Station 6193 061B 20102 456 0.65

Harrington Station 6193 061B 20103 654 0.61

Harrington Station 6193 061B 20104 506 0.59

Harrington Station 6193 061B 20105 618 0.60

Harrington Station 6193 061B 20106 671 0.63

Harrington Station 6193 061B 20107 647 0.62

Harrington Station 6193 061B 20108 638 0.58

Harrington Station 6193 061B 20109 87 0.54

Harrington Station 6193 061B 2010 10 355 0.69

Harrington Station 6193 061B 2010 11 630 0.72

Harrington Station 6193 061B 2010 12 531 0.49

Harrington Station 6193 061B 20111 567 0.61

Harrington Station 6193 061B 20112 375 0.55

Harrington Station 6193 061B 20113 346 0.44

Harrington Station 6193 061B 20114 560 0.55

Harrington Station 6193 061B 20115 476 0.52

Harrington Station 6193 061B 20116 542 0.53

Harrington Station 6193 061B 20117 587 0.50

Harrington Station 6193 061B 20118 646 0.55

Harrington Station 6193 061B 20119 458 0.50

Harrington Station 6193 061B 2011 10 448 0.51

Harrington Station 6193 061B 2011 11 N/A

Harrington Station 6193 061B 2011 121 0.01

Harrington Station 6193 061B 20121 381 0.51
Harrington Station 6193 061B 2012

2 279 0.48

Harrington Station 6193 061B 20123 473 0.50

Harrington Station 6193 061B 20124 439 0.48

Harrington Station 6193 061B 20125 252 0.45

Harrington Station 6193 061B 20126 461 0.44

Harrington Station 6193 061B 20127 615 0.47

Harrington Station 6193 061B 20128 346 0.44

Harrington Station 6193 061B 20129 147 0.47

Harrington Station 6193 061B 2012 10 457 0.47

Harrington Station 6193 061B 2012 11 411 0.45

Harrington Station 6193 061B 2012 12 530 0.49

Harrington Station 6193 061B 20131 227 0.50

Harrington Station 6193 061B 20132 N/A

Harrington Station 6193 061B 20133 368 0.45

Harrington Station 6193 061B 20134 370 0.46

Harrington Station 6193 061B 20135 479 0.50

Harrington Station 6193 061B 20136 247 0.45

Harrington Station 6193 061B 20137 498 0.45

Harrington Station 6193 061B 20138 506 0.46

Harrington Station 6193 061B 20139 442 0.45

Harrington Station 6193 061B 2013 10 505 0.49

Harrington Station 6193 061B 2013 11 179 0.46

Harrington Station 6193 061B 2013 12 489 0.47 0.72

Harrington Station 6193 062B 20091 708 0.53

Harrington Station 6193 062B 20092 692 0.56

Harrington Station 6193 062B 20093 634 0.49

Harrington Station 6193 062B 20094 628 0.54

Harrington Station 6193 062B 20095 679 0.62

Harrington Station 6193 062B 20096 655 0.62

Harrington Station 6193 062B 20097 711 0.59

Harrington Station 6193 062B 20098 747 0.62

Harrington Station 6193 062B 20099 712 0.63

Harrington Station 6193 062B 2009 10 722 0.63

Harrington Station 6193 062B 2009 11 652 0.60

Harrington Station 6193 062B 2009 12 664 0.59

Harrington Station 6193 062B 20101 38 0.60

Harrington Station 6193 062B 201020 0.01

Harrington Station 6193 062B 20103 607 0.58

Harrington Station 6193 062B 20104 630 0.61

Harrington Station 6193 062B 20105 436 0.57

Harrington Station 6193 062B 20106 17 0.04

Harrington Station 6193 062B 20107 510 0.57

Harrington Station 6193 062B 20108 765 0.63

Harrington Station 6193 062B 20109 646 0.56
Harrington Station 6193 062B 2010 10 740 0.65

Harrington Station 6193 062B 2010 11 587 0.59

Harrington Station 6193 062B 2010 12 588 0.50

Harrington Station 6193 062B 20111 661 0.54

Harrington Station 6193 062B 20112 522 0.52

Harrington Station 6193 062B 20113 433 0.46

Harrington Station 6193 062B 20114 N/A

Harrington Station 6193 062B 20115 379 0.48

Harrington Station 6193 062B 20116 515 0.47

Harrington Station 6193 062B 20117 552 0.44

Harrington Station 6193 062B 20118 495 0.47

Harrington Station 6193 062B 20119 510 0.44

Harrington Station 6193 062B 2011 10 372 0.45

Harrington Station 6193 062B 2011 11 N/A

Harrington Station 6193 062B 2011 12 117 0.40

Harrington Station 6193 062B 20121 617 0.46

Harrington Station 6193 062B 20122 562 0.44

Harrington Station 6193 062B 20123 506 0.44

Harrington Station 6193 062B 20124 543 0.48

Harrington Station 6193 062B 20125 418 0.46

Harrington Station 6193 062B 20126 476 0.44

Harrington Station 6193 062B 20127 658 0.47

Harrington Station 6193 062B 20128 546 0.45

Harrington Station 6193 062B 20129 579 0.47

Harrington Station 6193 062B 2012 10 233 0.47

Harrington Station 6193 062B 2012 11 315 0.45

Harrington Station 6193 062B 2012 12 581 0.48

Harrington Station 6193 062B 20131 480 0.48

Harrington Station 6193 062B 20132 560 0.50

Harrington Station 6193 062B 20133 357 0.45

Harrington Station 6193 062B 20134 256 0.46

Harrington Station 6193 062B 20135 192 0.44

Harrington Station 6193 062B 20136 476 0.43

Harrington Station 6193 062B 20137 506 0.44

Harrington Station 6193 062B 20138 508 0.46

Harrington Station 6193 062B 20139 195 0.45

Harrington Station 6193 062B 2013 10 392 0.47

Harrington Station 6193 062B 2013 11 549 0.46

Harrington Station 6193 062B 2013 12 540 0.46 0.65

Harrington Station 6193 063B 20091 728 0.57

Harrington Station 6193 063B 20092 665 0.57

Harrington Station 6193 063B 20093 629 0.48

Harrington Station 6193 063B 20094 483 0.55

Harrington Station 6193 063B 20095 564 0.56
Harrington Station 6193 063B 2009

6 619 0.54

Harrington Station 6193 063B 20097 695 0.54

Harrington Station 6193 063B 20098 585 0.53

Harrington Station 6193 063B 20099 643 0.56

Harrington Station 6193 063B 2009 10 385 0.58

Harrington Station 6193 063B 2009 11 271 0.47

Harrington Station 6193 063B 2009 12 739 0.54

Harrington Station 6193 063B 20101 783 0.56

Harrington Station 6193 063B 20102 605 0.61

Harrington Station 6193 063B 20103 592 0.52

Harrington Station 6193 063B 20104 587 0.54

Harrington Station 6193 063B 20105 668 0.53

Harrington Station 6193 063B 20106 685 0.53

Harrington Station 6193 063B 20107 807 0.68

Harrington Station 6193 063B 20108 884 0.75

Harrington Station 6193 063B 20109 734 0.64

Harrington Station 6193 063B 2010 10 853 0.76

Harrington Station 6193 063B 2010 11 610 0.67

Harrington Station 6193 063B 2010 12 616 0.58

Harrington Station 6193 063B 20111 671 0.62

Harrington Station 6193 063B 20112 532 0.58

Harrington Station 6193 063B 20113 514 0.56

Harrington Station 6193 063B 20114 630 0.62

Harrington Station 6193 063B 20115 359 0.54

Harrington Station 6193 063B 20116 661 0.66

Harrington Station 6193 063B 20117 806 0.65

Harrington Station 6193 063B 20118 614 0.50

Harrington Station 6193 063B 20119 336 0.49

Harrington Station 6193 063B 2011 10 417 0.48

Harrington Station 6193 063B 2011 11 N/A

Harrington Station 6193 063B 2011 123 0.24

Harrington Station 6193 063B 20121 522 0.47

Harrington Station 6193 063B 20122 492 0.48

Harrington Station 6193 063B 20123 34 0.62

Harrington Station 6193 063B 20124 N/A

Harrington Station 6193 063B 20125 288 0.45

Harrington Station 6193 063B 20126 466 0.43

Harrington Station 6193 063B 20127 509 0.46

Harrington Station 6193 063B 20128 530 0.43

Harrington Station 6193 063B 20129 530 0.46

Harrington Station 6193 063B 2012 10 485 0.46

Harrington Station 6193 063B 2012 11 387 0.47

Harrington Station 6193 063B 2012 12 315 0.48

Harrington Station 6193 063B 20131 451 0.45
Harrington Station 6193 063B 2013

2 514 0.50

Harrington Station 6193 063B 20133 473 0.44

Harrington Station 6193 063B 20134 410 0.45

Harrington Station 6193 063B 20135 87 0.41

Harrington Station 6193 063B 20136 469 0.43

Harrington Station 6193 063B 20137 507 0.44

Harrington Station 6193 063B 20138 507 0.45

Harrington Station 6193 063B 20139 459 0.43

Harrington Station 6193 063B 2013 10 240 0.44

Harrington Station 6193 063B 2013 11 411 0.44

Harrington Station 6193 063B 2013 12 463 0.44 0.76

J T Deely 61811 20091 N/A

J T Deely 61811 200920 0.70

J T Deely 61811 20093 351 0.67

J T Deely 61811 20094 827 0.63

J T Deely 61811 20095 1,009 0.66

J T Deely 61811 20096 957 0.64

J T Deely 61811 20097 947 0.69

J T Deely 61811 20098 994 0.68

J T Deely 61811 20099 618 0.70

J T Deely 61811 2009 10 950 0.70

J T Deely 61811 2009 11 817 0.66

J T Deely 61811 2009 12 949 0.66

J T Deely 61811 20101 838 0.71

J T Deely 61811 201020 0.79

J T Deely 61811 20103 145 0.66

J T Deely 61811 20104 1,032 0.69

J T Deely 61811 20105 698 0.68

J T Deely 61811 20106 949 0.65

J T Deely 61811 20107 1,043 0.69

J T Deely 61811 20108 1,112 0.66

J T Deely 61811 20109 1,065 0.70

J T Deely 61811 2010 10 835 0.69

J T Deely 61811 2010 11 877 0.69

J T Deely 61811 2010 12 1,078 0.68

J T Deely 61811 20111 1,090 0.69

J T Deely 61811 20112 858 0.66

J T Deely 61811 20113 600 0.53

J T Deely 61811 20114 1,041 0.67

J T Deely 61811 20115 865 0.66

J T Deely 61811 20116 998 0.68

J T Deely 61811 20117 955 0.63

J T Deely 61811 20118 913 0.63

J T Deely 61811 20119 931 0.67
J T Deely 6181

1 2011 10 975 0.69

J T Deely 61811 2011 11 865 0.64

J T Deely 61811 2011 12 919 0.64

J T Deely 61811 20121 533 0.48

J T Deely 61811 20122 198 0.50

J T Deely 61811 20123 144 0.50

J T Deely 61811 20124 N/A

J T Deely 61811 20125 178 0.45

J T Deely 61811 20126 415 0.44

J T Deely 61811 20127 523 0.50

J T Deely 61811 20128 651 0.50

J T Deely 61811 20129 516 0.55

J T Deely 61811 2012 10 442 0.47

J T Deely 61811 2012 11 60 0.49

J T Deely 61811 2012 12 N/A

J T Deely 61811 20131 N/A

J T Deely 61811 20132 112 0.48

J T Deely 61811 20133 652 0.47

J T Deely 61811 20134 661 0.47

J T Deely 61811 20135 671 0.46

J T Deely 61811 20136 608 0.43

J T Deely 61811 20137 682 0.44

J T Deely 61811 20138 681 0.47

J T Deely 61811 20139 199 0.42

J T Deely 61811 2013 10 348 0.45

J T Deely 61811 2013 11 637 0.47

J T Deely 61811 2013 12 724 0.49 0.79

J T Deely 61812 20091 1,014 0.68

J T Deely 61812 20092 954 0.68

J T Deely 61812 20093 1,043 0.69

J T Deely 61812 20094 816 0.64

J T Deely 61812 20095 1,066 0.66

J T Deely 61812 20096 836 0.64

J T Deely 61812 20097 748 0.67

J T Deely 61812 20098 1,053 0.68

J T Deely 61812 20099 723 0.69

J T Deely 61812 2009 10 N/A

J T Deely 61812 2009 11 N/A

J T Deely 61812 2009 12 371 0.68

J T Deely 61812 20101 1,067 0.71

J T Deely 61812 20102 645 0.67

J T Deely 61812 20103 1,091 0.65

J T Deely 61812 20104 1,024 0.69

J T Deely 61812 20105 976 0.67
J T Deely 6181

2 20106 951 0.65

J T Deely 61812 20107 1,015 0.69

J T Deely 61812 20108 1,042 0.66

J T Deely 61812 20109 916 0.71

J T Deely 61812 2010 10 922 0.69

J T Deely 61812 2010 11 945 0.69

J T Deely 61812 2010 12 946 0.68

J T Deely 61812 20111 957 0.69

J T Deely 61812 20112 880 0.66

J T Deely 61812 20113 711 0.54

J T Deely 61812 20114 23 0.67

J T Deely 61812 20115 866 0.67

J T Deely 61812 20116 945 0.68

J T Deely 61812 20117 929 0.63

J T Deely 61812 20118 931 0.63

J T Deely 61812 20119 871 0.67

J T Deely 61812 2011 10 814 0.69

J T Deely 61812 2011 11 840 0.64

J T Deely 61812 2011 12 904 0.64

J T Deely 61812 20121 486 0.47

J T Deely 61812 20122 293 0.51

J T Deely 61812 20123 253 0.48

J T Deely 61812 20124 380 0.47

J T Deely 61812 20125 309 0.43

J T Deely 61812 20126 457 0.44

J T Deely 61812 20127 579 0.49

J T Deely 61812 20128 622 0.50

J T Deely 61812 20129 575 0.53

J T Deely 61812 2012 10 507 0.47

J T Deely 61812 2012 11 450 0.45

J T Deely 61812 2012 12 442 0.46

J T Deely 61812 20131 300 0.45

J T Deely 61812 20132 N/A

J T Deely 61812 20133 137 0.46

J T Deely 61812 20134 390 0.45

J T Deely 61812 20135 649 0.46

J T Deely 61812 20136 645 0.43

J T Deely 61812 20137 561 0.44

J T Deely 61812 20138 611 0.47

J T Deely 61812 20139 727 0.48

J T Deely 61812 2013 10 620 0.44

J T Deely 61812 2013 11 215 0.46

J T Deely 61812 2013 12 686 0.49 0.71

Monticello 61471 20091 2,026 1.01
Monticello 6147

1 20092 1,849 1.02

Monticello 61471 20093 1,825 1.01

Monticello 61471 20094 1,671 0.90

Monticello 61471 20095 1,194 0.80

Monticello 61471 20096 1,498 0.83

Monticello 61471 20097 1,888 0.89

Monticello 61471 20098 1,709 0.84

Monticello 61471 20099 1,746 0.86

Monticello 61471 2009 10 1,389 0.74

Monticello 61471 2009 11 1,767 0.90

Monticello 61471 2009 12 1,946 0.99

Monticello 61471 20101 1,365 0.96

Monticello 61471 20102 1,638 0.92

Monticello 61471 20103 1,688 0.93

Monticello 61471 20104 724 1.23

Monticello 61471 20105 660 0.91

Monticello 61471 20106 1,641 0.85

Monticello 61471 20107 1,810 0.89

Monticello 61471 20108 1,822 0.89

Monticello 61471 20109 1,771 0.95

Monticello 61471 2010 10 2,140 1.11

Monticello 61471 2010 11 1,879 1.01

Monticello 61471 2010 12 2,022 0.97

Monticello 61471 20111 1,956 0.93

Monticello 61471 20112 1,839 1.05

Monticello 61471 20113 1,545 1.11

Monticello 61471 20114 1,897 1.01

Monticello 61471 20115 1,917 0.97

Monticello 61471 20116 1,905 0.96

Monticello 61471 20117 2,095 1.01

Monticello 61471 20118 2,140 1.07

Monticello 61471 20119 1,837 1.00

Monticello 61471 2011 10 1,902 1.04

Monticello 61471 2011 11 1,687 1.06

Monticello 61471 2011 12 1,176 1.08

Monticello 61471 20121 1,006 1.06

Monticello 61471 20122 N/A

Monticello 61471 20123 334 1.15

Monticello 61471 20124 1,531 1.13

Monticello 61471 20125 1,909 1.33

Monticello 61471 20126 1,742 1.19

Monticello 61471 20127 1,559 1.07

Monticello 61471 20128 1,674 1.05

Monticello 61471 20129 1,570 1.10
Monticello 6147

1 2012 10 1,500 1.03

Monticello 61471 2012 11 1,100 0.82

Monticello 61471 2012 12 N/A

Monticello 61471 20131 N/A

Monticello 61471 201320 0.03

Monticello 61471 20133 N/A

Monticello 61471 20134 N/A

Monticello 61471 20135 514 1.11

Monticello 61471 20136 1,701 0.96

Monticello 61471 20137 1,938 0.94

Monticello 61471 20138 1,756 0.89

Monticello 61471 20139 775 0.82

Monticello 61471 2013 10 N/A

Monticello 61471 2013 11 N/A

Monticello 61471 2013 12 N/A 1.33

Monticello 61472 20091 2,158 0.99

Monticello 61472 20092 1,849 0.98

Monticello 61472 20093 2,072 1.00

Monticello 61472 20094 1,813 0.91

Monticello 61472 20095 1,166 0.84

Monticello 61472 20096 1,678 0.85

Monticello 61472 20097 1,783 0.86

Monticello 61472 20098 1,723 0.86

Monticello 61472 20099 1,701 0.86

Monticello 61472 2009 10 1,472 0.73

Monticello 61472 2009 11 1,757 0.90

Monticello 61472 2009 12 1,758 0.90

Monticello 61472 20101 1,865 0.92

Monticello 61472 20102 1,477 0.86

Monticello 61472 20103 1,609 0.89

Monticello 61472 20104 1,472 1.06

Monticello 61472 20105 1,197 0.88

Monticello 61472 20106 1,568 0.85

Monticello 61472 20107 1,589 0.86

Monticello 61472 20108 1,708 0.90

Monticello 61472 20109 1,738 0.95

Monticello 61472 2010 10 1,928 1.04

Monticello 61472 2010 11 1,737 0.97

Monticello 61472 2010 12 1,983 1.00

Monticello 61472 20111 1,942 0.98

Monticello 61472 20112 1,435 1.05

Monticello 61472 20113 159 0.97

Monticello 61472 20114 1,819 1.03

Monticello 61472 20115 1,832 0.97
Monticello 6147

2 20116 1,830 0.97

Monticello 61472 20117 1,909 0.98

Monticello 61472 20118 1,995 1.06

Monticello 61472 20119 1,578 0.98

Monticello 61472 2011 10 1,648 1.05

Monticello 61472 2011 11 1,681 1.03

Monticello 61472 2011 12 609 1.06

Monticello 61472 201210 0.03

Monticello 61472 20122 N/A

Monticello 61472 20123 N/A

Monticello 61472 20124 N/A

Monticello 61472 20125 1,374 1.26

Monticello 61472 20126 1,770 1.18

Monticello 61472 20127 1,730 1.04

Monticello 61472 20128 1,709 1.04

Monticello 61472 20129 1,507 1.08

Monticello 61472 2012 10 1,581 1.02

Monticello 61472 2012 11 1,307 0.83

Monticello 61472 2012 123 0.60

Monticello 61472 20131 N/A

Monticello 61472 20132 N/A

Monticello 61472 20133 N/A

Monticello 61472 20134 N/A

Monticello 61472 20135 450 0.99

Monticello 61472 20136 1,692 0.98

Monticello 61472 20137 1,969 0.94

Monticello 61472 20138 1,541 0.85

Monticello 61472 20139 1,419 0.74

Monticello 61472 2013 10 N/A

Monticello 61472 2013 11 N/A

Monticello 61472 2013 12 N/A 1.26

Tolk Station 6194 171B 20091 1,093 0.66

Tolk Station 6194 171B 20092 454 0.64

Tolk Station 6194 171B 20093 N/A

Tolk Station 6194 171B 20094 708 0.57

Tolk Station 6194 171B 20095 898 0.61

Tolk Station 6194 171B 20096 1,046 0.64

Tolk Station 6194 171B 20097 1,099 0.61

Tolk Station 6194 171B 20098 1,043 0.59

Tolk Station 6194 171B 20099 1,036 0.65

Tolk Station 6194 171B 2009 10 1,127 0.67

Tolk Station 6194 171B 2009 11 1,120 0.64

Tolk Station 6194 171B 2009 12 1,059 0.65

Tolk Station 6194 171B 20101 1,092 0.66
Tolk Station 6194 171B 2010

2 954 0.64

Tolk Station 6194 171B 20103 932 0.72

Tolk Station 6194 171B 20104 1,193 0.63

Tolk Station 6194 171B 20105 1,168 0.60

Tolk Station 6194 171B 20106 1,196 0.63

Tolk Station 6194 171B 20107 1,143 0.62

Tolk Station 6194 171B 20108 1,240 0.65

Tolk Station 6194 171B 20109 959 0.55

Tolk Station 6194 171B 2010 10 969 0.58

Tolk Station 6194 171B 2010 11 1,051 0.60

Tolk Station 6194 171B 2010 12 515 0.60

Tolk Station 6194 171B 20111 1,076 0.61

Tolk Station 6194 171B 20112 908 0.58

Tolk Station 6194 171B 20113 829 0.47

Tolk Station 6194 171B 20114 682 0.44

Tolk Station 6194 171B 20115 697 0.49

Tolk Station 6194 171B 20116 940 0.56

Tolk Station 6194 171B 20117 970 0.58

Tolk Station 6194 171B 20118 930 0.54

Tolk Station 6194 171B 20119 860 0.52

Tolk Station 6194 171B 2011 10 934 0.57

Tolk Station 6194 171B 2011 11 869 0.52

Tolk Station 6194 171B 2011 12 852 0.50

Tolk Station 6194 171B 20121 166 0.54

Tolk Station 6194 171B 201220 0.07

Tolk Station 6194 171B 20123 805 0.57

Tolk Station 6194 171B 20124 712 0.47

Tolk Station 6194 171B 20125 879 0.51

Tolk Station 6194 171B 20126 867 0.51

Tolk Station 6194 171B 20127 904 0.52

Tolk Station 6194 171B 20128 705 0.51

Tolk Station 6194 171B 20129 859 0.52

Tolk Station 6194 171B 2012 10 917 0.54

Tolk Station 6194 171B 2012 11 842 0.53

Tolk Station 6194 171B 2012 12 957 0.56

Tolk Station 6194 171B 20131 863 0.53

Tolk Station 6194 171B 20132 819 0.54

Tolk Station 6194 171B 20133 882 0.50

Tolk Station 6194 171B 20134 268 0.48

Tolk Station 6194 171B 20135 822 0.46

Tolk Station 6194 171B 20136 725 0.43

Tolk Station 6194 171B 20137 821 0.46

Tolk Station 6194 171B 20138 870 0.48

Tolk Station 6194 171B 20139 535 0.45
Tolk Station 6194 171B 2013 10 675 0.48

Tolk Station 6194 171B 2013 11 790 0.49

Tolk Station 6194 171B 2013 12 797 0.47 0.72

Tolk Station 6194 172B 20091 1,163 0.62

Tolk Station 6194 172B 20092 1,041 0.60

Tolk Station 6194 172B 20093 1,147 0.56

Tolk Station 6194 172B 20094 1,045 0.62

Tolk Station 6194 172B 20095 668 0.56

Tolk Station 6194 172B 20096 553 0.59

Tolk Station 6194 172B 20097 1,051 0.57

Tolk Station 6194 172B 20098 999 0.56

Tolk Station 6194 172B 20099 868 0.61

Tolk Station 6194 172B 2009 10 1,319 0.63

Tolk Station 6194 172B 2009 11 1,062 0.59

Tolk Station 6194 172B 2009 12 1,044 0.61

Tolk Station 6194 172B 20101 1,086 0.60

Tolk Station 6194 172B 20102 1,034 0.58

Tolk Station 6194 172B 20103 736 0.57

Tolk Station 6194 172B 20104 1,094 0.59

Tolk Station 6194 172B 20105 813 0.58

Tolk Station 6194 172B 20106 948 0.63

Tolk Station 6194 172B 20107 1,250 0.62

Tolk Station 6194 172B 20108 1,158 0.63

Tolk Station 6194 172B 20109 968 0.56

Tolk Station 6194 172B 2010 10 935 0.59

Tolk Station 6194 172B 2010 11 1,061 0.60

Tolk Station 6194 172B 2010 12 977 0.57

Tolk Station 6194 172B 20111 261 0.65

Tolk Station 6194 172B 20112 N/A

Tolk Station 6194 172B 20113 142 0.47

Tolk Station 6194 172B 20114 805 0.46

Tolk Station 6194 172B 20115 909 0.50

Tolk Station 6194 172B 20116 1,008 0.55

Tolk Station 6194 172B 20117 1,098 0.60

Tolk Station 6194 172B 20118 1,114 0.57

Tolk Station 6194 172B 20119 1,053 0.54

Tolk Station 6194 172B 2011 10 1,027 0.56

Tolk Station 6194 172B 2011 11 863 0.54

Tolk Station 6194 172B 2011 12 1,005 0.52

Tolk Station 6194 172B 20121 958 0.55

Tolk Station 6194 172B 20122 995 0.58

Tolk Station 6194 172B 20123 466 0.61

Tolk Station 6194 172B 20124 804 0.53

Tolk Station 6194 172B 20125 991 0.55
Tolk Station 6194 172B 2012

6 866 0.48

Tolk Station 6194 172B 20127 890 0.48

Tolk Station 6194 172B 20128 935 0.50

Tolk Station 6194 172B 20129 864 0.48

Tolk Station 6194 172B 2012 10 942 0.50

Tolk Station 6194 172B 2012 11 899 0.49

Tolk Station 6194 172B 2012 12 948 0.51

Tolk Station 6194 172B 20131 852 0.48

Tolk Station 6194 172B 20132 842 0.49

Tolk Station 6194 172B 20133 936 0.49

Tolk Station 6194 172B 20134 913 0.50

Tolk Station 6194 172B 20135 881 0.47

Tolk Station 6194 172B 20136 833 0.45

Tolk Station 6194 172B 20137 917 0.48

Tolk Station 6194 172B 20138 909 0.50

Tolk Station 6194 172B 20139 844 0.47

Tolk Station 6194 172B 2013 10 922 0.51

Tolk Station 6194 172B 2013 11 883 0.52

Tolk Station 6194 172B 2013 12 853 0.49 0.65

W A Parish 3470 WAP5 20091 1,358 0.63

W A Parish 3470 WAP5 20092 1,272 0.62

W A Parish 3470 WAP5 20093 614 0.66

W A Parish 3470 WAP5 20094 599 0.57

W A Parish 3470 WAP5 20095 1,578 0.64

W A Parish 3470 WAP5 20096 1,485 0.63

W A Parish 3470 WAP5 20097 1,490 0.60

W A Parish 3470 WAP5 20098 1,063 0.53

W A Parish 3470 WAP5 20099 1,146 0.57

W A Parish 3470 WAP5 2009 10 1,181 0.54

W A Parish 3470 WAP5 2009 11 994 0.58

W A Parish 3470 WAP5 2009 12 1,364 0.60

W A Parish 3470 WAP5 20101 1,545 0.67

W A Parish 3470 WAP5 20102 1,162 0.69

W A Parish 3470 WAP5 20103 1,398 0.72

W A Parish 3470 WAP5 20104 1,266 0.69

W A Parish 3470 WAP5 20105 1,303 0.65

W A Parish 3470 WAP5 20106 1,464 0.63

W A Parish 3470 WAP5 20107 1,378 0.61

W A Parish 3470 WAP5 20108 1,161 0.57

W A Parish 3470 WAP5 20109 1,370 0.68

W A Parish 3470 WAP5 2010 10 1,115 0.69

W A Parish 3470 WAP5 2010 11 1,328 0.80

W A Parish 3470 WAP5 2010 12 1,742 0.78

W A Parish 3470 WAP5 20111 1,621 0.72
W A Parish 3470 WAP5 2011

2 1,273 0.68

W A Parish 3470 WAP5 20113 160 0.64

W A Parish 3470 WAP5 20114 840 0.70

W A Parish 3470 WAP5 20115 1,545 0.70

W A Parish 3470 WAP5 20116 1,406 0.66

W A Parish 3470 WAP5 20117 1,630 0.69

W A Parish 3470 WAP5 20118 1,568 0.68

W A Parish 3470 WAP5 20119 1,459 0.70

W A Parish 3470 WAP5 2011 10 1,420 0.76

W A Parish 3470 WAP5 2011 11 897 0.71

W A Parish 3470 WAP5 2011 12 1,174 0.66

W A Parish 3470 WAP5 20121 578 0.62

W A Parish 3470 WAP5 20122 764 0.68

W A Parish 3470 WAP5 20123 1,391 0.67

W A Parish 3470 WAP5 20124 1,199 0.63

W A Parish 3470 WAP5 20125 975 0.58

W A Parish 3470 WAP5 20126 1,338 0.64

W A Parish 3470 WAP5 20127 1,317 0.64

W A Parish 3470 WAP5 20128 1,303 0.61

W A Parish 3470 WAP5 20129 547 0.58

W A Parish 3470 WAP5 2012 10 1,188 0.67

W A Parish 3470 WAP5 2012 11 1,251 0.61

W A Parish 3470 WAP5 2012 12 921 0.63

W A Parish 3470 WAP5 20131 887 0.63

W A Parish 3470 WAP5 20132 841 0.63

W A Parish 3470 WAP5 20133 1,210 0.62

W A Parish 3470 WAP5 20134 1,070 0.68

W A Parish 3470 WAP5 20135 1,446 0.65

W A Parish 3470 WAP5 20136 1,075 0.59

W A Parish 3470 WAP5 20137 1,107 0.61

W A Parish 3470 WAP5 20138 1,194 0.63

W A Parish 3470 WAP5 20139 1,240 0.65

W A Parish 3470 WAP5 2013 10 1,153 0.65

W A Parish 3470 WAP5 2013 11 864 0.70

W A Parish 3470 WAP5 2013 12 1,249 0.65 0.80

W A Parish 3470 WAP6 20091 1,292 0.66

W A Parish 3470 WAP6 20092 1,182 0.65

W A Parish 3470 WAP6 20093 1,242 0.62

W A Parish 3470 WAP6 20094 940 0.60

W A Parish 3470 WAP6 20095 1,425 0.69

W A Parish 3470 WAP6 20096 1,377 0.66

W A Parish 3470 WAP6 20097 1,236 0.62

W A Parish 3470 WAP6 20098 1,196 0.52

W A Parish 3470 WAP6 20099 1,082 0.57
W A Parish 3470 WAP6 2009 10 1,017 0.56

W A Parish 3470 WAP6 2009 11 534 0.62

W A Parish 3470 WAP6 2009 12 685 0.64

W A Parish 3470 WAP6 20101 1,468 0.73

W A Parish 3470 WAP6 20102 1,540 0.78

W A Parish 3470 WAP6 20103 1,458 0.82

W A Parish 3470 WAP6 20104 1,411 0.78

W A Parish 3470 WAP6 20105 1,372 0.72

W A Parish 3470 WAP6 20106 1,492 0.71

W A Parish 3470 WAP6 20107 1,436 0.69

W A Parish 3470 WAP6 20108 1,189 0.62

W A Parish 3470 WAP6 20109 1,471 0.74

W A Parish 3470 WAP6 2010 10 971 0.73

W A Parish 3470 WAP6 2010 11 1,463 0.87

W A Parish 3470 WAP6 2010 12 1,879 0.83

W A Parish 3470 WAP6 20111 1,798 0.75

W A Parish 3470 WAP6 20112 1,212 0.72

W A Parish 3470 WAP6 20113 1,313 0.68

W A Parish 3470 WAP6 20114 1,713 0.71

W A Parish 3470 WAP6 20115 1,689 0.70

W A Parish 3470 WAP6 20116 1,649 0.67

W A Parish 3470 WAP6 20117 1,777 0.70

W A Parish 3470 WAP6 20118 1,774 0.70

W A Parish 3470 WAP6 20119 1,640 0.72

W A Parish 3470 WAP6 2011 10 1,591 0.76

W A Parish 3470 WAP6 2011 11 1,006 0.72

W A Parish 3470 WAP6 2011 12 1,107 0.67

W A Parish 3470 WAP6 20121 140 0.70

W A Parish 3470 WAP6 20122 N/A

W A Parish 3470 WAP6 20123 1,061 0.67

W A Parish 3470 WAP6 20124 1,360 0.65

W A Parish 3470 WAP6 20125 1,280 0.58

W A Parish 3470 WAP6 20126 1,467 0.64

W A Parish 3470 WAP6 20127 1,079 0.63

W A Parish 3470 WAP6 20128 1,462 0.61

W A Parish 3470 WAP6 20129 1,250 0.60

W A Parish 3470 WAP6 2012 10 1,402 0.67

W A Parish 3470 WAP6 2012 11 1,346 0.61

W A Parish 3470 WAP6 2012 12 848 0.63

W A Parish 3470 WAP6 20131 746 0.61

W A Parish 3470 WAP6 20132 591 0.67

W A Parish 3470 WAP6 20133 1,408 0.64

W A Parish 3470 WAP6 20134 1,384 0.69

W A Parish 3470 WAP6 20135 1,518 0.68
W A Parish 3470 WAP6 2013

6 1,338 0.63

W A Parish 3470 WAP6 20137 1,536 0.64

W A Parish 3470 WAP6 20138 1,344 0.64

W A Parish 3470 WAP6 20139 1,363 0.65

W A Parish 3470 WAP6 2013 10 1,459 0.64

W A Parish 3470 WAP6 2013 11 1,346 0.70

W A Parish 3470 WAP6 2013 12 1,533 0.65 0.87

W A Parish 3470 WAP7 20091 1,084 0.66

W A Parish 3470 WAP7 20092 1,006 0.66

W A Parish 3470 WAP7 20093 1,052 0.62

W A Parish 3470 WAP7 20094 812 0.56

W A Parish 3470 WAP7 20095 1,082 0.61

W A Parish 3470 WAP7 20096 942 0.55

W A Parish 3470 WAP7 20097 1,216 0.61

W A Parish 3470 WAP7 20098 1,263 0.63

W A Parish 3470 WAP7 20099 690 0.59

W A Parish 3470 WAP7 2009 10 1,011 0.54

W A Parish 3470 WAP7 2009 11 1,094 0.62

W A Parish 3470 WAP7 2009 12 1,242 0.67

W A Parish 3470 WAP7 20101 1,257 0.74

W A Parish 3470 WAP7 20102 1,191 0.72

W A Parish 3470 WAP7 20103 1,361 0.82

W A Parish 3470 WAP7 20104 1,204 0.77

W A Parish 3470 WAP7 20105 935 0.68

W A Parish 3470 WAP7 20106 1,292 0.73

W A Parish 3470 WAP7 20107 1,211 0.68

W A Parish 3470 WAP7 20108 1,157 0.62

W A Parish 3470 WAP7 20109 1,243 0.72

W A Parish 3470 WAP7 2010 10 1,050 0.72

W A Parish 3470 WAP7 2010 11 200 0.78

W A Parish 3470 WAP7 2010 12 1,099 0.75

W A Parish 3470 WAP7 20111 979 0.74

W A Parish 3470 WAP7 20112 1,046 0.73

W A Parish 3470 WAP7 20113 1,101 0.67

W A Parish 3470 WAP7 20114 1,088 0.69

W A Parish 3470 WAP7 20115 1,215 0.69

W A Parish 3470 WAP7 20116 1,210 0.67

W A Parish 3470 WAP7 20117 1,317 0.68

W A Parish 3470 WAP7 20118 1,301 0.67

W A Parish 3470 WAP7 20119 1,312 0.78

W A Parish 3470 WAP7 2011 10 1,205 0.81

W A Parish 3470 WAP7 2011 11 1,001 0.75

W A Parish 3470 WAP7 2011 12 372 0.63

W A Parish 3470 WAP7 20121 N/A
W A Parish 3470 WAP7 2012

2 517 0.74

W A Parish 3470 WAP7 20123 1,190 0.75

W A Parish 3470 WAP7 20124 701 0.71

W A Parish 3470 WAP7 20125 948 0.67

W A Parish 3470 WAP7 20126 929 0.66

W A Parish 3470 WAP7 20127 919 0.63

W A Parish 3470 WAP7 20128 1,201 0.67

W A Parish 3470 WAP7 20129 839 0.58

W A Parish 3470 WAP7 2012 10 1,074 0.65

W A Parish 3470 WAP7 2012 11 1,198 0.73

W A Parish 3470 WAP7 2012 12 874 0.69

W A Parish 3470 WAP7 20131 256 0.60

W A Parish 3470 WAP7 20132 294 0.67

W A Parish 3470 WAP7 20133 1,261 0.68

W A Parish 3470 WAP7 20134 1,395 0.75

W A Parish 3470 WAP7 20135 1,321 0.70

W A Parish 3470 WAP7 20136 1,103 0.67

W A Parish 3470 WAP7 20137 1,381 0.69

W A Parish 3470 WAP7 20138 1,210 0.64

W A Parish 3470 WAP7 20139 973 0.67

W A Parish 3470 WAP7 2013 100 0.00

W A Parish 3470 WAP7 2013 11 885 0.70

W A Parish 3470 WAP7 2013 12 1,286 0.68 0.82

Welsh Power Plant 61391 20091 791 0.48

Welsh Power Plant 61391 20092 649 0.47

Welsh Power Plant 61391 20093 865 0.51

Welsh Power Plant 61391 20094 768 0.47

Welsh Power Plant 61391 20095 181 0.53

Welsh Power Plant 61391 20096 812 0.49

Welsh Power Plant 61391 20097 922 0.49

Welsh Power Plant 61391 20098 883 0.48

Welsh Power Plant 61391 20099 860 0.48

Welsh Power Plant 61391 2009 10 883 0.47

Welsh Power Plant 61391 2009 11 891 0.48

Welsh Power Plant 61391 2009 12 555 0.49

Welsh Power Plant 61391 20101 172 0.44

Welsh Power Plant 61391 20102 779 0.49

Welsh Power Plant 61391 20103 376 0.49

Welsh Power Plant 61391 20104 772 0.48

Welsh Power Plant 61391 20105 832 0.47

Welsh Power Plant 61391 20106 870 0.48

Welsh Power Plant 61391 20107 867 0.46

Welsh Power Plant 61391 20108 852 0.47

Welsh Power Plant 61391 20109 764 0.45
Welsh Power Plant 6139

1 2010 10 760 0.46

Welsh Power Plant 61391 2010 11 499 0.44

Welsh Power Plant 61391 2010 12 816 0.44

Welsh Power Plant 61391 20111 829 0.44

Welsh Power Plant 61391 20112 671 0.43

Welsh Power Plant 61391 20113 798 0.45

Welsh Power Plant 61391 20114 753 0.44

Welsh Power Plant 61391 20115 21 0.40

Welsh Power Plant 61391 20116 713 0.47

Welsh Power Plant 61391 20117 860 0.44

Welsh Power Plant 61391 20118 821 0.44

Welsh Power Plant 61391 20119 739 0.44

Welsh Power Plant 61391 2011 10 787 0.44

Welsh Power Plant 61391 2011 11 723 0.43

Welsh Power Plant 61391 2011 12 686 0.40

Welsh Power Plant 61391 20121 720 0.41

Welsh Power Plant 61391 20122 685 0.43

Welsh Power Plant 61391 20123 487 0.42

Welsh Power Plant 61391 20124 650 0.42

Welsh Power Plant 61391 20125 705 0.42

Welsh Power Plant 61391 20126 668 0.43

Welsh Power Plant 61391 20127 773 0.43

Welsh Power Plant 61391 20128 777 0.42

Welsh Power Plant 61391 20129 315 0.43

Welsh Power Plant 61391 2012 10 304 0.44

Welsh Power Plant 61391 2012 11 686 0.42

Welsh Power Plant 61391 2012 12 721 0.42

Welsh Power Plant 61391 20131 573 0.41

Welsh Power Plant 61391 20132 585 0.44

Welsh Power Plant 61391 20133 481 0.42

Welsh Power Plant 61391 20134 645 0.46

Welsh Power Plant 61391 20135 515 0.43

Welsh Power Plant 61391 20136 608 0.43

Welsh Power Plant 61391 20137 608 0.42

Welsh Power Plant 61391 20138 654 0.43

Welsh Power Plant 61391 20139 571 0.43

Welsh Power Plant 61391 2013 100 0.01

Welsh Power Plant 61391 2013 11 541 0.43

Welsh Power Plant 61391 2013 12 688 0.43 0.53

Welsh Power Plant 61392 20091 812 0.47

Welsh Power Plant 61392 20092 701 0.45

Welsh Power Plant 61392 20093 817 0.51

Welsh Power Plant 61392 20094 177 0.45

Welsh Power Plant 61392 20095 933 0.51
Welsh Power Plant 6139

2 20096 873 0.50

Welsh Power Plant 61392 20097 960 0.49

Welsh Power Plant 61392 20098 922 0.48

Welsh Power Plant 61392 20099 756 0.49

Welsh Power Plant 61392 2009 10 884 0.48

Welsh Power Plant 61392 2009 11 671 0.49

Welsh Power Plant 61392 2009 12 947 0.51

Welsh Power Plant 61392 20101 862 0.46

Welsh Power Plant 61392 20102 730 0.48

Welsh Power Plant 61392 20103 676 0.46

Welsh Power Plant 61392 20104 792 0.48

Welsh Power Plant 61392 20105 835 0.45

Welsh Power Plant 61392 20106 839 0.47

Welsh Power Plant 61392 20107 883 0.46

Welsh Power Plant 61392 20108 833 0.45

Welsh Power Plant 61392 20109 621 0.44

Welsh Power Plant 61392 2010 10 208 0.44

Welsh Power Plant 61392 2010 11 729 0.43

Welsh Power Plant 61392 2010 12 785 0.43

Welsh Power Plant 61392 20111 716 0.43

Welsh Power Plant 61392 20112 669 0.44

Welsh Power Plant 61392 20113 846 0.46

Welsh Power Plant 61392 20114 566 0.45

Welsh Power Plant 61392 20115 804 0.46

Welsh Power Plant 61392 20116 815 0.46

Welsh Power Plant 61392 20117 850 0.44

Welsh Power Plant 61392 20118 881 0.45

Welsh Power Plant 61392 20119 367 0.45

Welsh Power Plant 61392 2011 10 339 0.43

Welsh Power Plant 61392 2011 11 787 0.45

Welsh Power Plant 61392 2011 12 745 0.41

Welsh Power Plant 61392 20121 751 0.43

Welsh Power Plant 61392 20122 644 0.42

Welsh Power Plant 61392 20123 740 0.42

Welsh Power Plant 61392 20124 131 0.40

Welsh Power Plant 61392 20125 687 0.42

Welsh Power Plant 61392 20126 707 0.43

Welsh Power Plant 61392 20127 788 0.43

Welsh Power Plant 61392 20128 793 0.43

Welsh Power Plant 61392 20129 249 0.43

Welsh Power Plant 61392 2012 10 581 0.44

Welsh Power Plant 61392 2012 11 747 0.42

Welsh Power Plant 61392 2012 12 770 0.42

Welsh Power Plant 61392 20131 620 0.40
Welsh Power Plant 6139

2 20132 586 0.44

Welsh Power Plant 61392 20133 655 0.42

Welsh Power Plant 61392 20134 256 0.44

Welsh Power Plant 61392 20135 285 0.44

Welsh Power Plant 61392 20136 448 0.43

Welsh Power Plant 61392 20137 638 0.43

Welsh Power Plant 61392 20138 672 0.44

Welsh Power Plant 61392 20139 607 0.44

Welsh Power Plant 61392 2013 10 496 0.41

Welsh Power Plant 61392 2013 11 405 0.42

Welsh Power Plant 61392 2013 12 492 0.42 0.51

Welsh Power Plant 61393 20091 859 0.48

Welsh Power Plant 61393 20092 516 0.47

Welsh Power Plant 61393 20093 366 0.50

Welsh Power Plant 61393 20094 811 0.49

Welsh Power Plant 61393 20095 933 0.53

Welsh Power Plant 61393 20096 845 0.50

Welsh Power Plant 61393 20097 884 0.50

Welsh Power Plant 61393 20098 890 0.49

Welsh Power Plant 61393 20099 509 0.49

Welsh Power Plant 61393 2009 10 456 0.48

Welsh Power Plant 61393 2009 11 870 0.50

Welsh Power Plant 61393 2009 12 919 0.52

Welsh Power Plant 61393 20101 799 0.46

Welsh Power Plant 61393 20102 773 0.49

Welsh Power Plant 61393 20103 867 0.49

Welsh Power Plant 61393 20104 92 0.47

Welsh Power Plant 61393 20105 971 0.48

Welsh Power Plant 61393 20106 940 0.49

Welsh Power Plant 61393 20107 1,010 0.48

Welsh Power Plant 61393 20108 974 0.48

Welsh Power Plant 61393 20109 864 0.45

Welsh Power Plant 61393 2010 10 796 0.44

Welsh Power Plant 61393 2010 11 700 0.42

Welsh Power Plant 61393 2010 12 748 0.44

Welsh Power Plant 61393 20111 678 0.46

Welsh Power Plant 61393 20112 53 0.36

Welsh Power Plant 61393 20113 834 0.47

Welsh Power Plant 61393 20114 831 0.47

Welsh Power Plant 61393 20115 858 0.46

Welsh Power Plant 61393 20116 813 0.47

Welsh Power Plant 61393 20117 887 0.45

Welsh Power Plant 61393 20118 875 0.45

Welsh Power Plant 61393 20119 816 0.44
Welsh Power Plant 6139

3 2011 10 860 0.46

Welsh Power Plant 61393 2011 11 584 0.45

Welsh Power Plant 61393 2011 12 746 0.42

Welsh Power Plant 61393 20121 769 0.44

Welsh Power Plant 61393 20122 680 0.44

Welsh Power Plant 61393 20123 751 0.43

Welsh Power Plant 61393 20124 654 0.43

Welsh Power Plant 61393 20125 236 0.41

Welsh Power Plant 61393 20126 563 0.43

Welsh Power Plant 61393 20127 810 0.44

Welsh Power Plant 61393 20128 861 0.44

Welsh Power Plant 61393 20129 641 0.43

Welsh Power Plant 61393 2012 10 769 0.43

Welsh Power Plant 61393 2012 11 715 0.42

Welsh Power Plant 61393 2012 12 684 0.42

Welsh Power Plant 61393 20131 507 0.40

Welsh Power Plant 61393 20132 330 0.45

Welsh Power Plant 61393 20133 333 0.42

Welsh Power Plant 61393 20134 710 0.46

Welsh Power Plant 61393 20135 718 0.44

Welsh Power Plant 61393 20136 614 0.42

Welsh Power Plant 61393 20137 680 0.42

Welsh Power Plant 61393 20138 696 0.44

Welsh Power Plant 61393 20139 647 0.44

Welsh Power Plant 61393 2013 10 566 0.41

Welsh Power Plant 61393 2013 11 586 0.43

Welsh Power Plant 61393 2013 12 705 0.43 0.53
 Avg. NOx 

Rate 

(lb/MMBtu) NOx (tons)

 Heat Input 

(MMBtu)

 Operating 

Time

 Gross Load 

(MW-h)

Gross Heat 

Rate 

(Btu/kWh)

0.1312 281 4,251,977 744 435,573 9,762

0.1179 217 3,653,119 672 372,986 9,794

0.1178 228 3,814,937 744 382,404 9,976

0.115 160 2,743,733 552.58 271,184 10,118

0.1363 193 2,702,337 542.12 270,808 9,979

0.1456 284 3,903,517 720 391,543 9,970

0.148 285 3,843,867 706.85 383,697 10,018

0.143 243 3,367,750 624.67 334,246 10,076

0.1389 267 3,780,728 720 375,267 10,075

0.15 260 3,439,093 715.68 363,805 9,453

0.1341 241 3,561,355 720 369,296 9,644

0.1498 284 3,771,709 726.4 395,851 9,528

0.1351 271 4,001,658 744 421,332 9,498

0.1403 276 3,924,158 671.77 411,375 9,539

0.1453 228 3,126,123 555.62 322,925 9,681

0.1309 246 3,735,858 669.38 391,206 9,550

0.1353 271 3,961,899 740.15 413,987 9,570

0.1357 278 4,080,485 720 430,438 9,480

0.1402 303 4,315,721 744 453,532 9,516

0.1385 295 4,251,623 744 445,333 9,547

0.1414 285 3,999,412 719.98 422,370 9,469

0.1406 279 3,913,033 737.22 406,075 9,636

0.1345 264 3,875,566 719.93 398,123 9,735

0.1349 283 4,118,812 744 423,873 9,717

0.1371 267 3,840,935 700.7 398,893 9,629

0.1292 232 3,537,090 672 366,075 9,662

0.1264 212 3,389,909 744 342,827 9,888

0.1342 6 90,656 22.98 8,822 10,277

0.1589 266 3,358,803 696.98 345,467 9,722

0.1453 274 3,807,942 720 392,923 9,691

0.1411 286 4,122,582 744 423,708 9,730

0.1499 262 3,623,026 703.24 371,375 9,756

0.1531 293 3,928,000 720 405,987 9,675

0.14 258 3,770,369 744 392,794 9,599

0.132 210 3,184,748 719.96 329,841 9,655

0.1292 188 2,953,436 736.63 303,820 9,721

0.1199 105 1,792,195 465.81 184,258 9,727

0.1421 203 2,919,353 613.28 305,184 9,566

0.1315 219 3,349,041 699.02 347,906 9,626

0.1299 235 3,543,140 720 368,996 9,602
0.1297 200 3,045,771 653.19 316,892 9,611

0.133 227 3,388,515 664.15 355,304 9,537

0.1334 256 3,800,806 744 396,173 9,594

0.1342 257 3,832,353 744 399,178 9,601

0.1271 237 3,692,002 720 382,262 9,658

0.1276 265 4,139,395 741.97 425,275 9,733

0.1372 161 2,347,168 456.07 243,238 9,650

0.1335 248 3,702,587 744 384,504 9,630

0.1326 220 3,287,390 645.2 337,093 9,752

0.1265 221 3,457,296 672 354,210 9,761

0.1282 266 4,162,619 744 424,147 9,814

0.134 191 2,892,085 515.04 296,898 9,741

0.1282 217 3,351,809 669.63 342,329 9,791

0.1307 222 3,416,090 659.95 346,624 9,855

0.135 275 4,089,086 744 415,328 9,845

0.1316 266 4,037,660 744 406,462 9,934

0.1355 222 3,321,815 636.13 334,384 9,934

0.1386 256 3,744,497 690.68 380,392 9,844

0.1297 236 3,650,772 698.45 375,371 9,726

0.1316 270 4,132,287 743.97 424,571 9,733

0.1409 260 3,697,339 718.04 364,884 10,133

0.1369 231 3,320,293 631.22 324,938 10,218

0.1369 178 2,587,460 588.01 254,327 10,174

0.1372 233 3,406,285 687.85 332,479 10,245 0 N/A

0.1494 185 2,454,143 486.12 251,131 9,772

0.153 307 3,992,875 744 417,362 9,567

0.1537 298 3,855,899 740.4 404,361 9,536

0.1451 267 3,670,903 720 384,703 9,542

0.1429 275 3,845,881 739.66 380,787 10,100

0.1566 292 3,764,871 720 375,718 10,020

0.1534 309 4,096,351 697.14 401,292 10,208

0.1548 303 3,921,674 656.31 382,260 10,259

0.1527 314 4,136,153 672 413,092 10,013

0.1441 318 4,407,241 741.46 441,460 9,983

0.1388 301 4,331,812 720 435,202 9,954

0.1406 289 4,095,032 735.73 420,403 9,741

0.1386 295 4,251,769 719.97 437,379 9,721

0.1433 296 4,144,828 708.06 427,835 9,688

0.145 324 4,468,449 744 457,616 9,765

0.1433 296 4,125,283 720 427,714 9,645

0.1463 192 2,632,610 530.58 271,644 9,691

0.1384 249 3,571,231 675.45 373,982 9,549

0.141 295 4,152,025 743.98 433,304 9,582

0.1335 281 4,195,598 744 430,404 9,748
0.1352 231 3,380,813 658.02 345,013 9,799

0.1362 257 3,771,247 744 367,702 10,256

0.1433 268 3,764,088 707.51 370,698 10,154

0.145 293 4,085,442 744 398,577 10,250

0.1416 257 3,697,402 642.69 355,072 10,413

0.1307 268 4,176,041 715.35 399,682 10,448

0.1443 284 3,996,999 706.55 390,116 10,246

0.1412 289 4,139,126 720 405,899 10,197

0.1473 196 2,748,490 512.51 263,011 10,450

0.1285 219 3,385,574 720 327,907 10,325

0.1201 198 3,267,989 744 320,802 10,187

0.1319 193 2,963,973 682.26 285,976 10,364

0.1296 98 1,526,308 333.87 146,461 10,421

0.1266 237 3,714,581 744 368,816 10,072

0.1276 237 3,600,816 720 365,753 9,845

0.1292 237 3,563,784 744 359,122 9,924

0.1313 234 3,476,766 656.23 355,672 9,775

0.1266 255 3,904,771 744 396,202 9,856

0.1338 266 3,898,932 744 394,643 9,880

0.1354 260 3,747,907 720 378,297 9,907

0.1367 95 1,345,699 262.72 134,930 9,973

0.14 98 1,406,353 291.37 141,429 9,944

0.1248 219 3,446,420 703.15 347,059 9,930

0.1292 248 3,779,616 743.98 383,653 9,852

0.1286 195 2,971,267 599.32 300,555 9,886

0.133 253 3,739,435 684.88 385,818 9,692

0.1378 268 3,867,020 704.37 398,534 9,703

0.13 245 3,724,025 744 381,677 9,757

0.123 202 3,239,359 651.72 332,089 9,754

0.1299 263 3,994,735 744 410,996 9,720

0.1336 268 3,945,803 744 404,571 9,753

0.135 266 3,906,180 720 400,370 9,756

0.1307 246 3,761,727 698.21 381,818 9,852

0.1297 169 2,616,042 499.7 265,363 9,858

0.1339 275 4,082,251 744 421,642 9,682

0.1532 345 4,489,087 744 482,456 9,305

0.1592 330 4,143,710 672 435,981 9,504

0.1549 327 4,199,605 703.82 445,771 9,421

0.1569 341 4,346,168 720 465,766 9,331

0.1598 365 4,563,738 744 485,032 9,409

0.1879 420 4,465,211 720 469,297 9,515

0.1697 328 3,809,791 642.68 401,851 9,481

0.1575 335 4,256,471 730.83 473,964 8,981

0.1633 343 4,193,705 720 467,818 8,964
0.1621 361 4,448,301 744 483,760 9,195

0.166 349 4,176,821 720 456,053 9,159

0.1662 355 4,237,611 701.77 442,921 9,567

0.1665 380 4,561,900 744 481,991 9,465

0.1619 271 3,302,205 575.6 355,025 9,301 0 N/A

0.1736 77 886,649 223.34 115,103 7,703

0.1594 313 3,871,007 713 453,696 8,532

0.1481 339 4,571,472 720 478,660 9,551

0.1552 366 4,716,242 744 497,223 9,485

0.1414 303 4,282,118 696.58 454,455 9,423

0.1349 303 4,455,379 720 478,048 9,320

0.1426 326 4,548,938 744 482,052 9,437

0.1325 293 4,414,824 720 475,535 9,284

0.1347 263 3,886,066 648.77 415,253 9,358

0.1273 294 4,625,971 744 495,637 9,333

0.1225 253 4,114,571 672 440,644 9,338

0.1254 263 4,178,957 690.9 445,804 9,374

0.135 277 4,094,936 681.98 440,987 9,286

0.1277 266 4,147,014 688.88 447,408 9,269

0.1273 294 4,623,666 720 479,257 9,648

0.1244 303 4,874,712 744 498,750 9,774

0.1264 303 4,720,536 742.58 481,728 9,799

0.1333 296 4,433,304 697.33 454,475 9,755 0 N/A 0 N/A

0.1625 84 973,651 201.26 102,458 9,503

0.1322 295 4,444,472 744 473,542 9,386

0.1221 256 4,179,882 696 446,829 9,355

0.1231 275 4,453,709 744 474,838 9,379

0.1293 256 3,947,081 670.72 419,627 9,406

0.1232 276 4,489,893 744 480,168 9,351

0.122 253 4,138,102 695.32 440,547 9,393

0.1306 292 4,463,179 740.71 476,808 9,361

0.1362 314 4,606,274 744 491,117 9,379

0.1293 286 4,417,565 720 467,503 9,449

0.1261 290 4,594,245 744 487,493 9,424

0.1164 259 4,444,000 720 473,640 9,383

0.1378 314 4,548,716 744 486,708 9,346

0.1313 237 3,577,934 606.95 383,683 9,325

0.1321 265 4,009,074 672 430,184 9,319

0.122 267 4,367,440 744 467,691 9,338

0.1244 231 3,715,568 623 396,941 9,361

0.1255 205 3,229,122 565.87 342,274 9,434
0.137 301 4,371,744 714.07 459,536 9,513

0.1368 320 4,670,321 744 489,011 9,551

0.1279 297 4,640,423 744 486,279 9,543

0.1337 301 4,504,205 720 475,286 9,477

0.1262 231 3,671,608 599.83 389,498 9,427

0.1366 88 1,248,602 230.73 131,693 9,481

0.1362 300 4,399,552 717.28 467,971 9,401

0.234 258 2,146,698 625 200,379 10,713

0.229 258 2,240,912 672 226,039 9,914

0.2262 249 2,175,397 713 225,516 9,646

0.2419 166 1,361,138 499 145,640 9,346

0.2318 242 2,087,809 744 221,292 9,435

0.2407 243 2,004,872 698.95 213,973 9,370

0.2229 251 1,952,932 744 206,787 9,444

0.2675 335 2,432,731 744 243,074 10,008

0.2739 322 2,291,104 717.98 236,256 9,698

0.2862 343 2,263,294 732 232,963 9,715

0.3046 329 2,097,452 720 235,746 8,897

0.3354 365 2,141,677 742.95 246,165 8,700

0.3353 296 1,739,645 626 205,608 8,461

0.36 259 1,399,561 411 129,295 10,825

0.2553 285 2,134,567 741.93 222,399 9,598

0.2246 201 1,708,446 649 181,603 9,408

0.257 275 2,071,326 704.95 220,382 9,399

0.2738 301 2,120,665 692 217,420 9,754

0.2725 302 2,086,234 721 220,674 9,454

0.2473 282 2,184,988 741.98 229,023 9,540

0.2398 41 322,648 115 33,407 9,658

0.259 142 1,033,390 393.2 104,907 9,851

0.4179 366 1,751,387 719 195,279 8,969

0.1693 181 2,179,935 743.78 238,645 9,135

0.1851 171 1,848,713 725.58 233,496 7,918

0.1794 121 1,359,881 626.19 182,333 7,458

0.1499 120 1,576,917 723.93 214,426 7,354

0.1648 170 2,052,069 720 244,053 8,408

0.1613 145 1,817,605 700.67 207,463 8,761

0.1597 164 2,063,735 720 214,244 9,633

0.1512 178 2,343,218 725.34 236,715 9,899

0.1585 187 2,354,053 743.97 242,410 9,711

0.1646 150 1,831,739 720 196,128 9,340

0.1766 157 1,768,010 618 184,868 9,564 0 N/A

0.1483 23 294,363 272.81 26,277 11,202

0.1644 123 1,485,529 591.74 150,181 9,892
0.157 90 1,155,654 423.83 121,683 9,497

0.1696 158 1,881,681 728.55 204,455 9,203

0.1498 138 1,829,393 692.95 196,291 9,320

0.1395 83 1,127,270 409.27 115,147 9,790

0.1564 164 2,083,055 640.25 205,851 10,119

0.1618 211 2,590,221 744 253,537 10,216

0.1628 127 1,560,182 581 188,184 8,291

0.1507 50 628,773 227.38 67,261 9,348

0.1496 144 1,931,630 743.7 221,395 8,725

0.1537 139 1,815,292 686.51 189,988 9,555

0.1423 154 2,166,702 744 224,667 9,644

0.1543 70 913,732 311.58 95,704 9,547 0 N/A

0.1712 145 1,640,458 568.66 155,886 10,523

0.1633 130 1,599,091 593.72 156,754 10,201

0.1645 159 1,934,830 602.46 185,603 10,425

0.1342 77 1,102,397 406.48 102,684 10,736

0.148 162 2,197,983 744 209,609 10,486

0.1389 153 2,180,809 741.98 206,899 10,540

0.1398 138 1,973,793 719.94 191,962 10,282

0.1363 142 2,064,871 744 207,894 9,932

0.1295 51 772,391 335.94 75,275 10,261

0.1382 146 2,091,584 744 201,904 10,359

0.1414 189 2,690,840 729.17 253,302 10,623

0.1528 186 2,454,352 672 231,839 10,586

0.1636 209 2,607,532 744 244,856 10,649

0.1723 193 2,326,061 718 216,968 10,721

0.1453 156 2,193,507 744 224,065 9,790

0.1374 144 2,125,907 720 221,016 9,619

0.139 165 2,392,885 739.93 245,537 9,746

0.1521 180 2,428,484 743.62 247,084 9,829

0.1453 162 2,263,862 706.1 237,564 9,529

0.1498 170 2,274,240 722.88 240,367 9,462

0.1627 174 2,155,656 720 241,684 8,919

0.1733 196 2,248,305 715.85 235,817 9,534

0.07559 127,855 136.52 12,753 10,025

0.10973 55,702 88 7,774 7,165

0.1653 171 2,079,249 742 214,202 9,707

0.1744 174 2,062,244 720 215,881 9,553

0.1613 121 1,523,279 487.53 159,721 9,537

0.0536 22 818,868 624.41 75,415 10,858

0.155 151 1,795,565 618.01 178,269 10,072

0.184 225 2,436,617 744 243,831 9,993

0.159 186 2,322,396 678.05 231,224 10,044
0.1693 194 2,283,568 701.51 231,979 9,844

0.1629 157 2,002,955 717.92 205,143 9,764

0.1684 195 2,341,629 744 239,738 9,767

0.1767 214 2,429,798 744 254,510 9,547

0.1979 196 2,019,199 671.95 213,248 9,469

0.1627 150 1,866,382 645.95 197,749 9,438 0 N/A

0.1538 125 1,585,721 583.07 150,926 10,507

0.1781 186 2,189,144 718.77 212,115 10,321

0.1606 198 2,494,018 744 242,413 10,288

0.1579 170 2,104,488 654.11 199,622 10,542

0.1611 183 2,291,018 694.23 216,828 10,566

0.1821 152 1,667,144 518.12 156,266 10,669 0 N/A

0.192 57 590,684 287.41 48,340 12,219

0.2269 301 2,656,428 741 244,777 10,852

0.173 225 2,576,634 695.97 228,363 11,283

0.168 194 2,300,721 724.4 204,427 11,254

0.1333 150 2,250,536 720 212,107 10,610

0.1334 122 1,802,173 506.57 169,728 10,618

0.1425 157 2,147,136 631.53 198,712 10,805

0.1462 205 2,792,838 744 255,760 10,920

0.1428 175 2,437,438 718.08 223,307 10,915

0.1541 189 2,471,143 720 237,803 10,392

0.1487 74 982,094 337.23 92,027 10,672

0.1408 104 1,413,011 504.43 130,502 10,827

0.1623 194 2,432,117 741.08 221,300 10,990

0.1552 155 1,994,710 612.3 186,520 10,694

0.1509 168 2,257,663 671.93 213,025 10,598

0.1497 115 1,573,748 526.43 148,617 10,589

0.1896 102 1,111,657 503.4 103,074 10,785

0.1614 71 876,758 314.4 82,977 10,566

0.1442 159 2,189,678 720 207,298 10,563

0.1433 166 2,286,278 743.98 215,920 10,589

0.1478 164 2,201,656 744 211,128 10,428

0.1633 71 867,487 353.07 75,552 11,482

0.1543 135 1,654,982 524.52 140,963 11,741

0.1681 193 2,361,418 720 202,913 11,638

0.1484 174 2,352,340 744 202,100 11,639

0.1574 200 2,554,217 731.84 250,037 10,215

0.1544 180 2,331,493 647 219,258 10,634

0.1585 208 2,613,678 744 247,038 10,580

0.1568 138 1,748,632 569.8 165,403 10,572

0.1505 150 2,007,119 620.67 188,658 10,639
0.1525 177 2,305,581 698.16 216,228 10,663

0.1372 178 2,594,308 744 245,615 10,562

0.1428 159 2,212,965 666.44 209,178 10,579

0.1466 168 2,293,841 674.64 216,812 10,580

0.152 99 1,328,153 385.04 126,840 10,471

0.1456 87 1,140,370 381.34 105,213 10,839

0.2151 296 2,735,985 722.05 245,468 11,146

0.181 254 2,799,004 744 260,018 10,765

0.158 159 1,978,230 649.79 193,354 10,231

0.1554 177 2,284,852 741.98 224,860 10,161

0.1563 169 2,162,265 720 207,835 10,404

0.1661 211 2,539,207 744 239,608 10,597

0.1516 195 2,566,939 718.98 252,325 10,173

0.1586 189 2,372,039 721.81 247,945 9,567

0.1548 183 2,368,840 740.98 253,008 9,363

0.1495 170 2,280,336 720 245,520 9,288

0.1529 173 2,254,780 744 241,973 9,318

0.1486 134 1,825,572 720 200,270 9,116

0.1501 159 2,116,284 742.98 234,175 9,037

0.1535 167 2,176,396 743.55 247,650 8,788

0.1548 141 1,820,867 669 207,097 8,792

0.1563 144 1,847,128 725.02 210,936 8,757

0.1562 161 2,040,399 714.31 234,157 8,714

0.2077 135 1,322,417 520.81 144,265 9,167

0.1794 178 2,009,200 720 216,581 9,277

0.2116 267 2,470,418 744 248,345 9,948

0.1519 185 2,450,482 744 246,126 9,956

0.156 107 1,365,926 472.58 139,003 9,827

0.1649 141 1,730,641 612.83 181,094 9,557 0 N/A

0.02271 26,317 55.38 361 72,899

0.1664 183 2,206,880 742.44 225,944 9,767

0.1586 162 2,032,770 671.42 211,437 9,614

0.1783 10 108,880 50.02 11,576 9,406 0 N/A

0.1654 109 1,290,960 497.12 137,918 9,360

0.1728 183 2,189,853 694.66 225,140 9,727

0.1519 168 2,189,803 664.63 221,009 9,908

0.1538 189 2,477,679 743.97 250,671 9,884

0.1412 161 2,327,695 720 238,787 9,748

0.1654 166 2,114,132 727 223,987 9,439

0.1565 127 1,657,512 603.86 167,799 9,878

0.1423 87 1,317,851 479.5 131,561 10,017

0.146 157 1,988,300 683.14 192,989 10,303
0.1491 151 2,051,788 670.07 210,426 9,751

0.1604 165 2,148,311 744 221,774 9,687

0.207 175 1,839,460 717.24 186,477 9,864

0.1492 36 428,290 190.64 39,146 10,941

0.1819 193 2,180,482 701.97 199,632 10,922

0.1679 188 2,294,112 743.97 213,060 10,767

0.1664 180 2,266,283 742 211,819 10,699

0.1963 191 2,145,676 719.95 199,943 10,731

0.1781 91 1,099,720 380.07 104,304 10,543

0.1717 153 1,870,717 632.82 177,079 10,564

0.1569 164 2,110,046 744 202,419 10,424 0 N/A

0.14840 8648 10,788

0.1418 74 1,054,960 335 91,447 11,536

0.1472 191 2,606,034 719 230,051 11,328

0.1501 231 3,060,575 744 270,873 11,299

0.1438 215 2,986,792 720 269,490 11,083

0.1421 195 2,749,728 727.75 263,858 10,421

0.1453 213 2,918,161 744 281,654 10,361

0.1412 125 1,763,004 507.5 184,103 9,576

0.1409 191 2,716,335 744 289,901 9,370

0.1342 168 2,494,980 720 267,406 9,330

0.1334 191 2,862,450 742.75 293,899 9,740

0.1357 160 2,347,445 527.5 211,541 11,097

0.141508 0.51 7,550

0.1364 31 442,359 137 36,415 12,148

0.1403 211 3,002,597 720 252,251 11,903

0.1333 137 2,046,414 579.5 188,388 10,863

0.1326 194 2,910,911 720 273,758 10,633

0.1358 206 3,039,079 744 284,847 10,669

0.1384 233 3,355,347 744 312,238 10,746

0.135 205 3,026,058 720 287,041 10,542

0.1365 165 2,428,816 697.75 231,760 10,480

0.1385 176 2,529,263 720 241,891 10,456

0.1448 227 3,163,909 739 306,713 10,316

0.1402 223 3,168,500 684.25 292,420 10,835

0.1398 180 2,612,021 644.25 234,591 11,134

0.1384 157 2,282,935 632 239,496 9,532

0.1327 206 3,099,332 720 304,508 10,178

0.1321 171 2,607,145 669.75 271,205 9,613

0.1223 178 2,922,276 720 309,122 9,453

0.1004 151 3,010,231 743 323,895 9,294

0.0783 114 2,880,509 744 302,535 9,521

0.0818 113 2,773,519 720 295,148 9,397
0.0894 126 2,829,342 744 301,273 9,391

0.079 106 2,696,948 719.75 284,345 9,485

0.0802 113 2,862,405 744 303,104 9,444

0.0976 101 2,243,219 744 228,502 9,817

0.117 44 790,856 330.75 78,216 10,111

0.0999 27 580,252 218.25 55,409 10,472 0 N/A

0.0984 39 789,693 359 74,826 10,554

0.0938 82 1,873,602 682 170,815 10,969

0.0812 85 2,110,042 635.5 206,061 10,240

0.0796 104 2,595,030 744 256,646 10,111

0.0787 75 1,890,999 575.25 186,143 10,159

0.0783 74 1,877,442 578.75 184,244 10,190

0.0735 10 247,608 88.75 25,028 9,893 0 N/A 0 N/A

0.1213 31 463,453 179 50,133 9,244

0.1208 169 2,787,264 744 278,551 10,006

0.0961 136 2,815,769 720 278,378 10,115

0.0754 110 2,903,664 744 278,197 10,437

0.0769 108 2,796,829 677.25 265,864 10,520

0.0811 124 3,065,660 744 289,453 10,591

0.0817 120 2,901,729 743.75 275,456 10,534

0.0653 31 939,612 228.5 88,276 10,644

0.0726 58 1,555,264 463.75 147,401 10,551

0.1014 134 2,695,528 720 270,775 9,955

0.072 107 2,967,627 744 293,058 10,126

0.1426 213 2,997,108 744 286,213 10,472

0.1466 207 2,806,216 661.75 256,792 10,928

0.1471 224 3,039,727 744 271,638 11,190

0.147 188 2,568,196 714.75 227,274 11,300

0.1501 244 3,231,313 744 286,162 11,292

0.1446 188 2,598,389 620 234,726 11,070

0.1399 157 2,236,676 612 216,855 10,314

0.1453 226 3,090,500 744 298,246 10,362

0.1395 146 2,090,555 597 227,086 9,206 0 N/A 0 N/A

0.1288 72 1,095,939 351.25 109,727 9,988

0.1342 203 3,008,796 743 294,243 10,226

0.143 139 1,913,803 592.75 225,951 8,470

0.1474 248 3,371,520 742.75 268,183 12,572

0.1403 210 2,979,224 720 250,340 11,901

0.1336 195 2,892,551 744 268,935 10,756
0.1326 195 2,914,444 720 274,077 10,634

0.1358 201 2,958,948 744 277,440 10,665

0.1384 218 3,143,677 744 292,519 10,747

0.1355 176 2,595,398 652.75 246,137 10,545

0.1362 183 2,691,538 744 257,266 10,462

0.1385 190 2,725,525 720 260,396 10,467

0.1446 198 2,775,092 648.75 268,515 10,335

0.1403 196 2,778,969 667 258,373 10,756

0.1403 184 2,670,040 669.25 242,294 11,020

0.1392 182 2,624,096 744 286,932 9,145

0.14775 68,040 23 7,295 9,327

0.1321 169 2,603,530 700 275,787 9,440

0.1223 169 2,766,500 720 292,846 9,447

0.1003 147 2,927,572 744 314,800 9,300

0.0783 114 2,938,184 744 307,480 9,556

0.0818 104 2,597,809 720 276,762 9,386

0.0855 98 2,352,322 681.25 253,494 9,280

0.079 102 2,617,397 720 276,400 9,470

0.0802 111 2,816,924 744 298,735 9,430

0.0976 88 2,046,024 744 211,154 9,690

0.0904 45 1,146,569 562.25 123,495 9,284

0.084 39 1,048,173 462.5 105,204 9,963

0.0711 49 1,607,895 720 162,515 9,894

0.0794 48 1,422,206 598.25 146,035 9,739

0.0927 82 2,056,154 719.5 193,466 10,628

0.0756 88 2,367,803 741.25 237,656 9,963

0.0796 98 2,468,140 744 245,153 10,068

0.0698 77 2,172,677 720 219,322 9,906

0.0676 72 2,144,564 715.75 215,897 9,933

0.0397 39 2,020,134 720 232,130 8,703

0.0331 31 1,920,795 744 215,654 8,907

0.0284 19 1,336,885 542 134,107 9,969 0 N/A

0.0981 27 599,094 258 61,683 9,712

0.0778 65 1,716,814 487 170,566 10,065

0.0754 106 2,804,715 744 269,317 10,414

0.0741 110 2,967,413 720 280,414 10,582

0.0739 92 2,541,555 642.5 238,818 10,642

0.0757 99 2,606,838 659.5 246,781 10,563

0.0405 60 3,044,045 703.25 269,847 11,281

0.0551 73 2,803,160 742.5 255,532 10,970

0.0716 32 937,602 238.25 91,866 10,206

0.0706 99 2,811,264 722 277,146 10,144

0.1574 316 4,005,110 744 429,020 9,335
0.1579 289 3,639,660 672 382,953 9,504

0.1466 265 3,601,095 726.48 374,659 9,612

0.1439 266 3,702,745 715.45 370,502 9,994

0.1405 213 3,000,777 558.43 285,891 10,496

0.1297 233 3,629,260 655.18 350,421 10,357

0.1337 284 4,251,396 744 407,781 10,426

0.1296 262 4,071,612 716.34 389,715 10,448

0.1349 272 4,038,837 718.77 387,375 10,426

0.1382 259 3,775,551 706.93 368,235 10,253

0.1306 258 3,930,040 720 386,580 10,166

0.1433 282 3,929,537 710.69 390,514 10,062

0.1315 187 2,854,641 548.95 279,345 10,219

0.1336 240 3,577,728 672 350,646 10,203

0.1236 228 3,640,496 744 354,051 10,282

0.1376 80 1,173,100 231.47 114,510 10,245

0.1316 99 1,451,768 303 141,015 10,295

0.1256 244 3,867,365 720 381,646 10,133

0.1309 266 4,067,268 744 398,101 10,217

0.1253 257 4,100,265 744 404,351 10,140

0.133 245 3,709,696 714.02 363,702 10,200

0.1375 265 3,870,586 741.53 376,189 10,289

0.1241 232 3,718,455 718.16 367,115 10,129

0.1267 265 4,160,991 743.98 413,318 10,067

0.1395 294 4,193,540 744 421,478 9,950

0.1469 258 3,491,439 671.61 349,857 9,980

0.1437 193 2,782,154 596.8 274,435 10,138

0.1263 240 3,758,677 720 369,085 10,184

0.1239 248 3,965,661 744 380,770 10,415

0.1288 249 3,966,432 719.8 384,346 10,320

0.132 265 4,164,842 744 400,088 10,410

0.13 249 3,983,286 744 385,472 10,334

0.1195 213 3,669,735 720 352,600 10,408

0.1094 194 3,650,124 744 349,764 10,436

0.1112 173 3,197,617 720 319,396 10,011

0.1183 121 2,174,105 517.5 216,805 10,028

0.106 96 1,888,709 477.53 189,265 9,979 0 N/A

0.1222 37 582,116 157.58 57,225 10,172

0.1502 189 2,708,971 718.06 264,338 10,248

0.1645 223 2,873,793 742.13 282,767 10,163

0.1487 209 2,938,648 720 287,446 10,223

0.1447 200 2,906,773 693.29 285,190 10,192

0.1434 221 3,193,008 744 315,692 10,114

0.1454 201 2,843,289 720 277,862 10,233
0.1599 223 2,911,163 744 281,735 10,333

0.1432 184 2,676,982 685.72 257,996 10,376 0 N/A 0 N/A

0.04430 1,430 5.082 N/A

0 N/A 0 N/A

0.123 57 923,558 209.08 88,846 10,395

0.1228 218 3,561,499 718.08 347,559 10,247

0.1274 263 4,116,894 744 401,680 10,249

0.1312 260 3,944,913 743.93 380,478 10,368

0.1402 132 1,893,586 383.71 183,655 10,311 0 N/A 0 N/A 0 N/A

0.1479 324 4,371,464 744 434,795 10,054

0.1389 262 3,763,039 672 376,178 10,003

0.1423 294 4,130,725 744 412,954 10,003

0.1385 277 3,993,770 720 398,310 10,027

0.1473 204 2,768,336 518.6 279,409 9,908

0.1332 265 3,965,406 720 405,909 9,769

0.1376 286 4,149,649 744 419,758 9,886

0.1444 282 4,003,757 740.73 406,204 9,857

0.1425 282 3,955,739 720 403,741 9,798

0.1509 307 4,057,812 744 409,986 9,897

0.1374 270 3,923,748 720 393,515 9,971

0.1554 306 3,914,121 693.59 393,164 9,955

0.14 285 4,046,714 744 407,517 9,930

0.1368 237 3,440,361 656.4 345,077 9,970

0.1391 252 3,596,785 744 361,765 9,942

0.144 200 2,783,538 562.82 282,343 9,859

0.1279 172 2,712,220 583.34 277,159 9,786

0.1236 227 3,669,172 720 377,027 9,732

0.1223 228 3,704,927 744 379,983 9,750

0.1388 264 3,787,009 744 389,792 9,715

0.1325 242 3,653,440 717.7 375,003 9,742

0.1308 242 3,695,175 744 375,004 9,854

0.1208 218 3,593,990 720 360,106 9,980

0.1236 246 3,951,255 744 392,758 10,060

0.1241 248 3,972,659 744 392,183 10,130

0.1238 170 2,732,032 552.43 274,755 9,944

0.1609 26 327,783 73.88 31,186 10,511

0.136 242 3,545,612 701.07 349,677 10,140

0.1233 236 3,769,191 743.98 381,437 9,882
0.1247 234 3,765,245 720 390,318 9,647

0.1274 243 3,890,670 740.38 399,774 9,732

0.1315 247 3,771,270 744 383,823 9,826

0.1186 190 3,211,187 660.05 327,294 9,811

0.1187 183 3,128,915 665.68 315,123 9,929

0.1103 181 3,274,792 720 326,279 10,037

0.1053 59 1,146,819 266.45 110,017 10,424

0.03030 1,072 5.450 N/A

0 N/A 0 N/A 0 N/A

0.1364 148 2,179,726 562.81 214,345 10,169

0.1331 199 3,007,555 720 297,956 10,094

0.1221 203 3,323,514 744 326,798 10,170

0.1207 200 3,295,283 744 323,520 10,186

0.1223 171 2,780,788 720 268,039 10,375

0.1208 189 3,104,019 744 297,768 10,424

0.1199 194 3,162,482 720 308,304 10,258

0.06621 8,731 8.25 705 12,385 0 N/A 0 N/A 0 N/A 0 N/A

0.1161 55 905,631 205.12 88,241 10,263

0.1207 208 3,459,117 697.73 331,073 10,448

0.1232 259 4,173,800 741.25 388,963 10,731

0.1203 212 3,634,208 691.57 336,652 10,795

0.1131 210 3,818,453 716.72 350,935 10,881 0 N/A 0 N/A 0 N/A

0.1813 300 3,315,180 744 404,082 8,204

0.1762 126 1,418,061 309.66 157,880 8,982 0 N/A

0.1677 221 2,488,955 637.43 249,951 9,958

0.217 328 2,958,477 648.37 312,803 9,458

0.2055 339 3,274,255 720 352,246 9,295

0.2271 414 3,621,307 742.45 380,931 9,506

0.2212 392 3,527,521 731.82 382,191 9,230

0.2043 324 3,168,308 720 342,755 9,244

0.1715 289 3,361,681 744 365,052 9,209

0.1707 298 3,479,544 720 370,545 9,390

0.1833 300 3,261,860 744 392,959 8,301

0.191 314 3,328,030 744 391,441 8,502
0.1876 281 2,990,416 672 354,729 8,430

0.2409 315 2,573,859 537.89 267,810 9,611

0.2085 397 3,766,699 720 361,354 10,424

0.1947 381 3,891,909 744 382,149 10,184

0.1855 352 3,779,588 720 368,111 10,268

0.1785 334 3,694,211 708.53 359,613 10,273

0.1852 355 3,811,320 744 376,853 10,114

0.2039 354 3,459,642 710.83 349,821 9,890

0.2125 353 3,329,007 675.52 336,614 9,890

0.1865 330 3,523,698 720 373,214 9,441

0.1795 164 1,713,133 409.81 185,156 9,252

0.1999 352 3,519,049 744 390,413 9,014

0.2061 323 3,130,422 672 353,756 8,849

0.2076 370 3,562,677 744 400,911 8,886

0.1929 300 3,083,770 718.95 371,443 8,302

0.2022 293 2,825,101 688.06 356,993 7,914

0.185 313 3,352,054 720 379,699 8,828

0.1843 309 3,321,367 732.15 379,674 8,748

0.1942 335 3,432,398 742.99 399,329 8,595

0.1991 327 3,276,457 720 386,357 8,480

0.2001 329 3,283,374 722.45 385,956 8,507

0.1955 326 3,328,786 720 389,810 8,540

0.1991 341 3,419,376 744 404,629 8,451

0.2136 67 618,175 143.97 76,088 8,125

0.0420 3,946 35.60 N/A

0.1502 212 2,819,755 724.4 316,161 8,919

0.1411 217 3,048,555 667.85 325,785 9,358

0.1441 249 3,430,494 743.9 377,553 9,086

0.1416 240 3,392,437 720 376,757 9,004

0.1413 250 3,502,763 731.93 389,065 9,003

0.1288 177 2,737,806 616.59 305,926 8,949

0.1325 221 3,333,419 720 382,269 8,720

0.1303 223 3,418,528 744 396,231 8,628

0.1247 200 3,192,459 719.53 370,266 8,622

0.1224 209 3,406,920 744 392,038 8,690

0.1249 205 3,285,791 744 376,290 8,732

0.1286 197 3,058,255 671.82 348,414 8,778

0.1286 225 3,505,621 744 397,583 8,817

0.1218 72 1,126,526 285.9 124,871 9,022

0.1298 230 3,547,375 744 400,477 8,858

0.1307 218 3,335,125 720 370,847 8,993

0.1451 260 3,579,637 743.98 399,021 8,971

0.142 260 3,657,470 744 403,107 9,073

0.1264 154 2,356,652 509.67 257,083 9,167
0.1279 183 2,816,002 687.31 310,500 9,069

0.1269 202 3,194,119 720 361,331 8,840

0.1301 219 3,367,766 743.98 387,823 8,684

0.1987 373 3,740,401 725.83 364,291 10,268

0.1761 304 3,455,429 672 337,481 10,239

0.1722 350 4,073,818 744 366,304 11,121

0.1726 292 3,367,051 710.2 325,675 10,339

0.1819 217 2,366,795 578.68 233,475 10,137

0.1867 180 1,867,609 480.56 182,668 10,224

0.2155 406 3,708,917 744 365,394 10,150

0.2125 381 3,560,769 709.97 360,815 9,869

0.1744 263 2,855,476 701.18 295,117 9,676

0.1905 403 4,200,479 730.83 368,580 11,396

0.1916 357 3,600,269 679.95 330,753 10,885

0.1765 306 3,450,181 675.88 345,433 9,988

0.1673 305 3,600,920 711.96 359,321 10,021

0.1774 316 3,547,104 672 353,787 10,026

0.2044 272 2,600,894 522.72 262,995 9,890

0.1959 366 3,738,904 720 367,892 10,163

0.1615 231 2,787,091 587.89 264,719 10,528

0.1742 268 2,987,259 580.6 280,257 10,659

0.1788 359 4,007,069 744 375,310 10,677

0.1724 322 3,704,579 684.95 354,572 10,448

0.1735 303 3,433,433 720 344,442 9,968

0.1675 269 3,153,512 696.5 332,298 9,490

0.1689 300 3,549,221 720 375,761 9,445

0.1698 291 3,403,057 681.54 351,969 9,669

0.1732 70 806,767 169.5 82,910 9,731 0 N/A

0.1173 47 610,770 237.41 63,935 9,553

0.195 342 3,509,345 720 377,195 9,304

0.2039 375 3,669,025 744 397,206 9,237

0.1865 340 3,645,525 719.85 392,973 9,277

0.173 320 3,680,339 724.03 383,810 9,589

0.1731 340 3,930,570 739.29 403,572 9,739

0.1679 327 3,889,026 720 392,773 9,901

0.1645 303 3,660,555 704.95 370,965 9,868

0.1627 266 3,171,927 676.3 326,894 9,703

0.173 336 3,879,838 744 401,280 9,669

0.1752 306 3,485,186 744 382,858 9,103

0.1796 310 3,408,478 675 345,605 9,862

0.1653 127 1,535,670 335.26 161,999 9,480

0.1844 293 3,005,769 647.08 313,338 9,593

0.1908 348 3,628,598 744 373,562 9,714
0.1549 281 3,617,682 720 371,982 9,725

0.1542 289 3,726,004 715.88 384,066 9,701

0.1596 299 3,729,401 718.22 385,194 9,682

0.1833 330 3,588,062 717.43 369,723 9,705

0.1732 330 3,807,217 744 394,029 9,662

0.153 282 3,689,961 720 386,199 9,555

0.1651 310 3,736,488 744 390,141 9,577

0.1639 294 3,576,756 744 371,796 9,620

0.1554 265 3,413,231 671.98 354,307 9,634

0.1612 307 3,806,915 744 405,607 9,386

0.1563 284 3,635,214 720 391,053 9,296

0.1618 304 3,760,813 744 398,449 9,439

0.1427 262 3,666,307 720 373,316 9,821

0.1547 293 3,789,395 737.98 394,017 9,617

0.1616 297 3,662,399 735.15 389,019 9,414

0.1519 271 3,561,583 717.62 373,865 9,526

0.1515 272 3,581,419 743.97 385,695 9,286

0.1639 282 3,424,329 720 369,685 9,263

0.1611 284 3,516,534 744 389,640 9,025

0.0552 120 4,327,612 744 443,893 9,749

0.0522 108 4,106,964 672 426,488 9,630

0.0525 48 1,869,396 307.5 189,637 9,858

0.0824 74 2,098,274 453.92 208,680 10,055

0.0503 124 4,915,222 744 497,815 9,874

0.0516 120 4,713,953 716.76 478,768 9,846

0.05 124 4,974,855 744 501,562 9,919

0.0515 102 4,042,960 669.47 407,823 9,914

0.0512 103 4,006,892 720 409,912 9,775

0.0512 112 4,395,076 744 449,009 9,788

0.052 88 3,432,113 616.8 353,541 9,708

0.0505 114 4,528,342 744 471,243 9,609

0.0508 117 4,638,129 744 451,707 10,268

0.0539 89 3,367,473 568.31 331,696 10,152

0.0517 99 3,868,652 744 387,526 9,983

0.0519 93 3,659,542 706.05 372,008 9,837

0.0507 100 3,997,403 743.92 410,099 9,747

0.052 120 4,619,151 720 464,396 9,947

0.0504 112 4,488,430 744 446,600 10,050

0.0507 103 4,091,390 669.25 418,170 9,784

0.0502 101 4,048,938 720 412,696 9,811

0.0505 80 3,235,416 744 324,417 9,973

0.0493 81 3,329,738 720 331,404 10,047

0.0605 135 4,485,492 744 454,022 9,879

0.0655 148 4,529,219 744 459,194 9,863
0.0667 125 3,756,713 672 382,552 9,820

0.0658 16 499,464 98.67 49,756 10,038

0.0556 64 2,409,685 461.41 247,577 9,733

0.0475 103 4,401,882 744 457,959 9,612

0.0428 91 4,263,013 720 440,798 9,671

0.0424 100 4,719,674 744 494,199 9,550

0.0422 97 4,615,332 744 487,147 9,474

0.0447 93 4,166,060 720 437,926 9,513

0.0429 79 3,712,064 744 376,549 9,858

0.0462 56 2,520,488 551.24 257,424 9,791

0.0428 75 3,535,826 744 358,909 9,852

0.0436 40 1,859,000 489.65 186,076 9,991

0.0458 48 2,239,727 458 236,968 9,452

0.0424 87 4,155,891 744 445,585 9,327

0.0413 78 3,786,199 720 411,108 9,210

0.053 87 3,361,654 652.64 354,050 9,495

0.0645 132 4,153,045 720 441,448 9,408

0.0663 135 4,127,295 743 431,670 9,561

0.0649 138 4,280,659 744 419,865 10,195

0.0638 61 1,876,818 405.64 187,530 10,008

0.0608 107 3,525,287 680.48 356,434 9,890

0.0634 128 4,088,532 720 419,424 9,748

0.0637 92 2,917,892 744 300,423 9,713

0.0645 90 2,826,426 744 303,898 9,301

0.0647 85 2,659,054 672 284,201 9,356

0.0642 124 3,899,349 744 414,045 9,418

0.064 103 3,166,798 592.09 338,061 9,368

0.0659 146 4,449,122 744 469,153 9,483

0.0651 117 3,629,049 652.3 382,996 9,475

0.0661 118 3,610,089 685.63 381,621 9,460

0.0691 130 3,783,765 744 403,868 9,369

0.0745 142 3,806,896 720 415,185 9,169

0.0747 131 3,525,541 744 395,779 8,908

0.0766 93 2,454,463 595.09 273,380 8,978

0.0743 143 3,857,686 744 434,320 8,882

0.0531 104 3,903,931 744 427,530 9,131

0.0527 96 3,633,331 672 408,307 8,899

0.0528 106 4,010,583 744 461,140 8,697

0.0755 105 3,125,372 645.43 365,698 8,546

0.0527 109 4,139,065 744 478,915 8,643

0.0736 155 4,164,159 720 476,514 8,739

0.0784 155 3,962,131 672.28 425,908 9,303

0.078 178 4,566,050 744 490,130 9,316

0.0783 148 3,801,920 720 409,432 9,286
0.0792 142 3,606,183 673.12 396,813 9,088

0.0758 65 1,710,253 312.58 186,962 9,148

0.0584 58 2,127,024 399.27 227,934 9,332

0.0521 102 3,996,428 711.85 422,160 9,467

0.0519 101 3,938,700 672 422,064 9,332

0.0506 89 3,553,394 744 372,828 9,531

0.0503 91 3,617,311 720 382,147 9,466

0.0503 94 3,794,070 743.73 402,944 9,416

0.0525 111 4,226,094 720 455,811 9,272

0.0504 104 4,186,680 744 432,168 9,688

0.0499 95 3,824,560 636.34 395,758 9,664

0.0506 99 3,953,826 720 409,237 9,661

0.053 68 2,663,042 617.21 263,287 10,115

0.0492 82 3,356,456 720 329,433 10,189

0.0525 118 4,528,850 744 443,130 10,220

0.0509 122 4,798,828 744 465,057 10,319

0.0555 91 3,367,117 575.11 324,658 10,371

0.0515 97 3,848,590 654.3 374,776 10,269

0.0534 128 4,800,030 720 465,763 10,306

0.056 135 4,797,105 744 456,566 10,507

0.0645 158 4,907,177 720 463,445 10,588

0.0639 162 5,076,180 744 481,207 10,549

0.064 162 5,056,273 744 483,037 10,468

0.0664 150 4,541,183 720 434,715 10,446

0.0635 131 4,169,043 744 377,739 11,037

0.0635 88 2,805,934 551.13 263,342 10,655

0.0634 105 3,326,128 687.68 310,391 10,716

0.064 13 396,512 82.42 35,837 11,064 0 N/A

0.0555 88 3,158,602 583.81 301,659 10,471

0.0512 106 4,204,320 720 400,131 10,507

0.051 110 4,388,364 744 412,666 10,634

0.0516 118 4,605,212 720 431,746 10,666

0.0479 78 3,410,746 597.25 328,663 10,378

0.0415 99 4,817,282 744 456,435 10,554

0.0457 94 4,186,129 720 393,771 10,631

0.0437 90 4,199,765 744 390,952 10,742

0.0431 93 4,393,366 720 404,915 10,850

0.0434 56 2,674,189 627.55 236,184 11,322

0.0452 53 2,451,926 544.56 216,602 11,320

0.0431 37 1,761,487 403.83 158,542 11,111

0.0412 89 4,391,762 744 410,187 10,707

0.0433 85 3,996,585 650.43 373,214 10,709

0.0487 107 4,484,966 718.57 420,227 10,673
0.0535 111 4,233,610 656.88 397,259 10,657

0.0502 120 4,821,249 744 449,154 10,734

0.0511 104 4,184,762 675.5 386,272 10,834

0.0521 107 4,167,801 635.82 386,764 10,776

0.052 116 4,532,573 744 421,548 10,752

0.0541 102 3,828,326 720 351,058 10,905

0.0517 121 4,745,595 744 449,524 10,557

0.0411 68 3,300,283 744 375,380 8,792

0.0411 63 3,059,055 672 343,275 8,911

0.0409 69 3,398,231 744 387,953 8,759

0.0479 61 2,911,024 692.1 320,293 9,089

0.0399 71 3,563,497 744 405,415 8,790

0.0398 68 3,448,220 674.16 397,449 8,676

0.0395 79 3,992,200 744 453,590 8,801

0.0398 80 4,007,408 743.1 448,804 8,929

0.0431 49 2,322,891 490.24 262,661 8,844

0.0399 75 3,747,118 744 436,895 8,577

0.0401 71 3,545,401 720 412,466 8,596

0.04 74 3,699,791 744 438,722 8,433

0.0423 72 3,404,269 744 426,639 7,979

0.0402 66 3,298,479 672 391,387 8,428

0.0398 66 3,320,280 744 390,914 8,494

0.042 66 3,126,543 720 394,470 7,926

0.0654 89 2,757,917 680.59 324,579 8,497

0.0647 115 3,547,814 720 414,810 8,553

0.064 115 3,587,810 744 420,754 8,527

0.0654 123 3,751,249 744 431,687 8,690

0.0642 110 3,431,669 720 393,819 8,714

0.0645 94 2,916,334 698.08 324,857 8,977

0.0541 14 508,810 149.55 54,961 9,258

0.0443 63 2,913,255 659.65 325,492 8,950

0.0452 58 2,660,745 584.7 297,978 8,929

0.0457 65 2,860,092 625.62 317,201 9,017

0.0448 72 3,279,996 741.77 363,451 9,025

0.0456 70 3,153,946 646.7 349,010 9,037

0.044 78 3,526,609 744 389,918 9,044

0.0443 81 3,632,845 720 398,167 9,124

0.0441 85 3,849,106 744 421,136 9,140

0.0446 87 3,897,155 744 417,044 9,345

0.0448 75 3,351,978 714.47 364,890 9,186

0.045 67 2,975,578 744 320,654 9,280

0.0448 60 2,658,983 720 287,473 9,250

0.0459 27 1,178,119 291.45 129,751 9,080 0 N/A
0.0491 33 1,398,649 379.9 155,844 8,975

0.0428 68 3,167,731 744 358,998 8,824

0.0429 43 1,987,628 478.87 216,339 9,188

0.0421 60 2,843,311 645.02 299,271 9,501

0.044 60 2,803,282 579.39 287,345 9,756

0.0419 60 2,901,276 620.17 296,431 9,787

0.0408 73 3,586,500 743.78 367,832 9,750

0.0415 60 2,898,973 662.81 293,043 9,893

0.0415 69 3,298,108 744 340,986 9,672

0.0418 69 3,303,817 720 344,093 9,602

0.0415 52 2,516,536 688.48 261,447 9,625

0.0492 19 853,102 212.84 87,337 9,768

0.0457 19 881,131 216.97 89,106 9,889

0.0404 75 3,695,767 744 389,512 9,488

0.0403 74 3,723,907 695.54 382,575 9,734

0.0397 75 3,771,739 699.62 376,120 10,028

0.041 66 3,289,115 609.28 337,894 9,734

0.0392 78 3,975,638 744 410,733 9,679

0.0394 75 3,774,686 744 388,084 9,726

0.0416 61 2,924,790 510.52 301,896 9,688

0.03880 1,126 2.540 N/A

0.0416 52 2,512,982 603.73 265,162 9,477

0.0395 75 3,795,003 744 410,460 9,246

0.1857 309 3,298,232 744 344,383 9,577

0.1908 271 2,787,706 664.92 291,787 9,554

0.1894 327 3,409,643 744 354,468 9,619

0.1734 290 3,292,946 720 331,003 9,948

0.166 62 687,341 176.52 68,059 10,099

0.1744 294 3,320,844 696.01 329,662 10,073

0.175 332 3,774,430 744 363,130 10,394

0.182 339 3,693,906 732.73 355,997 10,376

0.1804 327 3,601,332 720 351,284 10,252

0.1865 352 3,764,746 744 371,688 10,129

0.1902 355 3,723,440 720 364,429 10,217

0.1871 217 2,253,331 492.08 227,407 9,909

0.1916 78 777,161 189.7 76,649 10,139

0.1951 316 3,206,791 671.51 322,754 9,936

0.187 159 1,551,507 387.44 153,927 10,079

0.1965 319 3,197,628 686.75 318,792 10,030

0.1945 350 3,541,435 733.06 349,275 10,139

0.1898 344 3,607,458 720 352,475 10,235

0.1923 365 3,781,246 744 371,518 10,178

0.193 357 3,655,607 741.82 362,106 10,095

0.1911 329 3,396,031 710.43 338,343 10,037
0.1878 314 3,286,119 702.43 327,769 10,026

0.1897 229 2,287,411 511.49 228,919 9,992

0.1884 350 3,703,538 744 372,452 9,944

0.1899 357 3,752,770 744 375,649 9,990

0.1946 304 3,117,545 672 316,722 9,843

0.1833 328 3,532,172 734 356,762 9,901

0.1824 312 3,407,293 717.33 339,376 10,040

0.17979 105,916 23.93 10,550 10,039

0.1827 286 3,060,577 685.57 296,847 10,310

0.1808 355 3,927,632 744 378,236 10,384

0.194 365 3,726,554 734.48 366,993 10,154

0.1911 326 3,365,733 690.08 334,124 10,073

0.2108 381 3,576,356 744 360,552 9,919

0.2104 361 3,392,671 719.97 342,184 9,915

0.2023 347 3,416,432 744 349,602 9,772

0.2104 370 3,469,084 732.07 354,988 9,772

0.2007 325 3,213,272 696 331,182 9,702

0.1948 230 2,298,060 531.37 229,536 10,012

0.1851 292 3,105,907 720 314,324 9,881

0.1862 319 3,372,001 744 342,401 9,848

0.1829 289 3,110,465 720 309,477 10,051

0.1948 352 3,584,713 729.45 362,056 9,901

0.1888 347 3,656,126 744 362,790 10,078

0.191 140 1,467,156 337.48 144,776 10,134

0.1658 126 1,379,411 335.79 139,638 9,878

0.178 295 3,263,345 714.58 337,461 9,670

0.1812 311 3,405,693 744 357,349 9,530

0.1733 252 2,827,148 729.1 297,537 9,502

0.1736 233 2,637,205 672 277,974 9,487

0.1711 207 2,277,878 585.12 239,212 9,522

0.19 274 2,813,417 695.43 296,495 9,489

0.1776 222 2,396,739 606.25 246,632 9,718

0.1784 257 2,854,693 720 292,747 9,751

0.1829 269 2,896,301 720.25 293,684 9,862

0.1801 278 3,036,977 744 300,862 10,094

0.1914 250 2,633,236 646.9 259,520 10,147

0.01330 948 11.89 12 79,753

0.1708 227 2,547,410 713.07 262,370 9,709

0.1872 302 3,193,594 744 326,822 9,772

0.171 298 3,479,830 732.62 343,508 10,130

0.1722 268 3,107,360 672 307,779 10,096

0.1716 278 3,233,920 647.42 314,802 10,273

0.157 64 788,723 191.32 76,084 10,366

0.1693 308 3,635,074 744 356,224 10,204
0.1737 306 3,497,631 701.75 336,641 10,390

0.1764 345 3,901,360 744 370,513 10,530

0.1763 337 3,823,356 744 365,787 10,452

0.1711 267 3,097,725 631.12 292,973 10,573

0.1766 325 3,675,311 744 375,314 9,793

0.1759 242 2,712,274 557.49 272,239 9,963

0.1756 325 3,702,071 744 382,840 9,670

0.176 329 3,737,469 744 381,508 9,797

0.1726 264 3,046,185 627.06 306,975 9,923

0.1651 250 2,970,091 625.96 294,926 10,071

0.1698 285 3,321,972 706.45 329,354 10,086

0.1674 311 3,702,749 742.84 359,431 10,302

0.1707 310 3,595,398 713.4 344,503 10,436

0.1741 336 3,853,748 744 373,094 10,329

0.1776 329 3,698,309 744 363,816 10,165

0.1751 250 2,849,089 577.4 273,179 10,429

0.1572 77 952,227 221.45 93,042 10,234

0.1664 284 3,428,942 720 344,035 9,967

0.1693 309 3,669,844 742.75 363,665 10,091

0.1767 287 3,328,981 734.38 330,181 10,082

0.1769 267 3,063,503 672 307,918 9,949

0.1777 326 3,663,058 744 368,413 9,943

0.1718 220 2,515,423 554.78 251,408 10,005

0.177 307 3,506,832 744 352,170 9,958

0.1742 313 3,549,515 708.88 350,413 10,130

0.1793 348 3,882,075 744 382,655 10,145

0.1819 357 3,923,837 742.93 379,321 10,344

0.179 147 1,644,256 337.53 160,416 10,250

0.1537 137 1,560,557 394.94 146,766 10,633

0.1825 320 3,489,531 719.97 343,789 10,150

0.1648 298 3,593,102 744 353,838 10,155

0.1731 306 3,485,154 725.52 344,433 10,119

0.1637 252 3,034,390 638.15 300,743 10,090

0.1676 298 3,529,053 743.97 340,590 10,362

0.1673 55 651,605 145.68 62,350 10,451

0.1616 267 3,239,554 700.67 316,888 10,223

0.1674 278 3,274,514 720 314,734 10,404

0.1674 311 3,667,569 714.7 352,313 10,410

0.1761 329 3,700,760 740.78 355,421 10,412

0.1624 109 1,171,419 308.19 114,897 10,195

0.1551 213 2,634,794 591.56 264,531 9,960

0.1605 286 3,547,486 720 352,394 10,067

0.1692 310 3,632,574 744 361,652 10,044

0.1673 263 3,075,376 728.1 306,701 10,027
0.1603 215 2,638,090 666.35 267,061 9,878

0.1617 256 3,123,007 744 317,333 9,841

0.1685 98 1,154,200 289.93 116,395 9,916

0.1619 107 1,291,270 383.68 127,066 10,162

0.1598 176 2,099,041 540.68 205,909 10,194

0.1675 247 2,943,365 744 288,822 10,191

0.1634 252 3,031,430 744 294,435 10,296

0.1726 240 2,738,830 707.65 267,655 10,233

0.155 193 2,431,434 731.8 239,176 10,166

0.1541 150 1,931,511 720 188,078 10,270

0.1533 180 2,317,249 744 229,826 10,083

0.1921 351 3,605,333 744 344,914 10,453

0.1847 206 2,198,385 480.95 212,187 10,361

0.1991 151 1,468,751 316.42 134,913 10,887

0.1812 301 3,306,771 720 336,941 9,814

0.1802 321 3,540,942 744 352,168 10,055

0.1741 295 3,366,726 692.95 331,330 10,161

0.1709 304 3,544,527 729.71 349,373 10,145

0.1718 311 3,614,974 744 361,009 10,014

0.1691 175 2,068,930 432.72 206,670 10,011

0.1832 184 1,909,183 485.22 206,164 9,261

0.197 345 3,490,980 720 361,268 9,663

0.2038 363 3,558,099 744 384,101 9,263

0.2085 364 3,457,869 737.38 368,885 9,374

0.1943 312 3,185,814 666.7 324,178 9,827

0.2066 368 3,551,912 646.77 330,209 10,757

0.1472 38 394,304 133.94 34,662 11,376

0.1815 370 4,058,905 744 362,535 11,196

0.1837 357 3,823,163 707.04 337,001 11,345

0.1854 394 4,243,601 744 378,001 11,226

0.2003 410 4,078,180 744 373,180 10,928

0.1864 359 3,811,969 706.8 343,086 11,111

0.1991 365 3,647,907 744 368,340 9,904

0.1874 314 3,332,076 720 349,110 9,544

0.1877 324 3,407,224 731.87 362,653 9,395

0.1943 290 2,951,086 644.95 314,318 9,389

0.2397 35 296,033 73.7 23,005 12,868

0.237 418 3,516,489 743.03 359,697 9,776

0.2034 361 3,533,893 720 357,468 9,886

0.2012 377 3,730,526 744 368,164 10,133

0.2074 368 3,463,873 673.8 331,783 10,440

0.2102 415 3,948,787 744 381,984 10,338

0.2052 402 3,902,901 732.53 373,072 10,462

0.194 361 3,704,682 720 358,073 10,346
0.1965 374 3,776,337 744 368,044 10,261

0.2076 270 2,611,303 551.64 254,090 10,277

0.2051 367 3,562,463 744 365,681 9,742

0.1985 351 3,503,606 734.69 359,551 9,744

0.1945 307 3,114,661 664.62 319,226 9,757

0.1912 333 3,452,878 724.05 336,942 10,248

0.1811 284 3,061,995 658.92 289,892 10,563

0.1707 99 1,141,720 278.43 103,427 11,039

0.1971 263 2,589,825 560.03 243,380 10,641

0.1935 361 3,694,293 702.23 347,290 10,637

0.1983 388 3,901,183 744 367,897 10,604

0.1878 292 2,997,915 638.17 281,712 10,642

0.1954 351 3,559,149 744 352,627 10,093

0.1938 330 3,382,477 720 354,441 9,543

0.1836 306 3,295,934 732.86 351,664 9,372

0.1832 240 2,541,808 647.54 269,213 9,442

0.1799 134 1,477,846 372.93 157,238 9,399

0.1905 155 1,569,406 385.6 166,578 9,421

0.1823 283 3,078,277 720 315,252 9,764

0.1904 319 3,291,843 744 324,809 10,135

0.1822 275 2,921,531 707.37 276,936 10,549

0.1957 320 3,244,272 744 309,562 10,480

0.2007 322 3,197,486 744 304,044 10,517

0.1813 274 2,954,710 707.56 282,977 10,442

0.1712 241 2,730,191 688.25 267,770 10,196

0.1761 245 2,741,588 720 283,571 9,668

0.181 302 3,280,408 744 328,867 9,975
Max Gross 

Heat Rate 

(Btu/kWh)

 Operating 

Status Unit Type

 Fuel Type 

(Primary)

 Fuel Type 

(Secondary)

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

10,277 Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

10,450 Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

9,799 Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

11,202 Operating Tangentially-firedCoal

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas
Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

12,219 Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

72,899 Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

12,148 Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

12,572 Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

10,496 Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

12,385 Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal
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Operating Tangentially-firedCoal

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10,424 Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal
Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

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Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

Operating Tangentially-firedCoal

11,396 Operating Tangentially-firedCoal

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas
Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

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Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

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Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

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Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

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Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

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10,268 Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas
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Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

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Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas
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Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

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11,322 Operating Dry bottom wall-fired boiler Coal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas
Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Tangentially-firedCoal Pipeline Natural Gas

10,028 Operating Tangentially-firedCoal Pipeline Natural Gas

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal
Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

79,753 Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal
Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal
Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

10,633 Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal
Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

Operating Dry bottom wall-fired boiler Coal

12,868 Operating Dry bottom wall-fired boiler Coal
 SO2 Control(s)

 NOx 

Control(s) PM Control(s)

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator
Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic 

Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator
Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic 

Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse
Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse
Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA (Began Oct 16, 2010)<br>OElectrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator
Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Electrostatic Precipitator

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse
eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

eline Natural Gas Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse
Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>Overfi

Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse
Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>Overfi

Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA<br>OverfiBaghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse
Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse
Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Closed-coupled/Separated OFA Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator
Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic 

Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator
Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic 

Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator
Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic 

Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Low NOx Burner Technology w/ Separated OFA<br>Selective Non-catalytic Baghouse<br>Electrostatic Precipitator

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse
Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA (Began Jan 20, 2012)<br>OBaghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse
Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Low NOx Burner Technology w/ Separated OFA<br>Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse
Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

Overfire Air Baghouse

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Variable Designation Units Value

Unit Size (Gross) A (MW) 500

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 9,500

SO2 Rate D (lb/MMBtu) 2.00

Type of Coal E LIG-PRB Blend

HHV Bituminous BTU/lb 11,000

HHV PRB BTU/lb 8,400

HHV Lignite BTU/lb 7,200

Percent Lignite if Blended 50

Particulate Capture F ESP

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 4.75E+09

NSR K 1.43

Trona Feed Rate M (ton/hr) 16.33

Sorbent Waste Rate N (ton/hr) 11.65

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 17.05

User Input --->

Include Aux Power in 

VOM Q (%) 0.65

Trona Cost R ($/ton) 170
Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,000,000

SO2 Emission Baseline (tons/year) 30,000

Capital Cost Calculation

 BM ($) $18,348,000

 BM ($/kW) 37

Total Project Cost

 A1 $917,000

 A2 $917,000

 A3 $917,000

 CECC($) $21,099,000

 CECC($/kW) 42

 B1 $1,055,000

 TPC ($) $22,154,000

 TPC ($/kw) 44

 B2 $0

 TPC ($) $22,154,000

 TPC ($/kw) 44

Fixed O&M Cost

 FOMO ($/kW yr) 0.50

 FOMM ($/kW yr) 0.37

 FOMA ($/kW yr) 0.02 Fixed O&M additional addministrative labor costs

Fixed O&M maintenance material and labor costs

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Base module cost per kW

Engineering and construction management costs

Labor adjustment for 6 x 10 hour shift premium, per diem

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Costs are all based on 2012 d

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 
 FOM ($/kW yr) 0.89

Variable O&M

 VOMR ($/MWh) 5.55

 VOMW ($/MWh) 2.87

 VOMP ($/MWh) 0.39

 VOM ($/MWh) 8.82

Annualization

Capital, engineering and 

construction cost $21,099,000

Capital Recovery factor 0.0806

Annualized capital costs $1,700,293

Variable operating costs $35,260,822

Fixed operating costs $404,356

Total annualized costs $37,365,470

SO2 emissions reduction 

(tons) 15,000

$/ton 2,491

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)

Excludes owner's costs and AFUDC

VOM*(Gross Load)

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder assumed 

PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and unreacted 

drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% inert in the Trona 

sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; HHV is 

proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A

<---- User Input
<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent waste 

alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

strative labor costs

erial and labor costs

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

management costs

our shift premium, per diem, etc..

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

e all based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 
MW)*(8760 hours/year)

disposal that includes both the sorbent and the fly ash waste not removed prior to the sorbent 

onal auxillary power required (refer to Aux Power % above)
Comments

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB

Max annual value from 2009-2013

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Max monthly value from 2009-2013

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Based on input from Solvay

Choices for Input Boxes 

Three year average from 2009-2013, 

excluding max and min values
default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

LIG LIG-PRB Blend

or Input Boxes 
Facility Unit

Big Brown 1

Variable Designation Units Value

Unit Size (Gross) A (MW) 572.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 9,854

SO2 Rate D (lb/MMBtu) 2.00

Type of Coal E LIG-PRB Blend

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,343

HHV Lignite BTU/lb 6,850

Percent Lignite if Blended 61

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 5.65E+09

NSR K 0.85

Trona Feed Rate M (ton/hr) 11.50

Sorbent Waste Rate N (ton/hr) 7.99

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 21.94

User Input --->

Include Aux Power in 

VOM Q (%) 0.40
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,950,573

SO2 Emission Baseline (tons/year) 30,667

Capital Cost Calculation

 BM ($) $16,606,000

 BM ($/kW) 29

Total Project Cost

 A1 $830,000

 A2 $830,000

 A3 $830,000

 CECC($) $19,096,000

 CECC($/kW) 33

 B1 $955,000

 TPC ($) $20,051,000

 TPC ($/kw) 35

 B2 $0

 TPC ($) $20,051,000

 TPC ($/kw) 35

Fixed O&M Cost

 FOMO ($/kW yr) 0.44

 FOMM ($/kW yr) 0.29

 FOMA ($/kW yr) 0.02

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs

Total project cost per kW

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Labor adjustment for 6 x 10 hour shift premium, per diem

Contractor profit and fees
 FOM ($/kW yr) 0.74

Variable O&M

 VOMR ($/MWh) 3.64

 VOMW ($/MWh) 2.61

 VOMP ($/MWh) 0.24

 VOM ($/MWh) 6.49

Annualization

Capital, engineering and 

construction cost $19,096,000

Capital Recovery factor 0.0806

Annualized capital costs $1,538,878

Variable operating costs $32,128,615

Fixed operating costs $419,378

Total annualized costs $34,086,871

SO2 emissions reduction 

(tons) 15,334

$/ton 2,223

H/(100%)*(SO2 emission baseline)

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Variable O&M costs for trona reagent

Total Fixed O&M costs
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

our shift premium, per diem, etc..
MW)*(8760 hours/year)

disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Big Brown 1

Variable Designation Units Value

Unit Size (Gross) A (MW) 572.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 9,854

SO2 Rate D (lb/MMBtu) 2.00

Type of Coal E LIG-PRB Blend

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,343

HHV Lignite BTU/lb 6,850

Percent Lignite if Blended 61

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 90

Heat Input J (Btu/hr) 5.65E+09

NSR K 2.61

Trona Feed Rate M (ton/hr) 35.37

Sorbent Waste Rate N (ton/hr) 25.23

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 21.94

User Input --->

Include Aux Power in 

VOM Q (%) 1.23
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,950,573

SO2 Emission Baseline (tons/year) 30,667

Capital Cost Calculation

 BM ($) $29,007,000

 BM ($/kW) 51

Total Project Cost

 A1 $1,450,000

 A2 $1,450,000

 A3 $1,450,000

 CECC($) $33,357,000

 CECC($/kW) 58

 B1 $1,668,000

 TPC ($) $35,025,000

 TPC ($/kw) 61

 B2 $0

 TPC ($) $35,025,000

 TPC ($/kw) 61

Fixed O&M Cost

 FOMO ($/kW yr) 0.44

 FOMM ($/kW yr) 0.51

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.96

Variable O&M

 VOMR ($/MWh) 11.19

 VOMW ($/MWh) 4.12

 VOMP ($/MWh) 0.74

 VOM ($/MWh) 16.05

Annualization

Capital, engineering and 

construction cost $33,357,000

Capital Recovery factor 0.0806

Annualized capital costs $2,688,121

Variable operating costs $79,452,946

Fixed operating costs $543,175

Total annualized costs $82,684,241

SO2 emissions reduction 

(tons) 27,600

$/ton 2,996

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Big Brown 2

Variable Designation Units Value

Unit Size (Gross) A (MW) 572.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,197

SO2 Rate D (lb/MMBtu) 1.91

Type of Coal E LIG-PRB Blend

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,347

HHV Lignite BTU/lb 6,847

Percent Lignite if Blended 60

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 5.84E+09

NSR K 0.85

Trona Feed Rate M (ton/hr) 11.36

Sorbent Waste Rate N (ton/hr) 7.90

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 22.59

User Input --->

Include Aux Power in 

VOM Q (%) 0.40
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,921,894

SO2 Emission Baseline (tons/year) 30,814

Capital Cost Calculation

 BM ($) $16,551,000

 BM ($/kW) 29

Total Project Cost

 A1 $828,000

 A2 $828,000

 A3 $828,000

 CECC($) $19,035,000

 CECC($/kW) 33

 B1 $952,000

 TPC ($) $19,987,000

 TPC ($/kw) 35

 B2 $0

 TPC ($) $19,987,000

 TPC ($/kw) 35

Fixed O&M Cost

 FOMO ($/kW yr) 0.44

 FOMM ($/kW yr) 0.29

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.74

Variable O&M

 VOMR ($/MWh) 3.59

 VOMW ($/MWh) 2.66

 VOMP ($/MWh) 0.24

 VOM ($/MWh) 6.49

Annualization

Capital, engineering and 

construction cost $19,035,000

Capital Recovery factor 0.0806

Annualized capital costs $1,533,962

Variable operating costs $31,959,458

Fixed operating costs $416,402

Total annualized costs $33,909,822

SO2 emissions reduction 

(tons) 15,407

$/ton 2,201

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Big Brown 2

Variable Designation Units Value

Unit Size (Gross) A (MW) 572.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,197

SO2 Rate D (lb/MMBtu) 1.91

Type of Coal E LIG-PRB Blend

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,347

HHV Lignite BTU/lb 6,847

Percent Lignite if Blended 60

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 90

Heat Input J (Btu/hr) 5.84E+09

NSR K 2.61

Trona Feed Rate M (ton/hr) 34.96

Sorbent Waste Rate N (ton/hr) 24.94

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 22.59

User Input --->

Include Aux Power in 

VOM Q (%) 1.22
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,921,894

SO2 Emission Baseline (tons/year) 30,814

Capital Cost Calculation

 BM ($) $28,666,000

 BM ($/kW) 50

Total Project Cost

 A1 $1,433,000

 A2 $1,433,000

 A3 $1,433,000

 CECC($) $32,965,000

 CECC($/kW) 58

 B1 $1,648,000

 TPC ($) $34,613,000

 TPC ($/kw) 60

 B2 $0

 TPC ($) $34,613,000

 TPC ($/kw) 60

Fixed O&M Cost

 FOMO ($/kW yr) 0.44

 FOMM ($/kW yr) 0.50

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.96

Variable O&M

 VOMR ($/MWh) 11.06

 VOMW ($/MWh) 4.15

 VOMP ($/MWh) 0.73

 VOM ($/MWh) 15.94

Annualization

Capital, engineering and 

construction cost $32,965,000

Capital Recovery factor 0.0806

Annualized capital costs $2,656,531

Variable operating costs $78,456,412

Fixed operating costs $536,643

Total annualized costs $81,649,586

SO2 emissions reduction 

(tons) 27,733

$/ton 2,944

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Monticello 1

Variable Designation Units Value

Unit Size (Gross) A (MW) 562.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,299

SO2 Rate D (lb/MMBtu) 1.33

Type of Coal E LIG-PRB Blend

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,377

HHV Lignite BTU/lb 6,487

Percent Lignite if Blended 38

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 5.80E+09

NSR K 0.85

Trona Feed Rate M (ton/hr) 7.85

Sorbent Waste Rate N (ton/hr) 5.46

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 20.47

User Input --->

Include Aux Power in 

VOM Q (%) 0.28
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,523,648

SO2 Emission Baseline (tons/year) 17,865

Capital Cost Calculation

 BM ($) $14,902,000

 BM ($/kW) 26

Total Project Cost

 A1 $745,000

 A2 $745,000

 A3 $745,000

 CECC($) $17,137,000

 CECC($/kW) 30

 B1 $857,000

 TPC ($) $17,994,000

 TPC ($/kw) 32

 B2 $0

 TPC ($) $17,994,000

 TPC ($/kw) 32

Fixed O&M Cost

 FOMO ($/kW yr) 0.44

 FOMM ($/kW yr) 0.26

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.72

Variable O&M

 VOMR ($/MWh) 2.53

 VOMW ($/MWh) 2.30

 VOMP ($/MWh) 0.17

 VOM ($/MWh) 5.00

Annualization

Capital, engineering and 

construction cost $17,137,000

Capital Recovery factor 0.0806

Annualized capital costs $1,381,009

Variable operating costs $22,609,610

Fixed operating costs $374,199

Total annualized costs $24,364,819

SO2 emissions reduction 

(tons) 8,933

$/ton 2,728

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Monticello 1

Variable Designation Units Value

Unit Size (Gross) A (MW) 562.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,299

SO2 Rate D (lb/MMBtu) 1.33

Type of Coal E LIG-PRB Blend

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,377

HHV Lignite BTU/lb 6,487

Percent Lignite if Blended 38

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 90

Heat Input J (Btu/hr) 5.80E+09

NSR K 2.61

Trona Feed Rate M (ton/hr) 24.16

Sorbent Waste Rate N (ton/hr) 17.23

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 20.47

User Input --->

Include Aux Power in 

VOM Q (%) 0.86
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,523,648

SO2 Emission Baseline (tons/year) 17,865

Capital Cost Calculation

 BM ($) $20,505,000

 BM ($/kW) 36

Total Project Cost

 A1 $1,025,000

 A2 $1,025,000

 A3 $1,025,000

 CECC($) $23,580,000

 CECC($/kW) 42

 B1 $1,179,000

 TPC ($) $24,759,000

 TPC ($/kw) 44

 B2 $0

 TPC ($) $24,759,000

 TPC ($/kw) 44

Fixed O&M Cost

 FOMO ($/kW yr) 0.44

 FOMM ($/kW yr) 0.36

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.83

Variable O&M

 VOMR ($/MWh) 7.78

 VOMW ($/MWh) 3.35

 VOMP ($/MWh) 0.51

 VOM ($/MWh) 11.64

Annualization

Capital, engineering and 

construction cost $23,580,000

Capital Recovery factor 0.0806

Annualized capital costs $1,900,227

Variable operating costs $52,664,972

Fixed operating costs $426,218

Total annualized costs $54,991,417

SO2 emissions reduction 

(tons) 16,079

$/ton 3,420

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Monticello 2

Variable Designation Units Value

Unit Size (Gross) A (MW) 562.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,690

SO2 Rate D (lb/MMBtu) 1.26

Type of Coal E LIG-PRB Blend

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,387

HHV Lignite BTU/lb 6,484

Percent Lignite if Blended 35

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 6.02E+09

NSR K 0.85

Trona Feed Rate M (ton/hr) 7.72

Sorbent Waste Rate N (ton/hr) 5.37

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 20.89

User Input --->

Include Aux Power in 

VOM Q (%) 0.27
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,733,924

SO2 Emission Baseline (tons/year) 16,429

Capital Cost Calculation

 BM ($) $14,831,000

 BM ($/kW) 26

Total Project Cost

 A1 $742,000

 A2 $742,000

 A3 $742,000

 CECC($) $17,057,000

 CECC($/kW) 30

 B1 $853,000

 TPC ($) $17,910,000

 TPC ($/kw) 32

 B2 $0

 TPC ($) $17,910,000

 TPC ($/kw) 32

Fixed O&M Cost

 FOMO ($/kW yr) 0.44

 FOMM ($/kW yr) 0.26

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.72

Variable O&M

 VOMR ($/MWh) 2.49

 VOMW ($/MWh) 2.33

 VOMP ($/MWh) 0.16

 VOM ($/MWh) 4.98

Annualization

Capital, engineering and 

construction cost $17,057,000

Capital Recovery factor 0.0806

Annualized capital costs $1,374,562

Variable operating costs $23,585,904

Fixed operating costs $390,904

Total annualized costs $25,351,370

SO2 emissions reduction 

(tons) 8,215

$/ton 3,086

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Monticello 2

Variable Designation Units Value

Unit Size (Gross) A (MW) 562.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,690

SO2 Rate D (lb/MMBtu) 1.26

Type of Coal E LIG-PRB Blend

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,387

HHV Lignite BTU/lb 6,484

Percent Lignite if Blended 35

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 90

Heat Input J (Btu/hr) 6.02E+09

NSR K 2.61

Trona Feed Rate M (ton/hr) 23.75

Sorbent Waste Rate N (ton/hr) 16.94

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 20.89

User Input --->

Include Aux Power in 

VOM Q (%) 0.84
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,733,924

SO2 Emission Baseline (tons/year) 16,429

Capital Cost Calculation

 BM ($) $20,408,000

 BM ($/kW) 36

Total Project Cost

 A1 $1,020,000

 A2 $1,020,000

 A3 $1,020,000

 CECC($) $23,468,000

 CECC($/kW) 42

 B1 $1,173,000

 TPC ($) $24,641,000

 TPC ($/kw) 44

 B2 $0

 TPC ($) $24,641,000

 TPC ($/kw) 44

Fixed O&M Cost

 FOMO ($/kW yr) 0.44

 FOMM ($/kW yr) 0.36

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.82

Variable O&M

 VOMR ($/MWh) 7.65

 VOMW ($/MWh) 3.36

 VOMP ($/MWh) 0.51

 VOM ($/MWh) 11.52

Annualization

Capital, engineering and 

construction cost $23,468,000

Capital Recovery factor 0.0806

Annualized capital costs $1,891,202

Variable operating costs $54,514,200

Fixed operating costs $445,087

Total annualized costs $56,850,489

SO2 emissions reduction 

(tons) 14,786

$/ton 3,845

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Coleto Creek 1

Variable Designation Units Value

Unit Size (Gross) A (MW) 629.5

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,197

SO2 Rate D (lb/MMBtu) 0.92

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,837

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 6.42E+09

NSR K 0.85

Trona Feed Rate M (ton/hr) 6.01

Sorbent Waste Rate N (ton/hr) 4.18

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 17.43

User Input --->

Include Aux Power in 

VOM Q (%) 0.19
Trona Cost R ($/ton) 195

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 5,618,820

SO2 Emission Baseline (tons/year) 16,059

Capital Cost Calculation

 BM ($) $13,815,000

 BM ($/kW) 22

Total Project Cost

 A1 $691,000

 A2 $691,000

 A3 $691,000

 CECC($) $15,888,000

 CECC($/kW) 25

 B1 $794,000

 TPC ($) $16,682,000

 TPC ($/kw) 27

 B2 $0

 TPC ($) $16,682,000

 TPC ($/kw) 27

Fixed O&M Cost

 FOMO ($/kW yr) 0.40

 FOMM ($/kW yr) 0.22

 FOMA ($/kW yr) 0.01

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.63

Variable O&M

 VOMR ($/MWh) 1.86

 VOMW ($/MWh) 1.72

 VOMP ($/MWh) 0.11

 VOM ($/MWh) 3.69

Annualization

Capital, engineering and 

construction cost $15,888,000

Capital Recovery factor 0.0806

Annualized capital costs $1,280,357

Variable operating costs $20,731,452

Fixed operating costs $404,410

Total annualized costs $22,416,218

SO2 emissions reduction 

(tons) 8,030

$/ton 2,792

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Coleto Creek 1

Variable Designation Units Value

Unit Size (Gross) A (MW) 629.5

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,197

SO2 Rate D (lb/MMBtu) 0.92

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,837

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 90

Heat Input J (Btu/hr) 6.42E+09

NSR K 2.61

Trona Feed Rate M (ton/hr) 18.50

Sorbent Waste Rate N (ton/hr) 13.20

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 17.43

User Input --->

Include Aux Power in 

VOM Q (%) 0.59
Trona Cost R ($/ton) 195

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 5,618,820

SO2 Emission Baseline (tons/year) 16,059

Capital Cost Calculation

 BM ($) $19,010,000

 BM ($/kW) 30

Total Project Cost

 A1 $951,000

 A2 $951,000

 A3 $951,000

 CECC($) $21,863,000

 CECC($/kW) 35

 B1 $1,093,000

 TPC ($) $22,956,000

 TPC ($/kw) 36

 B2 $0

 TPC ($) $22,956,000

 TPC ($/kw) 36

Fixed O&M Cost

 FOMO ($/kW yr) 0.40

 FOMM ($/kW yr) 0.30

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.71

Variable O&M

 VOMR ($/MWh) 5.72

 VOMW ($/MWh) 2.43

 VOMP ($/MWh) 0.35

 VOM ($/MWh) 8.50

Annualization

Capital, engineering and 

construction cost $21,863,000

Capital Recovery factor 0.0806

Annualized capital costs $1,761,861

Variable operating costs $47,781,846

Fixed operating costs $457,979

Total annualized costs $50,001,685

SO2 emissions reduction 

(tons) 14,453

$/ton 3,460

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

W A Parrish WAP5

Variable Designation Units Value

Unit Size (Gross) A (MW) 638.7

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 9,955

SO2 Rate D (lb/MMBtu) 0.80

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,039

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 6.36E+09

NSR K 0.85

Trona Feed Rate M (ton/hr) 5.18

Sorbent Waste Rate N (ton/hr) 3.60

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 18.98

User Input --->

Include Aux Power in 

VOM Q (%) 0.16
Trona Cost R ($/ton) 192

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,838,372

SO2 Emission Baseline (tons/year) 14,157

Capital Cost Calculation

 BM ($) $13,241,000

 BM ($/kW) 21

Total Project Cost

 A1 $662,000

 A2 $662,000

 A3 $662,000

 CECC($) $15,227,000

 CECC($/kW) 24

 B1 $761,000

 TPC ($) $15,988,000

 TPC ($/kw) 25

 B2 $0

 TPC ($) $15,988,000

 TPC ($/kw) 25

Fixed O&M Cost

 FOMO ($/kW yr) 0.39

 FOMM ($/kW yr) 0.21

 FOMA ($/kW yr) 0.01

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.61

Variable O&M

 VOMR ($/MWh) 1.55

 VOMW ($/MWh) 1.77

 VOMP ($/MWh) 0.10

 VOM ($/MWh) 3.42

Annualization

Capital, engineering and 

construction cost $15,227,000

Capital Recovery factor 0.0806

Annualized capital costs $1,227,089

Variable operating costs $16,546,703

Fixed operating costs $338,198

Total annualized costs $18,111,990

SO2 emissions reduction 

(tons) 7,079

$/ton 2,559

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

W A Parrish WAP5

Variable Designation Units Value

Unit Size (Gross) A (MW) 638.7

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 9,955

SO2 Rate D (lb/MMBtu) 0.80

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,039

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 90

Heat Input J (Btu/hr) 6.36E+09

NSR K 2.61

Trona Feed Rate M (ton/hr) 15.94

Sorbent Waste Rate N (ton/hr) 11.37

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 18.98

User Input --->

Include Aux Power in 

VOM Q (%) 0.50
Trona Cost R ($/ton) 192

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,838,372

SO2 Emission Baseline (tons/year) 14,157

Capital Cost Calculation

 BM ($) $18,220,000

 BM ($/kW) 29

Total Project Cost

 A1 $911,000

 A2 $911,000

 A3 $911,000

 CECC($) $20,953,000

 CECC($/kW) 33

 B1 $1,048,000

 TPC ($) $22,001,000

 TPC ($/kw) 34

 B2 $0

 TPC ($) $22,001,000

 TPC ($/kw) 34

Fixed O&M Cost

 FOMO ($/kW yr) 0.39

 FOMM ($/kW yr) 0.29

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.69

Variable O&M

 VOMR ($/MWh) 4.78

 VOMW ($/MWh) 2.38

 VOMP ($/MWh) 0.30

 VOM ($/MWh) 7.46

Annualization

Capital, engineering and 

construction cost $20,953,000

Capital Recovery factor 0.0806

Annualized capital costs $1,688,527

Variable operating costs $36,091,083

Fixed operating costs $381,772

Total annualized costs $38,161,382

SO2 emissions reduction 

(tons) 12,741

$/ton 2,995

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

W A Parrish WAP6

Variable Designation Units Value

Unit Size (Gross) A (MW) 636.8

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,769

SO2 Rate D (lb/MMBtu) 0.87

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,039

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 6.86E+09

NSR K 0.85

Trona Feed Rate M (ton/hr) 6.07

Sorbent Waste Rate N (ton/hr) 4.22

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 20.47

User Input --->

Include Aux Power in 

VOM Q (%) 0.19
Trona Cost R ($/ton) 192

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,900,695

SO2 Emission Baseline (tons/year) 15,307

Capital Cost Calculation

 BM ($) $13,855,000

 BM ($/kW) 22

Total Project Cost

 A1 $693,000

 A2 $693,000

 A3 $693,000

 CECC($) $15,934,000

 CECC($/kW) 25

 B1 $797,000

 TPC ($) $16,731,000

 TPC ($/kw) 26

 B2 $0

 TPC ($) $16,731,000

 TPC ($/kw) 26

Fixed O&M Cost

 FOMO ($/kW yr) 0.39

 FOMM ($/kW yr) 0.22

 FOMA ($/kW yr) 0.01

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.62

Variable O&M

 VOMR ($/MWh) 1.83

 VOMW ($/MWh) 1.94

 VOMP ($/MWh) 0.11

 VOM ($/MWh) 3.88

Annualization

Capital, engineering and 

construction cost $15,934,000

Capital Recovery factor 0.0806

Annualized capital costs $1,284,064

Variable operating costs $19,027,337

Fixed operating costs $349,036

Total annualized costs $20,660,436

SO2 emissions reduction 

(tons) 7,654

$/ton 2,699

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

W A Parrish WAP6

Variable Designation Units Value

Unit Size (Gross) A (MW) 636.8

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,769

SO2 Rate D (lb/MMBtu) 0.87

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,039

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 90

Heat Input J (Btu/hr) 6.86E+09

NSR K 2.61

Trona Feed Rate M (ton/hr) 18.69

Sorbent Waste Rate N (ton/hr) 13.33

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 20.47

User Input --->

Include Aux Power in 

VOM Q (%) 0.59
Trona Cost R ($/ton) 192

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,900,695

SO2 Emission Baseline (tons/year) 15,307

Capital Cost Calculation

 BM ($) $19,065,000

 BM ($/kW) 30

Total Project Cost

 A1 $953,000

 A2 $953,000

 A3 $953,000

 CECC($) $21,924,000

 CECC($/kW) 34

 B1 $1,096,000

 TPC ($) $23,020,000

 TPC ($/kw) 36

 B2 $0

 TPC ($) $23,020,000

 TPC ($/kw) 36

Fixed O&M Cost

 FOMO ($/kW yr) 0.39

 FOMM ($/kW yr) 0.30

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.71

Variable O&M

 VOMR ($/MWh) 5.63

 VOMW ($/MWh) 2.65

 VOMP ($/MWh) 0.35

 VOM ($/MWh) 8.63

Annualization

Capital, engineering and 

construction cost $21,924,000

Capital Recovery factor 0.0806

Annualized capital costs $1,766,776

Variable operating costs $42,315,954

Fixed operating costs $395,356

Total annualized costs $44,478,086

SO2 emissions reduction 

(tons) 13,776

$/ton 3,229

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

W A Parrish WAP7

Variable Designation Units Value

Unit Size (Gross) A (MW) 559.4

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 9,654

SO2 Rate D (lb/MMBtu) 0.82

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,036

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 5.40E+09

NSR K 0.85

Trona Feed Rate M (ton/hr) 4.51

Sorbent Waste Rate N (ton/hr) 3.13

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 16.13

User Input --->

Include Aux Power in 

VOM Q (%) 0.16
Trona Cost R ($/ton) 192

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,682,905

SO2 Emission Baseline (tons/year) 12,335

Capital Cost Calculation

 BM ($) $12,730,000

 BM ($/kW) 23

Total Project Cost

 A1 $637,000

 A2 $637,000

 A3 $637,000

 CECC($) $14,641,000

 CECC($/kW) 26

 B1 $732,000

 TPC ($) $15,373,000

 TPC ($/kw) 27

 B2 $0

 TPC ($) $15,373,000

 TPC ($/kw) 27

Fixed O&M Cost

 FOMO ($/kW yr) 0.45

 FOMM ($/kW yr) 0.23

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.69

Variable O&M

 VOMR ($/MWh) 1.55

 VOMW ($/MWh) 1.72

 VOMP ($/MWh) 0.10

 VOM ($/MWh) 3.36

Annualization

Capital, engineering and 

construction cost $14,641,000

Capital Recovery factor 0.0806

Annualized capital costs $1,179,866

Variable operating costs $15,752,870

Fixed operating costs $368,792

Total annualized costs $17,301,527

SO2 emissions reduction 

(tons) 6,168

$/ton 2,805

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

W A Parrish WAP7

Variable Designation Units Value

Unit Size (Gross) A (MW) 559.4

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 9,654

SO2 Rate D (lb/MMBtu) 0.82

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,036

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 90

Heat Input J (Btu/hr) 5.40E+09

NSR K 2.61

Trona Feed Rate M (ton/hr) 13.87

Sorbent Waste Rate N (ton/hr) 9.90

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 16.13

User Input --->

Include Aux Power in 

VOM Q (%) 0.50
Trona Cost R ($/ton) 192

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,682,905

SO2 Emission Baseline (tons/year) 12,335

Capital Cost Calculation

 BM ($) $17,517,000

 BM ($/kW) 31

Total Project Cost

 A1 $876,000

 A2 $876,000

 A3 $876,000

 CECC($) $20,145,000

 CECC($/kW) 36

 B1 $1,007,000

 TPC ($) $21,152,000

 TPC ($/kw) 38

 B2 $0

 TPC ($) $21,152,000

 TPC ($/kw) 38

Fixed O&M Cost

 FOMO ($/kW yr) 0.45

 FOMM ($/kW yr) 0.31

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.78

Variable O&M

 VOMR ($/MWh) 4.76

 VOMW ($/MWh) 2.33

 VOMP ($/MWh) 0.30

 VOM ($/MWh) 7.38

Annualization

Capital, engineering and 

construction cost $20,145,000

Capital Recovery factor 0.0806

Annualized capital costs $1,623,413

Variable operating costs $34,555,902

Fixed operating costs $415,087

Total annualized costs $36,594,402

SO2 emissions reduction 

(tons) 11,102

$/ton 3,296

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Welsh 1

Variable Designation Units Value

Unit Size (Gross) A (MW) 521.6

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,068

SO2 Rate D (lb/MMBtu) 0.53

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,464

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F ESP

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 5.25E+09

NSR K 1.43

Trona Feed Rate M (ton/hr) 4.79

Sorbent Waste Rate N (ton/hr) 3.41

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 14.89

User Input --->

Include Aux Power in 

VOM Q (%) 0.18
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 3,827,597

SO2 Emission Baseline (tons/year) 8,084

Capital Cost Calculation

 BM ($) $12,947,000

 BM ($/kW) 25

Total Project Cost

 A1 $647,000

 A2 $647,000

 A3 $647,000

 CECC($) $14,888,000

 CECC($/kW) 29

 B1 $744,000

 TPC ($) $15,632,000

 TPC ($/kw) 30

 B2 $0

 TPC ($) $15,632,000

 TPC ($/kw) 30

Fixed O&M Cost

 FOMO ($/kW yr) 0.48

 FOMM ($/kW yr) 0.25

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.74

Variable O&M

 VOMR ($/MWh) 1.66

 VOMW ($/MWh) 1.75

 VOMP ($/MWh) 0.11

 VOM ($/MWh) 3.53

Annualization

Capital, engineering and 

construction cost $14,888,000

Capital Recovery factor 0.0806

Annualized capital costs $1,199,770

Variable operating costs $13,501,650

Fixed operating costs $325,118

Total annualized costs $15,026,538

SO2 emissions reduction 

(tons) 4,042

$/ton 3,718

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Welsh 1

Variable Designation Units Value

Unit Size (Gross) A (MW) 521.6

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,068

SO2 Rate D (lb/MMBtu) 0.53

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,464

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F ESP

Milled Trona G TRUE

Removal Target H % 80

Heat Input J (Btu/hr) 5.25E+09

NSR K 3.32

Trona Feed Rate M (ton/hr) 11.08

Sorbent Waste Rate N (ton/hr) 7.99

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 14.89

User Input --->

Include Aux Power in 

VOM Q (%) 0.43
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 3,827,597

SO2 Emission Baseline (tons/year) 8,084

Capital Cost Calculation

 BM ($) $16,435,000

 BM ($/kW) 32

Total Project Cost

 A1 $822,000

 A2 $822,000

 A3 $822,000

 CECC($) $18,901,000

 CECC($/kW) 36

 B1 $945,000

 TPC ($) $19,846,000

 TPC ($/kw) 38

 B2 $0

 TPC ($) $19,846,000

 TPC ($/kw) 38

Fixed O&M Cost

 FOMO ($/kW yr) 0.48

 FOMM ($/kW yr) 0.32

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.81

Variable O&M

 VOMR ($/MWh) 3.85

 VOMW ($/MWh) 2.19

 VOMP ($/MWh) 0.26

 VOM ($/MWh) 6.30

Annualization

Capital, engineering and 

construction cost $18,901,000

Capital Recovery factor 0.0806

Annualized capital costs $1,523,164

Variable operating costs $24,115,114

Fixed operating costs $354,687

Total annualized costs $25,992,966

SO2 emissions reduction 

(tons) 6,467

$/ton 4,019

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Welsh 2

Variable Designation Units Value

Unit Size (Gross) A (MW) 519.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,218

SO2 Rate D (lb/MMBtu) 0.51

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,470

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F ESP

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 5.31E+09

NSR K 1.43

Trona Feed Rate M (ton/hr) 4.66

Sorbent Waste Rate N (ton/hr) 3.32

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 15.05

User Input --->

Include Aux Power in 

VOM Q (%) 0.18
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 3,827,532

SO2 Emission Baseline (tons/year) 8,256

Capital Cost Calculation

 BM ($) $12,849,000

 BM ($/kW) 25

Total Project Cost

 A1 $642,000

 A2 $642,000

 A3 $642,000

 CECC($) $14,775,000

 CECC($/kW) 28

 B1 $739,000

 TPC ($) $15,514,000

 TPC ($/kw) 30

 B2 $0

 TPC ($) $15,514,000

 TPC ($/kw) 30

Fixed O&M Cost

 FOMO ($/kW yr) 0.48

 FOMM ($/kW yr) 0.25

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.74

Variable O&M

 VOMR ($/MWh) 1.62

 VOMW ($/MWh) 1.77

 VOMP ($/MWh) 0.11

 VOM ($/MWh) 3.50

Annualization

Capital, engineering and 

construction cost $14,775,000

Capital Recovery factor 0.0806

Annualized capital costs $1,190,664

Variable operating costs $13,390,807

Fixed operating costs $325,342

Total annualized costs $14,906,814

SO2 emissions reduction 

(tons) 4,128

$/ton 3,611

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Welsh 2

Variable Designation Units Value

Unit Size (Gross) A (MW) 519.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,218

SO2 Rate D (lb/MMBtu) 0.51

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,470

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F ESP

Milled Trona G TRUE

Removal Target H % 80

Heat Input J (Btu/hr) 5.31E+09

NSR K 3.32

Trona Feed Rate M (ton/hr) 10.79

Sorbent Waste Rate N (ton/hr) 7.78

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 15.05

User Input --->

Include Aux Power in 

VOM Q (%) 0.42
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 3,827,532

SO2 Emission Baseline (tons/year) 8,256

Capital Cost Calculation

 BM ($) $16,310,000

 BM ($/kW) 31

Total Project Cost

 A1 $816,000

 A2 $816,000

 A3 $816,000

 CECC($) $18,758,000

 CECC($/kW) 36

 B1 $938,000

 TPC ($) $19,696,000

 TPC ($/kw) 38

 B2 $0

 TPC ($) $19,696,000

 TPC ($/kw) 38

Fixed O&M Cost

 FOMO ($/kW yr) 0.48

 FOMM ($/kW yr) 0.31

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.81

Variable O&M

 VOMR ($/MWh) 3.76

 VOMW ($/MWh) 2.20

 VOMP ($/MWh) 0.25

 VOM ($/MWh) 6.21

Annualization

Capital, engineering and 

construction cost $18,758,000

Capital Recovery factor 0.0806

Annualized capital costs $1,511,640

Variable operating costs $23,755,748

Fixed operating costs $354,778

Total annualized costs $25,622,166

SO2 emissions reduction 

(tons) 6,605

$/ton 3,879

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Welsh 3

Variable Designation Units Value

Unit Size (Gross) A (MW) 519.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,426

SO2 Rate D (lb/MMBtu) 0.53

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,500

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F ESP

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 5.42E+09

NSR K 1.43

Trona Feed Rate M (ton/hr) 4.94

Sorbent Waste Rate N (ton/hr) 3.52

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 15.30

User Input --->

Include Aux Power in 

VOM Q (%) 0.19
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 3,931,843

SO2 Emission Baseline (tons/year) 8,609

Capital Cost Calculation

 BM ($) $13,064,000

 BM ($/kW) 25

Total Project Cost

 A1 $653,000

 A2 $653,000

 A3 $653,000

 CECC($) $15,023,000

 CECC($/kW) 29

 B1 $751,000

 TPC ($) $15,774,000

 TPC ($/kw) 30

 B2 $0

 TPC ($) $15,774,000

 TPC ($/kw) 30

Fixed O&M Cost

 FOMO ($/kW yr) 0.48

 FOMM ($/kW yr) 0.25

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.75

Variable O&M

 VOMR ($/MWh) 1.72

 VOMW ($/MWh) 1.81

 VOMP ($/MWh) 0.11

 VOM ($/MWh) 3.65

Annualization

Capital, engineering and 

construction cost $15,023,000

Capital Recovery factor 0.0806

Annualized capital costs $1,210,650

Variable operating costs $14,337,927

Fixed operating costs $336,087

Total annualized costs $15,884,663

SO2 emissions reduction 

(tons) 4,305

$/ton 3,690

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Welsh 3

Variable Designation Units Value

Unit Size (Gross) A (MW) 519.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,426

SO2 Rate D (lb/MMBtu) 0.53

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,500

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F ESP

Milled Trona G TRUE

Removal Target H % 80

Heat Input J (Btu/hr) 5.42E+09

NSR K 3.32

Trona Feed Rate M (ton/hr) 11.44

Sorbent Waste Rate N (ton/hr) 8.25

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 15.30

User Input --->

Include Aux Power in 

VOM Q (%) 0.44
Trona Cost R ($/ton) 181

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 3,931,843

SO2 Emission Baseline (tons/year) 8,609

Capital Cost Calculation

 BM ($) $16,584,000

 BM ($/kW) 32

Total Project Cost

 A1 $829,000

 A2 $829,000

 A3 $829,000

 CECC($) $19,071,000

 CECC($/kW) 37

 B1 $954,000

 TPC ($) $20,025,000

 TPC ($/kw) 39

 B2 $0

 TPC ($) $20,025,000

 TPC ($/kw) 39

Fixed O&M Cost

 FOMO ($/kW yr) 0.48

 FOMM ($/kW yr) 0.32

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.82

Variable O&M

 VOMR ($/MWh) 3.99

 VOMW ($/MWh) 2.27

 VOMP ($/MWh) 0.26

 VOM ($/MWh) 6.52

Annualization

Capital, engineering and 

construction cost $19,071,000

Capital Recovery factor 0.0806

Annualized capital costs $1,536,863

Variable operating costs $25,628,127

Fixed operating costs $366,841

Total annualized costs $27,531,831

SO2 emissions reduction 

(tons) 6,887

$/ton 3,998

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Tolk 171B

Variable Designation Units Value

Unit Size (Gross) A (MW) 533

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 9,706

SO2 Rate D (lb/MMBtu) 0.72

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,822

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 5.17E+09

NSR K 0.85

Trona Feed Rate M (ton/hr) 3.79

Sorbent Waste Rate N (ton/hr) 2.64

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 14.07

User Input --->

Include Aux Power in 

VOM Q (%) 0.14
Trona Cost R ($/ton) 195

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,598,970

SO2 Emission Baseline (tons/year) 10,031

Capital Cost Calculation

 BM ($) $12,120,000

 BM ($/kW) 23

Total Project Cost

 A1 $606,000

 A2 $606,000

 A3 $606,000

 CECC($) $13,938,000

 CECC($/kW) 26

 B1 $697,000

 TPC ($) $14,635,000

 TPC ($/kw) 27

 B2 $0

 TPC ($) $14,635,000

 TPC ($/kw) 27

Fixed O&M Cost

 FOMO ($/kW yr) 0.47

 FOMM ($/kW yr) 0.23

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.71

Variable O&M

 VOMR ($/MWh) 1.38

 VOMW ($/MWh) 1.57

 VOMP ($/MWh) 0.09

 VOM ($/MWh) 3.04

Annualization

Capital, engineering and 

construction cost $13,938,000

Capital Recovery factor 0.0806

Annualized capital costs $1,123,213

Variable operating costs $13,968,324

Fixed operating costs $374,040

Total annualized costs $15,465,578

SO2 emissions reduction 

(tons) 5,016

$/ton 3,084

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Tolk 171B

Variable Designation Units Value

Unit Size (Gross) A (MW) 533

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 9,706

SO2 Rate D (lb/MMBtu) 0.72

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,822

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 90

Heat Input J (Btu/hr) 5.17E+09

NSR K 2.61

Trona Feed Rate M (ton/hr) 11.67

Sorbent Waste Rate N (ton/hr) 8.32

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 14.07

User Input --->

Include Aux Power in 

VOM Q (%) 0.44
Trona Cost R ($/ton) 195

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,598,970

SO2 Emission Baseline (tons/year) 10,031

Capital Cost Calculation

 BM ($) $16,677,000

 BM ($/kW) 31

Total Project Cost

 A1 $834,000

 A2 $834,000

 A3 $834,000

 CECC($) $19,179,000

 CECC($/kW) 36

 B1 $959,000

 TPC ($) $20,138,000

 TPC ($/kw) 38

 B2 $0

 TPC ($) $20,138,000

 TPC ($/kw) 38

Fixed O&M Cost

 FOMO ($/kW yr) 0.47

 FOMM ($/kW yr) 0.31

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.80

Variable O&M

 VOMR ($/MWh) 4.26

 VOMW ($/MWh) 2.10

 VOMP ($/MWh) 0.26

 VOM ($/MWh) 6.62

Annualization

Capital, engineering and 

construction cost $19,179,000

Capital Recovery factor 0.0806

Annualized capital costs $1,545,567

Variable operating costs $30,461,398

Fixed operating costs $419,465

Total annualized costs $32,426,429

SO2 emissions reduction 

(tons) 9,028

$/ton 3,592

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Tolk 172B

Variable Designation Units Value

Unit Size (Gross) A (MW) 542.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,384

SO2 Rate D (lb/MMBtu) 0.65

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,821

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 50

Heat Input J (Btu/hr) 5.64E+09

NSR K 0.85

Trona Feed Rate M (ton/hr) 3.73

Sorbent Waste Rate N (ton/hr) 2.59

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 15.34

User Input --->

Include Aux Power in 

VOM Q (%) 0.14
Trona Cost R ($/ton) 195

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,596,449

SO2 Emission Baseline (tons/year) 11,034

Capital Cost Calculation

 BM ($) $12,064,000

 BM ($/kW) 22

Total Project Cost

 A1 $603,000

 A2 $603,000

 A3 $603,000

 CECC($) $13,873,000

 CECC($/kW) 26

 B1 $694,000

 TPC ($) $14,567,000

 TPC ($/kw) 27

 B2 $0

 TPC ($) $14,567,000

 TPC ($/kw) 27

Fixed O&M Cost

 FOMO ($/kW yr) 0.46

 FOMM ($/kW yr) 0.22

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.70

Variable O&M

 VOMR ($/MWh) 1.34

 VOMW ($/MWh) 1.65

 VOMP ($/MWh) 0.08

 VOM ($/MWh) 3.07

Annualization

Capital, engineering and 

construction cost $13,873,000

Capital Recovery factor 0.0806

Annualized capital costs $1,117,975

Variable operating costs $14,115,709

Fixed operating costs $366,470

Total annualized costs $15,600,155

SO2 emissions reduction 

(tons) 5,517

$/ton 2,828

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes 
Facility Unit

Tolk 172B

Variable Designation Units Value

Unit Size (Gross) A (MW) 542.9

Retrofit Factor B 1

Gross Heat Rate C (Btu/kWh) 10,384

SO2 Rate D (lb/MMBtu) 0.65

Type of Coal E PRB

HHV Bituminous BTU/lb 0

HHV PRB BTU/lb 8,821

HHV Lignite BTU/lb 0

Percent Lignite if Blended 0

Particulate Capture F BGH

Milled Trona G TRUE

Removal Target H % 90

Heat Input J (Btu/hr) 5.64E+09

NSR K 2.61

Trona Feed Rate M (ton/hr) 11.48

Sorbent Waste Rate N (ton/hr) 8.19

User Input ---> Include Fly Ash Waste Rate 

in VOM P (ton/hr) 15.34

User Input --->

Include Aux Power in 

VOM Q (%) 0.42
Trona Cost R ($/ton) 195

Waste Disposal Cost S ($/ton) 50

Aux Power Cost T ($/kWh) 0.06

Operating Labor Rate U ($/hr) 60

Interest Rate (%) 7

Equipment Lifetime (years) 30

Gross Load (MW-hours) 4,596,449

SO2 Emission Baseline (tons/year) 11,034

Capital Cost Calculation

 BM ($) $16,600,000

 BM ($/kW) 31

Total Project Cost

 A1 $830,000

 A2 $830,000

 A3 $830,000

 CECC($) $19,090,000

 CECC($/kW) 35

 B1 $955,000

 TPC ($) $20,045,000

 TPC ($/kw) 37

 B2 $0

 TPC ($) $20,045,000

 TPC ($/kw) 37

Fixed O&M Cost

 FOMO ($/kW yr) 0.46

 FOMM ($/kW yr) 0.31

 FOMA ($/kW yr) 0.02

Labor adjustment for 6 x 10 hour shift premium, per diem

Costs are all based on 2012 dolla

Explanation of Calculation

Includes: equipment, installation, buildings, foundations

Base DSI module includes all equipment from unloading 

Base module cost per kW

Engineering and construction management costs

Contractor profit and fees

Capital, engineering and construction cost subtotal

Capital, engineering and construction cost subtotal per k

Owners costs including "home office" costs (owner engin

Total project cost without AFUDC

Total project cost per kW without AFUDC

AFUDC (zero for less than 1 year engineering and constru

Total project cost

Total project cost per kW

Fixed O&M additional operating labor costs. Based on tw

Fixed O&M maintenance material and labor costs

Fixed O&M additional addministrative labor costs
 FOM ($/kW yr) 0.78

Variable O&M

 VOMR ($/MWh) 4.11

 VOMW ($/MWh) 2.17

 VOMP ($/MWh) 0.25

 VOM ($/MWh) 6.53

Annualization

Capital, engineering and 

construction cost $19,090,000

Capital Recovery factor 0.0806

Annualized capital costs $1,538,394

Variable operating costs $30,036,649

Fixed operating costs $410,837

Total annualized costs $31,985,880

SO2 emissions reduction 

(tons) 9,931

$/ton 3,221

Total Fixed O&M costs

Variable O&M costs for trona reagent

Variable O&M costs for waste disposal that includes both 

Variable O&M costs for additional auxillary power requir

Total variable O&M costs

Excludes owner's costs and AFUDC

VOM*(Gross Load)

FOM*(Gross Load)*(1000kw/MW)*(8760 hours/year)

H/(100%)*(SO2 emission baseline)
Calculation

<---- User Input

<---- User Input (An "average" retrofit has a factor = 1.0)

<---- User Input

<---- User Input

<--- User Input (PRB, BIT, LIG, or LIG-PRB Blend)

<---- User Input (default is 11,000 Btu/lb if applicable; else no meaning)

<---- User Input (default is 8,400 Btu/lb if applicable; else no meaning)

<---- User Input (default is 7,200 Btu/lb if applicable; else no meaning)

<---- User Input (If Type of Coal = "LIG-PRB Blend," Enter % Lignite. Remainder 

assumed PRB. If not "LIG-PRB Blend," no meaning)

<---- User Input

<---- User Input

Maximum Removal Targets:

Unmilled Trona with an ESP = 65%

Milled Trona with an ESP = 80%

Unmilled Trona with a BGH = 80%

Milled Trona with a BGH = 90%

A*C*1000

Unmilled Trona with an ESP = If(H<40,0.0350*H,0.352e^(0.0345*H))

Milled Trona with an ESP = If(H<40,0.0270*H,0.353e^(0.0280*H))

Unmilled Trona with a BGH = If(H<40,0.0215*H,0.295e^(0.0267*H))

Milled Trona with a BGH = If(H<40,0.0160*H,0.208e^(0.0281*H))

(1.2011*10^-6)*K*A*C*D

(0.7387-0.00073696*H/K)*M; Based on a final reaction product of NA2SO4 and 

unreacted drysorbent as NA2CO3. Waste product adjusted for a maximum of 5% 

inert in the Trona sorbent.

(A*C)*Ash in Coal*(1-Boiler Ash Removal)/(2*HHV)

For Bituminous Coal: Ash in Coal = 0.12; Boiler Ash Removal = 0.2; HHV= 11000

For PRB Coal: Ash in Coal = 0.06; Boiler Ash Removal = 0.2; HHV= 8400

For Lignite Coal: Ash in Coal = 0.08; Boiler Ash Removal = 0.2 HHV= 7200

For Blend Coal: Ash is proportional to lignite and PRB; Boiler Ash Removal = 0.2; 

HHV is proportional to lignite and PRB

If Milled Trona M*20/A, else M*18/A
<---- User Input

<---- User Input (Disposal cost with fly ash = $50. Without fly ash, the sorbent 

waste alone will be more difficult to dispose = $100)

<---- User Input

<---- User Input (Labor cost including all benefits)

<---- User Input

<---- User Input

<---- User Input

<---- User Input

our shift premium, per diem, etc..

l based on 2012 dollars

ion, buildings, foundations, electrical, and retrofit difficulty.

quipment from unloading to injection. 

management costs

ruction cost subtotal

ruction cost subtotal per kW

 office" costs (owner engineering, management, and procurement activities)

ar engineering and construction cycles)

ng labor costs. Based on two additional operators.

erial and labor costs

strative labor costs
disposal that includes both the sorbent and the fly ash waste not removed prior to the 

onal auxillary power required (refer to Aux Power % above)

MW)*(8760 hours/year)
Comments

Facility Unit MW

Big Brown 1

572.9

2

572.9

Max annual value from 2009-2013

Coleto Creek 1

629.5

Max monthly value from 2009-2013 Monticello 1

562.9

2 562.9

Tolk 171B 533.0

172B 542.9

W A Parrish WAP5 638.7

WAP6 636.8

WAP7 559.4

Welsh 1 521.6

One run with 50%, and another with 

either 80% or 90% based on particulate 

control device used

2

519.9

3 519.9

Pg 3 of the documentation lists example 

calculated NSRs which differ from those 

calculated from the formulae here. Per 

emails from Bill Stevens, the 

documentation is in error.

Assume fly ash waste rate is included in 

VOM

Assume aux power is included in VOM

Facilities to Analyze

Three year average from 2009-2013, 

excluding max and min values
Based on input from Solvay

default value

default value

default value

Max annual value from 2009-2013

3 -yr avg. 2009-2013, excluding max and 

min

Comments

 excludes owner's costs

 excludes owner's costs

includes owner's costs

includes owner's costs

includes owner's costs and AFUDC

includes owner's costs and AFUDC

Aux Power VOM 

Possibilities

Include Aux 

Power in VOM

Don't include 

Aux Power in 

VOM

Type of Coal Bituminous PRB LIG LIG-PRB Blend

Fly Ash Waste 

VOM 

Possibilities

Include Fly 

Ash Waste 

Rate in VOM

Don't include 

Fly Ash Waste 

Rate in VOM

Particulate 

Control Device ESP BGH

Milled Trone TRUE FALSE

Choices for Input Boxes