P. 1



# OAR Box

# 1865 Prepped byCharmelle Mathews



# Document

Number: 

# 124 ) IV-K-(l)- 5

Docket Number: 

# A-83-2 7

Printed 12/3/20083:22:18PM

Sheet 124of 198199 0 PROJECTE D NE WINDUSTRIA LFOSSI LFUEL-FIRE D BOILE R AI R EMISSIONS

. FUE LDEMAND, AND COST S
(LO H OIL/FLEXIBL E CARRIA6 E MARKE TGA S PRICES )

PREPARE D FOR : TH E U.S

. ENVIRONMENTA LPROTECTIO N AGENC Y

PREPARE D BY :
ENER6 YANDENVIRONMENTAL ANALYSIS , INC . 165 5 NORT HFOR T MYERDRIVE ARLINGTON , VIRGINI A 2220 9 10/«*/o 6 

# i s < I 

# 7
ILIS TO FTABLES 

# s

DESCRIPTIO N

OF TABL E

FUE L DEMAND

- NUMBE ROF UNIT S

- BTU S O F FUE L CONSUMPTIO N
POLLUTAN T EMISSION S
COST S
NO XONL Y

- CONTRO L COST S

- EMISSION S

< * NATIONAL IMPACTS B YSIZ E (MMBTU/HR )

- 10-5 0

- 50-7 5

- 75-10 0

- 100-15 0

- 150-20 0

- 200-25 0

- > 25 0

- > 10 0

- 100-25 0

- > 5 0

- TOTA L

REGIONAL IMPACT S

- S0 2 EMISSION S 100-15 0 MMBTU/HR 150-20 0 MMBTU/HR 200-25 0 MMBTU/HR
• , ' " > 25 0 MMBTU/HR

- FOSSI L FUE L DEMAND 100-15 0 MMBTU/HR 150-20 0 MMBTU/HR I . 200-25 0 MMBTU/HR > 25 0 MMBTU/HR

- ANNUALIZE DCOST S 100-15 0 MMBTU/HR 150-20 0 MMBTU/HR 200-25 0 MMBTU/HR > 25 0 MMBTU/ ! .

R TABL E NUMBE R 

### "

I 2
3
4

5 *

7 8 9 1 0 1 1 1 2 1 3 1 4 1 5 1 6 1 7

1 8 1 9 2 0 2 1

2 2 2 3 2 4 2 5

2 6 2 7 2 8 2 9NOTES ON IFCA M PROJECTION S innnniiiiiinnniinnn i

l

. NE H EE

A198 6 INDUSTRIA LOI LAND 6A S PRIC E PROJECTION S NE H IC F198 6 INDUSTRIA LCOALPRIC E PROJECTION S 2
. BASECASE

-S02 : CURREN TCOA LNSPS

-PM : PROPOSED COALNSPS (4 9 F R 25103 )

-NOX : N

O SIP'S , N

O NSPS
3

. OPTIO N CAS E 1 :

-COA LTYP E B , DIST

. AND 0. 8 PERCEN TSULFU R RESI D ARE I N COMPLIANC E 4

. OPTIO N CAS E 2 :

-SCRU B AL LCOALTYPE S 9 0 PERCEN T

-DIST

. AND 0. 3 PERCENTSULFU R RESI D ARE I N COMPLIANC E 5

. OPTIO N CAS E 3 :

-SCRU B AL LCOALAN D RESI D TYPE S 9 0 PERCEN T

-DIST

. I S I N COMPLIANC E

-NO TINCLUDED ) RESULT S HOUL D BE IDENTICA LT

O OPTIO N CASE 2

_ JINDUSTRIA L BOILE RNEHSOURCE PERFORMANC E STANDARD S ASSUMPTIONS OPTIO N CAS E 1 (AR021 3 )

BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT )

NATURA L GAS S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MMBTU ) NO XCEILIN

G(LB/MMBTU )
DISTILUT E FUE

L OI L S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MMBTU ) NO XCEILIN

G(LB/MMBTU ) 4 « RESIDUA

L FUEL OI L S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MMBTU ) NO XCEILIN

G(LB/MMBTU )
COA L S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MMBTU )

- FO R<30 XC

U NO XCEILIN

G(LB/MMBTU ) 10-3 0

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E 30-5 0

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E 50-7 5

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E 75-10 0

NONE NONE NONE

NONE NONE NONE

NONE NONE NONE

NONE NONE NONE NONE 100-15 0

NON E NON E NON E

NON E NON E NON E

0.8 0 NON E NON E

1.2 0 0.0 5 0.2 0 NON E 150-20 0

NON E NON E NON E

NON E NON E NON E

0.8 0 NON E NON E

1.2 0 0.0 5 0.2 0 NON E 200-25 0

NON E NON E NON E

NON E NON E NON E

0.8 0 NON E NON E

1.2 0 0.0 5 0.2 0 NON E >25 0

NON E NON E NON E

NON E NON E NON E

0.8 0 NON E NON E

1.2 0 0.0 5 0.0 5 NON E

MANDATOR

YSCRUBBIN

GREGUUTION S
RESIDUA L FUEL OI L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

L REQUIRE

D LO HSULFUR,EXEMPTIO

N (L BS02/MMBTU )
COA L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

L REQUIRE

D LO HSULFU REXEMPTIO

N (L BS02/HMBTU ) NON E NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NONE

NONE NONE NONE

NONE NONE NONE NONE NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E

inINDUSTRIA L BOILE RNE HSOURCE PERFORMANCE STANDARDS ASSUMPTIONS OPTIO N CAS E 2 (AR021 4 )

BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT )

NATURA L 6AS S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MMBTU ) NO XCEILIN

G(LB/MMBTU )
DISTILUT E FUE

L OI L S0 2 CEILIN

G(LB/MMBTU ) P HCEILIN

G(LB/MMBTU ) NOX.CEILIN

G(LB/MMBTU ) « RESIDUA

L FUEL OI L S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MMBTU ) NO XCEILIN

G(LB/MMBTU )
COA L S0 2 CEILIN

G(LB/MMBTU ) P N CEILIN G(LB/MMBTU )

- FO R<30 XC

U NO XCEILIN

G(LB/MMBTU ) 10-3 0

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E 30-5 0

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E 50-7 5

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E 75-10 0

NONE NONE NONE

NONE NONE NONE

NONE NONE NONE

NONE NONE NONE NONE 100-15 0

NON E NON E NON E

NON E NON E NON E

0.3 5 NON E NON E

1.2 0 0.0 5 0.2 0 NON E 150-20 0

NON E NON E NON E

NON E NON E NON E

0.3 5 NON E NON E

1.2 0 0.0 5 0.2 0 NON E 200-25 0

NON E NON E NON E

NON E NON E NON E

0.3 5 NON E NON E

1.2 0 0.0 5 0.2 0 NON E >25 0

NON E NON E NON E

NON E NON E NON E

0.3 5 NON E NON E

1.2 0 0.0 5 0.0 5 NON E

MANDATOR

YSCRUBBIN

GREGUUTION S
RESIDUA L FUE L OI L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

L REQUIRE

D LO HSULFUR , EXEMPTIO

N (L BS02/MMBTU )
COA L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

L REQUIRE

D LO HSULFU REXEMPTIO

N (L BS02/MHBTU ) NON E NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NONE

NONE NONE NONE

NONE NONE NONE NONE NON E

NON E NON E NON E

NON E 90.0 0 NON E NON E NON E

NON E NON E NON E

NON E 90.0 0 NON E NON E NON E

NON E NON E NON E

NON E 90.0 0 NON E NON E NON E

NON E NON E NON E

NON E 90.0 0 NON E NON E

T lTABLE 1 — 199 0 FUE

LDEMAN D (NUMBE RO F UNITS )

10-5 0 BOILE

RSIZE (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L
•TOTAL " TH E BAS E OPTIO N OPTIO N
NATURA L GAS TH E BAS E OPTIO N OPTIO N
COA L TH E BAS E OPTIO N OPTIO N CAS E CAS E 1 CAS E 2
AN DOI L CAS E CAS E 1 CAS E 2

CAS E CAS E 1 CAS E 2 1412 .

1412 . 1412 .

1412 . 1412 . 1412 .

0 . 0 . 0 . 577 .

577 . 577 .

577 . 577 . 577 .

0 . 0 . 0 . 271 .

271 . 271 .

271 . 271 . 271 .

0 . 0 . 0 . 135 .

135 . 135 .

135 . 135 . 135 .

0 . 0 . 0 . 62 .

62 . 62 .

62 . 62 . 62 .

0 . 0 . 0 . 136 .

136 . 136 .

134 . 134 . 136 .

2 . 2 . 0 . 2593 . 2593 . 2593 .

2591 . 2591 . 2593 .

2 . 2 . 0 .

T l

^ 11

4

1 "TOTAL " TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2
NATURA L GAS TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2
RESIDUA L FUE L OI L TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2
COA L TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2

1 10-5 0

132 . 132 . 132 .

102 . 102 . 102 .

30 . 30 . 30 .

0 . 0 . 0 . TABLE 2 —

199 0 FUE

L DEMAN D (10*«1 2 BTUS )
BOILE RSIZE 50-10 0 100-15 0

136 . 129 . 136 . 129 . 136 . 129 .

99 . 96 . 99 . 129 . 99 . 129 .

37 . 32 . 37 . 0 . 37 . 0 .

0 . 0 . 0 . 0 . 0 . 0 . (MMBTU/HR )

150-20 0 200-25 0

U l . 67 . U l . 67 . U l . 67 .

90 . 47 . U l . 66 . U l . 67 .

21 . 20 . 0 . 1 . 0 . 0 .

0 . 0 . 0 . 0 . 0 . 0 . > 25 0

191 . 191 . 191 .

147 . 184 . 191 .

40 . 3 . 0 .

4 . 4 . 0 . » 1

•

TOTA L

766 . 766 . 766 .

581 . ' 690 . 699 .

181 . 71 . 67 .

4 . 4 . 0 .

# 4

10-5 0 TABLE 3 — 199 0 EMISSIONS (10** 3 TONS )
BOILE RSIZE (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L S0 2 TH E BAS E OPTIO N OPTIO N
P M TH E BAS E OPTIO N OPTIO N
NO XTH E BAS E OPTIO N OPTIO N
PM1 0 TH E BAS E OPTIO N OPTIO N CAS E CAS E CAS E

CAS E CAS E CAS E

CAS E CAS E CAS E

CAS E CAS E CAS E 1 2

1 2

1 2

1 2 41 .

41 . 41 .

3 . 3 . 3 .

15 . 15 . 15 .

3 . 3 . 3 . 42 .

42 . 42 .

4 . 4 . 4 .

16 . 16 . 16 .

4 . 4 . 4 . 41 .

0 . 0 .

4 . 1 . 1 .

16 . 13 . 13 .

4 . 1 . 1 . 23 .

0 . 0 .

2 . 1 . 1 .

15 . 14 . 14 .

2 . 1 . 1 . 27 .

0 . 0 .

2 . 0 . 0 .

10 . 9 . 9 .

2 . 0 . 0 . 39 .

3 . 0 .

4 . 1 . 1 .

27 . 26 . 25 .

4 . 1 . 1 . 213 .

87 . 83 .

19 . 10 . 10 .

100 . 93 . 93 .

19 . 10 . 10 .

Tl C OTABL E 4~ 199 0 COST S (10**6 , •1985 )

10-5 0 BOILE RSIZ E (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L
ANNUALIZE

DCOST S TH E BAS E CAS E OPTIO N CAS E OPTIO N CAS E TOTA

L 1145. 0 1145. 0 1145. 0 948. 1

948. 1 948. 1 783. 5

784. 9 784. 9 617. 3

618. 1 618. 1 377. 4

379. 0 379. 0 1072. 1

1073. 7 1072. 6 4943. 5

4948. 9 4947. 8
CAPITA L COST S - TOTA

L TH E BAS E CAS E 1338. 5 1134. 9 792. 7 509. 9 300. 1 886. 2 4962. 3 OPTIO N CAS E 1 1338. 5 1134. 9 789. 6 508. 7 300. 1 886. 2 4958. 1 OPTIO N CAS E 2 1338. 5 1134. 9 789. 6 508. 7 300. 1 835. 5 4907. 3

T l PTABLE 5 — 199 0 NO

XCONTROLANNUALIZE DCOST S (10**6 , U985 )
BOILE RSIZ E (MMBTU/HR ) 10-5 0 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L
•TOTAL * TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2
NATURA L GAS AN

DOI L TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2
COA L TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2 0. 0

0. 0 0. 0

0. 0 0. 0 0. 0

0. 0 0. 0 0. 0 0. 0

0. 0 0. 0

0. 0 0. 0 0. 0

0. 0 0. 0 0. 0 0. 0

0. 0 0. 0

0. 0 0. 0 0. 0

0. 0 0. 0 0. 0 0. 0

0. 0 0. 0

0. 0 0. 0 0. 0

0. 0 0. 0 0. 0 0. 0

0. 0 0. 0

0. 0 0. 0 0. 0

0. 0 0. 0 0. 0 0. 0

0. 0 0. 0

0. 0 0. 0 0. 0

0. 0 0. 0 0. 0 0. 0

0. 0 0. 0

0. 0 0. 0 0. 0

0. 0 0. 0 0. 0TABL E 6 —199 0 NO XEMISSION S (10** 3 TONS )

10-5 0 BOILE RSIZ E (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L
"TOTAL " TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2
NATURA L GA S AN DOI L TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2
COA L THE BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2 15. 3

15. 3 15. 3

15. 3 15. 3 15. 3

0. 0 0. 0 0. 0 16. 4

16. 4 16. 4

16. 4 16. 4 16. 4

0. 0 0. 0 0. 0 16. 0

12. 7 12. 7

16. 0 12. 7 12. 7

0. 0 0. 0 0. 0 15. 4

14. 4 14. 4

15. 4 14. 4 14. 4

0. 0 0. 0 0. 0 10. 1

8. 7 8. 7

10. 1 8. 7 8. 7

0. 0 0. 0 0. 0 27. 0

25. 8 24. 9

25. 5 24. 3 24. 9

1. 5 1. 5 0. 0 100. 4

93. 4 92. 6

98. 9 91. 9 92. 6

1. 5 1. 5 0. 0

Tl
to

# 1

TABLE 7 — INDUSTRIA

L BOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 10-5 0

FUE L OEMAN D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L "TOTAL *
FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS OISTILUT E FUE

L OI L RESIDUA L FUEL OI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0
EMISSIONS ( XCHANG

E S0 2 P M NO X PM1 0
ANNUALIZE

DCOST S (10»*6 , *1985 > BOILE R FG DAN DP M

, NOX" " FUE L •TOTAL *FRO

M BAS E CASE ) TH E BAS E CAS E

1412 . 0 . 1412 .

102 . 0 . 30 . 0 . 132 .

40. 6 3. 4 15. 3 3. 4

0. 0 0. 0 0. 0 0. 0

619. 6 0. 0 0. 0 525. 4 1145. 0 OPTIO

N CAS E 1

1412 . 0 . 1412 .

102 . 0 . 30 . 0 . 132 .

40. 6 3. 4 15. 3 3. 4

0. 0 0. 0 0. 0 0. 0

619. 6 0. 0 0. 0 525. 4 1145. 0 OPTIO

N CAS E 2

1412 . 0 . 1412 .

102 . 0 . 30 . 0 . 132 .

40. 6 3. 4 15. 3 3. 4

0. 0 0. 0 0. 0 0. 0

619. 6 0. 0 0. 0 525. 4 1145. 0
ANNUALIZE

DCOST S (J C CHANG E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 0 0. 0
CAPITA L COST S (10**6 , «1985 ) BOILE R FG OAN DP M NO X "TOTAL * 1339 . 0 . 0 . 1339 . 1339 .

0 . 0 . 1339 . 1339 .

0 . 0 . 1339 .TABLE 8 — INDUSTRIA

L BOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 50-7 5

FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L •TOTAL *
FUEL DEMAN

D (10**1 2 BTUS ) NATURA L GAS . DISTILUT E FUEL OI L RESIDUA L FUEL OI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P N NO X PM1 0
EMISSIONS 17. CHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0
ANNUALIZE

DCOST S (10*«6 , *1985 ) BOILE R FG OAN DP M NOX" ' •
' FUEL «TOTAL * TH E BAS E CAS E

402 . 0 . 402 .

57 . 0 . 26 . 0 . 83 .

29. 2 2. 4 10. 4 2. 4

0. 0 0. 0 0. 0 0. 0

264. 8 0. 0 0. 0 329. 4 594. 1 OPTIO

N CAS E 1

402 . 0 . 402 .

57 . 0 . 26 . 0 . 83 .

29. 2 2. 4 10. 4 2. 4

0. 0 0. 0 0. 0 0. 0

264. 8 0. 0 0. 0 329. 4 594. 1 OPTIO

N CAS E 2

402 . 0 . 402 .

57 . 0 . 26 . 0 . 83 .

29. 2 2. 4 10. 4 2. 4

0. 0 0. 0 0. 0 0. 0

264. 8 0. 0 0. 0 329. 4 594. 1
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 0 0. 0
CAPITA L COST S (10**6 , $1985 ) BOILE R FG OAN DP M NO X •TOTAL * 735 . 0 . 0 . 735 . 735 .

0 . 0 . 735 . 735 .

0 . 0 . 735 .

T lTABLE 9 ~ INDUSTRIA L BOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 75-10 0

FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L GA S AN DOI L COA L "TOTAL *
FUE L DEMAN D (10**1 2 BTUS ) NATURA L GA S DISTILUT E FUE

L OI L RESIDUA L FUEL OI L COA L *TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0
EMISSIONS 17. CHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0
ANNUALIZE

DCOST S (10**6 , 91985 ) BOILE R FG DAN DP M

, NOX " ' FUEL •TOTAL * TH E BAS E CAS E

175 . 0 . 175 .

42 . 0 . 12 . 0 . 54 .

13. 3 1. 2 6. 0 1. 2

0. 0 0. 0 0. 0 0. 0

140. 5 0. 0 0. 0 213. 5 354. 0 OPTIO

N CAS E 1

175 . 0 . 175 .

42 . 0 . 12 . 0 . 54 .

13. 3 1. 2 6. 0 1. 2

0. 0 0. 0 0. 0 0. 0

140. 5 0. 0 0. 0 213. 5 354. 0 OPTIO

N CAS E 2

175 . 0 . 175 .

42 . 0 . 12 . 0 . 54 .

13. 3 1. 2 6. 0 1. 2

0. 0 0. 0 0. 0 0. 0

140. 5 0. 0 0. 0 213. 5 354. 0
ANNUALIZE

DCOST S 17. CHANG

E FRO M BAS E CASE ) *TOTAL * 

### 0. 0 0. 0 0. 0
CAPITA L COST S (10»*6 , $1985 ) BOILE R FG DAN DP M NO X •TOTAL * 400 . 0 . 0 . 400 . 400 .

0 . 0 . 400 . 400 .

0 . 0 . 400 .

T lTABLE 1 0 ~ INDUSTRIA LBOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 100-15 0

FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L *TOTAL *
FUE L DEMAN D (10**1 2 BTUS ) NATURA L GA S DISTILLATE FUEL OI L RESIDUA L FUEL OI L COA L *TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0
EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0
ANNUALIZE

DCOST S (10**6 , $1985 ) BOILE R FG DAN DP H • NO X- FUE L *TOTAL» BAS E CAS E

271 . 0 . 271 .

96 . 0 . 32 . 0 . 129 .

40. 9 3. 5 16. 0 3. 5

0. 0 0. 0 0. 0 0. 0

270. 1 0. 0 0. 0 513. 5 783. 5 OPTIO

N CAS E 1

271 . 0 . 271 .

129 . 0 . 0 . 0 . 129 .

0. 0 0. 6 12. 7 0. 6

-100. 0 -82. 9 -20. 6 -82. 9

269. 5 0. 0 0. 0 515. 4 784. 9 OPTIO

N CAS E 2

271 . 0 . 271 .

129 . 0 . 0 . 0 . 129 .

0. 0 0. 6 12. 7 0. 6

-100. 0 -82. 9 -20. 6 -82. 9

269. 5 0. 0 0. 0 515. 4 784. 9
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) »TOTAL * 0. 0 0. 2 0. 2
CAPITA L COST S (10**6 , $1985 ) BOILE R FG OAN DP M NO X •TOTAL * 793 . 0 . 0 . 793 . 790 .

0 . 0 . 790 . 790 .

0 . 0 . 790 .

T lTABLE 11 — INDUSTRIA

L BOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 150-20 0

FUE L DEMAN D (NUMBE RO F UNITS ) NATURA L 6AS AN

DOI L COA L *TOTAL«
FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS DISTILUT E FUE

L OI L RESIDUA L FUEL OI L COA L *TOTAL» EMISSIONS (10** 3 TONS ) S0 2 FH NO X PM1 0
EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P N NO X PM1 0
ANNUALIZE

DCOST S (10**6 , $1985 ) BOILE R FG OAN DP M

, NOX 1 FUEL *TOTAL * : BAS E CAS E

135 . 0 . 135 .

90 . 0 . 21 . 0 . U l .

23. 0 2. 2 15. 4 2. 2

0. 0 0. 0 0. 0 0. 0

174. 6 0. 0 0. 0 442. 7 617. 3 OPTIO

N CAS E 1

135 . 0 . 135 .

U l . 0 . 0 . 0 . U l .

0. 0 0. 6 14. 4 0. 6

-100. 0 -72. 7 -6. 5 -72. 7

174. 4 0. 0 0. 0 443. 6 618. 1 OPTIO

N CAS E 2

135 . 0 . 135 .

U l . 0 . 0 . 0 . U l .

0. 0 0. 6 14. 4 0. 6

-100. 0 -72. 7 -6. 5 -72. 7

174. 4 0. 0 0. 0 443. 6 618. 1
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 1 0. 1
CAPITA L COST S (10**6 , $1985 ) BOILE R FG OAN DP M NO X •TOTAL * 510 . 0 . 0 . 510 . 509 .

0 .

_ , 0 . 509 . 509 .

0 . 0 . 509 .

T lTABL E 1 2 — INDUSTRIA

L BOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE . 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 200-25 0

FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L 6AS AN

OOI L COA L "TOTAL *
FUEL DEMAN

D (10**1 2 BTUS ) NATURA L GAS . DISTILUT E FUEL OI L RESIDUA L FUE L OI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0
EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0
ANNUALIZE

DCOST S (10**6 , $1985 ) BOILE R FG DAN DP M NOX * "
' FUEL •TOTAL * TH E BAS E CAS E

62 . 0 . 62 .

47 . 0 . 20 . 0 . 67 .

26. 8 2. 2 10. 1 2. 2

0. 0 0. 0 0. 0 0. 0

113. 2 0. 0 0. 0 264. 1 377. 4 OPTIO

N CAS E 1

62 . 0 . 62 .

66 . 0 . 1 . 0 . 67 .

0. 4 0. 4 8. 7 0. 4

-98. 5 -81. 8 -13. 9 -81. 8

113. 2 0. 0 0. 0 265. 8 379. 0 OPTIO

N CAS E 2

62 . 0 . 62 .

67 . 0 . 0 . 0 . 67 .

0. 0 0. 3 8. 7 0. 3

-100. 0 -86. 4 -13. 9 -86. 4

113. 2 0. 0 0. 0 265. 8 379. 0
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 4 0. 4
CAPITA L COST S (10**6 , $1985 ) BOILE R FG OAN DP M NO X •TOTAL * 300 . 0 . 0 . 300 . 300 .

0 . 0 . 300 . 300 .

0 . 0 . 300 .TABLE 1 3 — INDUSTRIA

L BOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) > 25 0

FUE L DEMAN D (NUMBE RO F UNITS ) NATURA L 6AS AN

DOI L COA L •TOTAL *
FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS . DISTILUT E FUEL OI L RESIDUA L FUEL OI L COA L •TOTAL *
EMISSIONS (10»» 3 TONS ) S0 2 P M NO X PM1 0
EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0
ANNUALIZE

DCOST S (10**6 , $1985 ) BOILE R FG OAN DP M NOX - "
' FUE L *TOTAL« TH E BAS E CAS E

134 . 2 . 136 .

147 . 0 . 40 . 4 . 191 .

39. 2 3. 6 27. 0 3. 6

0. 0 0. 0 0. 0 0. 0

321. 7 2. 1 0. 0 748. 3 1072. 1 OPTIO

N CAS E 1

134 . 2 . 136 .

184 . 0 . 3 . 4 . 191 .

3. 4 1. 1 25. 8 1. 1

-91. 3 -69. 4 -4. 4 -69. 4

321. 7 2. 1 0. 0 749. 9 1073. 7 OPTIO

N CAS E 2

136 . 0 . 136 .

191 . 0 . 0 . 0 . 191 .

0. 1 1. 0 24. 9 1. 0

-99. 7 -72. 2 -7. 8 -72. 2

311. 6 0. 0 0. 0 761. 0 1072. 6
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) *TOTAL * 0. 0 0. 2 0. 0
CAPITA L COST S (10**6 , $1985 ) BOILE R FG DAN DP M NO X "TOTAL * 880 . 6 . 0 . 886 . 880 .

6 . 0 . 886 . 835 .

0 . 0 . 835 .

Tl C OTABLE 1 4 INDUSTRIA L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) > 10 0

FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L •TOTAL *
FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS . DISTILUT E FUE

L OI L RESIDUA L FUEL OI L COA L *TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0
EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0
ANNUALIZE

DCOST S (10**6 , $1985 ) BOILE R FG DAN DP M

, NOX ' FUEL •TOTAL * TH E BAS E CAS E

602 . 2 . 604 .

381 . 0 . 113 . 4 . 498 .

129. 9 11. 5 68. 5 11. 5

0. 0 0. 0 0. 0 0. 0

879. 7 2. 1 0. 0 1968. 6 2850. 3 OPTIO

N CAS E 1

602 . 2 . 604 .

490 . 0 . 4 . 4 . 498 .

3. 8 2. 7 61. 6 2. 7

-97. 1 -76. 5 -10. 1 -76. 5

879. 0 2. 1 0. 0 1974. 7 2855. 7 OPTIO

N CAS E 2

604 . 0 . 604 .

498 . 0 . 0 . 0 . 498 .

0. 1 2. 5 60. 7 2. 5

-99. 9 -78. 3 -11. 4 -78. 3

868. 8 0. 0 0. 0 1985. 8 2854. 6
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) *TOTAL * 0. 0 0. 2 0. 1
CAPITA L COST S (10**6 , $1985 ) BOILE R FG OAN DP H NO X •TOTAL * 2483 . 6 . 0 . 2489 . 2478 .

6 . 0 . 2485 . 2434 .

0 . 0 . 2434 .TABLE 1 5 — INDUSTRIA

LBOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE . 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 100-25 0

FUEL OEMAN

D (NUMBE RO F UNITS ) NATURA L 6AS AN

D COA L •TOTAL * OI L

FUE L DEMAN D (10**1 2 BTUS ) NATURA L 6AS . DISTILUT E FUE

L OI L RESIOUA L FUE L OI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0
EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 PH NO X PM1 0
ANNUALIZE

DCOST S (10**6 , $1985 ) BOILE R FG OAN DP H NOX * FUEL •TOTAL * TH E BAS E CAS E

468 . 0 . 468 .

234 . 0 . 73 . 0 . 307 .

90. 7 7. 9 41. 5 7. 9

0. 0 0. 0 0. 0 0. 0

557. 9 0. 0 0. 0 1220. 3 1778. 2 OPTIO

N CAS E 1

468 . 0 . ' 468 .

306 . 0 . 1 . 0 . 307 .

0. 4 1. 6 35. 8 1. 6

-99. 6 -79. 7 -13. 7 -79. 7

557. 2 0. 0 0. 0 1224. 8 1782. 0 OPTIO

N CAS E 2

468 . 0 . 468 .

307 . 0 . 0 . 0 . 307 .

0. 0 1. 5 35. 8 1. 5

-100. 0 -81. 0 -13. 7 -81. 0

557. 2 0. 0 0. 0 1224. 8 1782. 0
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) *TOTAL * 0. 0 0. 2 0. 2
CAPITA L COST S (10**6 , $1985 ) BOILE R FG DAN DP M NO X •TOTAL * 1603 . 0 . 0 . 1603 . 1598 .

0 . 0 . 1598 . 159 8

0 0 159 8

T lTABLE 1 6 INDUSTRIA LBOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) > 5 0

FUE L DEMAN D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L •TOTAL *
FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS . DISTILUT E FUEL OI L RESIDUA L FUE L OI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0
EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 PH NO X PM1 0
ANNUALIZE

DCOST S (10**6 , $1985 ) BOILE R FG DAN DP M NO X FUEL •TOTAL * TH E BAS E CAS E

1179 . 2 . 1161 .

479 . 0 . 151 . 4 . 634 .

172. 4 15. 1 84. 9 15. 1

0. 0 0. 0 0. 0 0. 0

1284. 9 2. 1 0. 0 2511. 5 3798. 5 OPTIO

N CAS E 1

1179 . 2 . 1181 .

588 . 0 . 41 . 4 . 634 .

46. 3 6. 3 78. 0 6. 3

-73. 1 -58. 3 -8. 1 -58. 3

1284. 2 2. 1 0. 0 2517. 6 3803. 9 OPTIO

N CAS E 2

1181 . 0 . 1181 .

597 . 0 . 37 . 0 . 634 .

42. 6 6. 1 77. 1 6. 1

-75. 3 -59. 6 -9. 2 -59. 6

1274. 1 0. 0 0. 0 2528. 7 3802. 7
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 1 0. 1
CAPITA L COST S (10**6 , $1985 ) BOILE R FG OAN DP H NO X •TOTAL * 3618 . 6 . 0 . 3624 . 3613 .

6 . 0 . 3620 . 3569 .

0 . 0 . 3569 .

r oTABLE 1 7 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) TOTA L

FUE L DEMAN D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L •TOTAL *
FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS DISTILUT E FUEL OI L RESIDUA L FUE L OI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PH1 0
EMISSIONS ( XCHANG

E S0 2 PH NO X PH1 0
ANNUALIZE

DCOST S (10**6 , $1985 ) BOILE R FG OAN DP H NOX - • •
' FUEL •TOTAL * FRO M BAS E CASE ) TH E BAS E CAS E

2591

. 2

. 2593

.

581

. 0

. 181

. 4'

. 766

.

212. 9 18. 5 100. 4 18. 5

0. 0 0. 0 0. 0 0. 0

1904. 6 2. 1 0. 0 3036. 8 4943. 5 OPTIO N

CAS E 1

2591

. 2

. 2593

.

690

. 0

. 7 1

. 4

. 766

.

86. 9 9. 8 93. 4 9. 8

-59. 2 -47. 0 -7. 0 -47. 0

1903. 9 2. 1 0. 0 3042. 9 4948. 9 OPTIO N

CASE 2

2593

. 0

. 2593

.

699

. 0

. 67

. 0

. 766

.

83. 2 9. 6 92. 6 9. 6

-60. 9 -48. 1 -7. 8 -46. 1

1893. 7 0. 0 0. 0 3054. 1 4947. 8
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 1 0. 1
CAPITA L COST S (10**6 , $1985 ) BOILE R FG OAN DP M NO X •TOTAL * 4956

. 6

. 0

. 4962

. 4952

.

6

. 0

. 4958

. 4907

.

0

. 0

. 4907

.SIZ E CUSS : 100-15 0 TABLE 1 8 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0
S0 2 EMISSIONS (SHOR T TONS )

BAS E CAS E NEHENG . NAT . GAS 1. 0 RESI DOI L 234. 0 COA L 0. 0 TOTA L 235. 0

OPTIO N CAS E 1 NEHENG . NAT . GAS 1. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 1. 0

OPTIO N CAS E 2 NEHENG . NAT . GAS 1. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 1. 0 N.Y./N.J . 1. 0 1025. 0 0. 0 1026. 0

N.Y./N.J . 1. 0 0. 0 0. 0 1. 0

N.Y./N.J . 1. 0 0. 0 0. 0 1. 0 MID . ATL .

1. 0 5994. 0 0. 0 5996. 0

MID .

MID . ATL . 3. 0 0. 0 0. 0 3. 0

ATL . 3. 0 0. 0 0. 0 3. 0 SO . ATL .

4. 0 8260. 0 0. 0 8264. 0

SO .

SO . ATL . 5. 0 0. 0 0. 0 5. 0

ATL . 5. 0 0. 0 0. 0 5. 0 MIDHES T

3. 0 15440. 0 0. 0 15443. 0

MIDHES T 7. 0 0. 0 0. 0 7. 0

MIDHES T 7. 0 0. 0 0. 0 7. 0 SO . HES T

11. 0 0. 0 0. 0 11. 0

SO . HES T 11. 0 0. 0 0. 0 11. 0

SO . HES T 11. 0 0. 0 0. 0 11. 0 CENTRA

L 0. 0 8172. 0 0. 0 8173. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0 NO .

NO .

NO . CNTR

L 3. 0 0. 0 0. 0 3. 0

CNTR L 3. 0 0. 0 0. 0 3. 0

CNTR L 3. 0 0. 0 0. 0 3. 0 HES T

3. 0 1750. 0 0. 0 1753. 0

HES T 3. 0 0. 0 0. 0 3. 0

HES T 3. 0 0. 0 0. 0 3. 0 NO .

NO .

NO . HES T 2. 0 0. 6 0. 0 2. 0

HES T 2. 0 0. 0 0. 0 2. 0

HES T 2. 0 0. 0 0. 0 2. 0 U S TOTA

L 29. 0 40876. 0 0. 0 40905. 0

U S

U S TOTA L 39. 0 0. 0 0. 0 39. 0

TOTA L 39. 0 0. 0 0. 0 39. 0SIZ E CUSS : 150-20 0 TABLE 1 9 — INDUSTRIA

L BOILE RNSP S REGIONA

LIMPACT S B

YBOILE RSIZE . 1986-199 0
S0 2 EMISSIONS (SHOR T TONS )

BAS E CAS E NEHENG . NAT . 6A S 0. 0 RESI DOI L 590. 0 COA L 0. 0 TOTA L 590. 0

OPTIO N CAS E 1 NEHENG . NAT . GAS 1. 0 RESI OOI L 0. 0 COA L 0. 0 TOTA L 1. 0

OPTIO N CAS E 2 NEHENG . NAT' . GAS 1. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 1. 0 N.Y./N.J . 1. 0 590. 0 0. 0 591. 0

N.Y./N.J . 1. 0 0. 0 0. 0 1. 0

N.Y./N.J . 1. 0 0. 0 0. 0 1. 0 HID . ATL .

2. 0 4063. 0 0. 0 4065. 0

MID .

HID . ATL . 3. 0 0. 0 0. 0 3. 0

ATL . 3. 0 0. 0 0. 0 3. 0 SO . ATL .

4. 0 2953. 0 0. 0 2956. 0

SO .

SO . ATL . 4. 0 0. 0 0. 0 4. 0

ATL . 4. 0 0. 0 0. 0 4. 0 MIDHES T

2. 0 12590. 0 0. 0 12591. 0

MIDHES T 5. 0 0. 0 0. 0 5. 0

MIDHES T 5. 0 0. 0 0. 0 5. 0 SO . HES T

11. 0 0. 0 0. 0 11. 0

SO . HES T 11. 0 0. 0 0. 0 11. 0

SO . HES T 11. 0 0. 0 0. 0 11. 0 CENTRA

L 1. 0 2214. 0 0. 0 2216. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0 NO .

NO .

NO . CNTR

L 2. 0 0. 0 0. 0 2. 0

CNTR L 2. 0 0. 0 0. 0 2. 0

CNTR L 2. 0 0. 0 0. 0 2. 0 HES T

3. 0 0. 0 0. 0 3. 0

HES T 3. 0 0. 0 0. 0 3. 0

HES T 3. 0 0. 0 0. 0 3. 0 NO .

NO .

NO . HES T 3. 0 0. 0 0. 0 3. 0

HES T 3. 0 0. 0 0. 0 3. 0

HES T 3. 0 0. 0 0. 0 3. 0 U S TOTA

L 27. 0 23000. 0 0. 0 23027. 0

U S

U S TOTA L 33. 0 0. 0 0. 0 33. 0

TOTA L 33. 0 0. 0 0. 0 33. 0



# IN > O lSIZ E CUSS : 200-25 0 TABLE 2 0 — INDUSTRIA

L BOILE RNSP S REGIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
S0 2 EMISSIONS (SHOR T TONS )

BAS E CAS E NEHENG . NAT . GAS 0. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 0. 0

OPTIO N CAS E 1 NEHENG . NAT . GAS 0. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 0. 0

OPTIO N CAS E 2 NEHENG . NAT . GAS 0. 0 RESI OOI L 0. 0 COA L 0. 0 TOTA L 0. 0 N.Y./N.J . 0. 0 354. 0 0. 0 355. 0

N.Y./N.J . 0. 0 354. 0 0. 0 355. 0

N.Y./N.J . 1. 0 0. 0 0. 0 1. 0 MID . ATL .

1. 0 3539. 0 0. 0 3540. 0

MID .

MID . ATL . 2. 0 0. 0 0. 0 2. 0

ATL . 2. 0 0. 0 0. 0 2. 0 SO . ATL .

2. 0 5220. 0 0. 0 5221. 0

SO .

SO . ATL . 3. 0 0. 0 0. 0 3. 0

ATL . 3. 0 0. 0 0. 0 3. 0 MIDHES T

0. 0 14497. 0 0. 0 14498. 0

MIDHES T 3. 0 0. 0 0. 0 3. 0

MIDHES T 3. 0 0. 0 0. 0 3. 0 SO .

SO .

SO . HES T 8. 0 0. 0 0. 0 8. 0

HES T 8. 0 0. 0 0. 0 8. 0

HES T 8. 0 0. 0 0. 0 8. 0 CENTRA

L 0. 0 3163. 0 0. 0 3163. 0

CENTRA L 1. 0 0. 0 0. 0 1. 0

CENTRA L 1. 0 0. 0 0. 0 1. 0 NO .

NO .

NO . CNTR

L 1. 0 0. 0 0. 0 1. 0

CNTR L 1. 0 0. 0 0. 0 1. 0

CNTR L 1. 0 0. 0 0. 0 1. 0 HES T

1. 0 0. 0 0. 0 1. 0

HES T 1. 0 0. 0 0. 0 1. 0

HES T 1. 0 0. 0 0. 0 1. 0 NO .

NO .

NO . HES T 1. 0 0. 0 0. 0 1. 0

HES T 1. 0 0. 0 0. 0 1. 0

HES T 1. 0 0. 0 0. 0 1. 0 U S TOTA

L 14. 0 26774. 0 0. 0 26788. 0

U S TOTA L 20. 0 354. 0 0. 0 374. 0

U S TOTA L 20. 0 0. 0 0. 0 20. 0SIZ E CUSS : > 25 0 TABL E 2 1 — INDUSTRIA

LBOILE RNSP S REGIONA

L IHPACT S B

YBOILE RSIZE , 1986-199 0 S0 2 EMISSIONS (SHOR T TONS )

BAS E
NAT . GAS RESI DOI L COA L TOTA L CAS E

NEHENG . 0. 0 1095. 0 0. 0 1096. 0

OPTIO N CAS E 1
NAT . GAS RESI DOI L COA L TOTA L NEHENG .

1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 2
NAf \ GAS RESI DOI L COA L TOTA L NEHENG .

1. 0 0. 0 0. 0 1. 0 N

N

N .Y./N.J . 1. 0 2475. 0 0. 0 2476. 0

.Y./N.J . 1. 0 1308. 0 0. 0 1309. 0

.Y./N.J . 2. 0 0. 0 0. 0 2. 0 MID . ATL .

2. 0 9372. 0 0. 0 9373. 0

MID .

HID . ATL . 5. 0 0. 0 0. 0 5. 0

ATL . 5. 0 0. 0 0. 0 5. 0 SO . ATL .

8. 0 1142. 0 0. 0 1150. 0

SO .

SO . ATL . 8. 0 0. 0 0. 0 8. 0

ATL . 8. 0 0. 0 0. 0 8. 0 HIDHES T

3. 0 18959. 0 0. 0 18962. 0

HIDHES T 9. 0 0. 0 0. 0 9. 0

HIDHES T 9. 0 0. 0 0. 0 9. 0 SO

SO

S O . HES T 20. 0 0. 0 0. 0 20. 0

. HES T 20. 0 0. 0 0. 0 20. 0

. HES T 20. 0 0. 0 0. 0 20. 0 CENTRA

L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0 NO . CNTR

L 2. 0 0. 0 2028. 0 2030. 0

NO . CNTR

L 2. 0 0. 0 2028. 0 2030. 0

NO . CNTR

L 3. 0 0. 0 0. 0 3. 0 HES T

3. 0 4036. 0 0. 0 4039. 0

HES T 4. 0 0. 0 0. 0 4. 0

HES T 4. 0 0. 0 0. 0 4. 0 NO .

NO .

NO . HES T 4. 0 0. 0 0. 0 4. 0

HES T 4. 0 0. 0 0. 0 4. 0

HES T 4. 0 0. 0 0. 0 4. 0 U S TOTA

L 44. 0 37079. 0 2028. 0 39151. 0

U S TOTA L 55. 0 1308. 0 2028. 0 3392. 0

U S TOTA L 57. 0 0. 0 0. 0 57. 0SIZ E CUSS : 100-15 0 TABL E 2 2 — INDUSTRIA

L BOILE RNSP S REGIONA

L IHPACT S B

YBOILE RSIZE , 1986-199 0
FOSSI LFUE

L DEMAN D(10*» 9 BTUS )

BAS E CAS E NEHENG . NAT . GAS 2409. 0 RESI OOI L 274. 0 COA L 0. 0 TOTA L 2683. 0

OPTIO N CAS E 1 NEHENG . NAT . 6A S 2683. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 2683. 0

OPTIO N CAS E 2 NEHENG . NAT* . GAS 2683. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 2683. 0 N

N

N •Y./N.J . 2409. 0 767. 0 0. 0 3176. 0

•Y./N.J . 3176. 0 0. 0 0. 0 3176. 0

.Y./N.J . 3176. 0 0. 0 0. 0 3176. 0 MID . ATL .

4380. 0 5858. 0 0. 0 10238. 0

MID . ATL . 10238. 0 0. 0 0. 0 10238. 0

MID . ATL . 10238. 0 0. 0 0. 0 10238. 0 SO . ATL .

12538. 0 5147. 0 0. 0 17684. 0

SO . ATL . 17684. 0 0. 0 0. 0 17684. 0

SO . ATL . 17684. 0 0. 0 0. 0 17684. 0 HIDHES T

9636. 0 13304. 0 0. 0 22940. 0

HIDHES T 22940. 0 0. 0 0. 0 22940. 0

HIDHES T 22940. 0 0. 0 0. 0 22940. 0 SO . HES T

37613. 0 0. 0 0. 0 37613. 0

SO . HES T 37613. 0 0. 0 0. 0 37613. 0

SO . HES T 37613. 0 0. 0 0. 0 37613. 0 CENTRA

L 1095. 0 5092. 0 0. 0 6187. 0

CENTRA L 6187. 0 0. 0 0. 0 6187. 0

CENTRA L 6187. 0 0. 0 0. 0 6187. 0 NO . CNTR

L 9362. 0 0. 0 0. 0 9362. 0

NO . CNTR

L 9362. 0 0. 0 0. 0 9362. 0

NO . CNTR

L 9362. 0 0. 0 0. 0 9362. 0 HES T

9417. 0 1807. 0 0. 0 11224. 0

HES T 11224. 0 0. 0 0. 0 11224. 0

HES T 11224. 0 0. 0 0. 0 11224. 0 NO . HES T

7501. 0 0. 0 0. 0 7501. 0

NO . HES T 7501. 0 0. 0 0. 0 7501. 0

NO . HES T 7501. 0 0. 0 0. 0 7501. 0 U S TOTA

L 96360. 0 32248. 0 0. 0 128608. 0

U S TOTA L 128608. 0 0. 0 0. 0 128608. 0

U S TOTA L 128608. 0 0. 0 0. 0 128608. 0SIZ E CUSS : 150-20 0 TABLE 2 3 — INDUSTRIA

L BOILE RNSP S REGIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
FOSSI LFUE

L DEMAN D(10** 9 BTUS )

BAS E CAS E NEHENG . NAT . GAS 1380. 0 RESI DOI L 690. 0 COA L 0. 0 TOTA L 2070. 0

OPTIO N CAS E 1 NEHENG . NAT . GAS 2070. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 2070. 0

OPTIO N CAS E 2 NEHENG . NAf . GAS 2070. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 2070. 0 N

N

N •Y./N.J . 3219. 0 690. 0 0. 0 3909. 0

.Y./N.J . 3909. 0 0. 0 0. 0 3909. 0

.Y./N.J . 3909. 0 0. 0 0. 0 3909. 0 MIO . ATL .

5059. 0 4752. 0 0. 0 9811. 0

HID . ATL . 9811. 0 0. 0 0. 0 9811. 0

MID . ATL . 9811. 0 0. 0 0. 0 9811. 0 SO . ATL .

12877. 0 1840. 0 0. 0 14717. 0

SO . ATL . 14717. 0 0. 0 0. 0 14717. 0

SO . ATL . 14717. 0 0. 0 0. 0 14717. 0 MIDHES T

5289. 0 11497. 0 0. 0 16786. 0

MIDHES T 16786. 0 0. 0 0. 0 16786. 0

MIDHES T 16786. 0 0. 0 0. 0 16786. 0 SO . HES T

35182. 0 0. 0 0. 0 35182. 0

SO . HES T 35182. 0 0. 0 0. 0 35182. 0

SO . HES T 35182. 0 0. 0 0. 0 35182. 0 CENTRA

L 3679. 0 1380. 0 0. 0 5059. 0

CENTRA L 5059. 0 0. 0 0. 0 5059. 0

CENTRA L 5059. 0 0. 0 0. 0 5059. 0 NO . CNTR

L 5979. 0 0. 0 0. 0 5979. 0

NO . CNTR

L 5979. 0 0. 0 0. 0 5979. 0

NO . CNTR

L 5979. 0 0. 0 0. 0 5979. 0 HES T

8508. 0 0. 0 0. 0 8508. 0

HES T 8508. 0 0. 0 0. 0 8508. 0

HES T 8508. 0 0. 0 0. 0 8508. 0 NO . HES T

9198. 0 0. 0 0. 0 9198. 0

NO . HES T 9198. 0 0. 0 0. 0 9198. 0

NO . HES T 9198. 0 0. 0 0. 0 9198. 0 U S TOTA

L 90370. 0 20849. 0 0. 0 111219. 0

U S TOTA L 111219. 0 0. 0 0. 0 111219. 0

U S TOTA L 111219. 0 0. 0 0. 0 111219. 0i

. l r

SIZ E CUSS : 200-25 0 TABL E 2 4—INDUSTRIA LBOILE R NSPS REGIONA LIMPACTS B YBOILE R SIZE , 1986-199 0 FOSSI LFUE LDEMAND (10** 9 BTUS)

BAS E CAS E NE H ENG

. NAT

. GA

S 887. 0 RESI D OI L0. 0 COA L0. 0 TOTA L887. 0

OPTIO N CASE 1 NE H ENG

. NAT

. 6A S 887. 0 RESI D OI L0. 0 COA L0. 0 TOTA L887. 0

OPTIO N CASE 2 NE H ENG

. NAT 1

. GA S 887. 0 RESI D OI L0. 0 COA L0. 0 TOTA L867. 0 N

N

N .Y./N.J

. 887. 0 887. 0 0. 0 1774. 0

.Y./N.J

. 887. 0 887. 0 0. 0 1774. 0

.Y./N.J

. 1774. 0 0. 0 0. 0 1774. 0 MID

. ATL

.

2365. 0 4139. 0 0. 0 6504. 0

HID

. ATL

. 6504. 0 0. 0 0. 0 6504. 0

HID

. ATL

. 6504. 0 0. 0 0. 0 6504. 0 SO

. ATL

.

5814. 0 3252. 0 0. 0 9067. 0

SO

. ATL

. 9067. 0 0. 0 0. 0 9067. 0

SO

. ATL

. 9067. 0 0. 0 0. 0 9067. 0 HIDHES T

1478. 0 9954. 0 0. 0 11432. 0

HIDHES T 11432. 0 0. 0 0. 0 11432. 0

HIDHES T 11432. 0 0. 0 0. 0 11432. 0 SO

. HEST

26411. 0 0. 0 0. 0 26411. 0

SO

. HEST 26411. 0 0. 0 0. 0 26411. 0

SO

. HEST 26411. 0 0. 0 0. 0 26411. 0 CENTRAL

0. 0 1971. 0 0. 0 1971. 0

CENTRAL 1971. 0 0. 0 0. 0 1971. 0

CENTRAL 1971. 0 0. 0 0. 0 1971. 0 NO

. CNTR L

3252. 0 0. 0 0. 0 3252. 0

NO

. CNTR L 3252. 0 0. 0 0. 0 3252. 0

NO

. CNTR L 3252. 0 0. 0 0. 0 3252. 0 HES

T 3055. 0 0. 0 0. 0 3055. 0

HES T 3055. 0 0. 0 0. 0 3055. 0

HES T 3055. 0 0. 0 0. 0 3055. 0 NO

. HEST

2661. 0 0. 0 0. 0 2661. 0

NO

. HEST 2661. 0 0. 0 0. 0 2661. 0

NO

. HEST 2661. 0 0. 0 0. 0 2661. 0 U S TOTA L

46811. 0 20203. 0 0. 0 67014. 0

U S TOTA L 66127. 0 887. 0 0. 0 67014. 0

U S TOTA L 67014. 0 0. 0 0. 0 67014. 0SIZ E CUSS : > 25 0 TABLE 2 5 — INDUSTRIA

L BOILE RNSP S REGIONA

L IHPACT S B

YBOILE RSIZE , 1986-199 0
FOSSI LFUELDEMAN

D(10** 9 BTUS )

BAS E CAS E NEHENG . NAT . GAS 712. 0 RESI DOI L 1281. 0 COA L 0. 0 TOTA L 1993. 0

OPTIO N CAS E 1 NEHENG . NAT . GAS 1993. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 1993. 0

OPTIO N CAS E 2 NEHENG . NAT . 6A S 1993. 0 RESI DOI L 0. 0 COA L 0. 0 TOTA L 1993. 0 N

N

N .Y./N.J . 2135. 0 3274. 0 0. 0 5409. 0

.Y./N.J . 2135. 0 3274. 0 0. 0 5409. 0

.Y./N.J . 5409. 0 0. 0 0. 0 5409. 0 MID . ATL .

5979. 0 10961. 0 0. 0 16940. 0

HID . ATL . 16940. 0 0. 0 0. 0 16940. 0

HID . ATL . 16940. 0 0. 0 0. 0 16940. 0 SO . ATL .

25765. 0 712. 0 0. 0 26477. 0

SO . ATL . 26477. 0 0. 0 0. 0 26477. 0

SO . ATL . 26477. 0 0. 0 0. 0 26477. 0 HIDHES T

10107. 0 20925. 0 0. 0 31032. 0

HIDHES T 31032. 0 0. 0 0. 0 31032. 0

MIDHES T 31032. 0 0. 0 0. 0 31032. 0 SO . HES T

65766. 0 0. 0 0. 0 65766. 0

SO . HES T 65766. 0 0. 0 0. 0 65766. 0

SO . HES T 65766. 0 0. 0 0. 0 65766. 0 CENTRA

L 6690. 0 0. 0 0. 0 6690. 0

CENTRA L 6690. 0 0. 0 0. 0 6690. 0

CENTRA L 6690. 0 0. 0 0. 0 6690. 0 NO . CNTR

L 5979. 0 0. 0 4271. 0 10249. 0

NO . CNTR

L 5979. 0 0. 0 4271. 0 10249. 0

NO . CNTR

L 10249. 0 0. 0 0. 0 10249. 0 HES T

10676. 0 2847. 0 0. 0 13523. 0

HES T 13523. 0 0. 0 0. 0 13523. 0

HES T 13523. 0 0. 0 0. 0 13523. 0 NO . HES T

13239. 0 0. 0 0. 0 13239. 0

NO . HES T 13239. 0 0. 0 0. 0 13239. 0

NO . HES T 13239. 0 0. 0 0. 0 13239. 0 U S TOTA

L 147047. 0 40000. 0 4271. 0 191318. 0

U S TOTA L 163774. 0 3274. 0 4271. 0 191318. 0

U S TOTA L 191318. 0 0. 0 0. 0 191318. 0

Tl C OSIZ E CUSS : 100-15 0 TABLE 2 6 — INDUSTRIA

LBOILE RNSP S REGIONA

LIHPACT S B

YBOILE RSIZE . 1986-199 0
ANNUALIZE

DCOST S (10** 6 198 5 $ )

BAS E CAS E NEHENG . NAT . GAS 16. 3 RESI DOI L 2. 1 COA L 0. 0 TOTA L 16. 4

OPTIO N CAS E 1 NEHENG . NAT . 6AS 18. 4 RESIOOI L 0. 0 COA L 0. 0 TOTA L 18. 4

OPTIO N CAS E 2 NEHENG . NAY . GAS 18. 4 RESI DOI L 0. 0 COA L 0. 0 TOTA L 18. 4 N.Y./N.J

. 15. 4 5. 0 0. 0 20. 3

N.Y./N.J

. 20. 6 0. 0 0. 0 20. 6

N.Y./N.J

. 20. 6 0. 0 0. 0 20. 6 MI D

MI D

MI D . ATL
. 27. 4 36. 9 0. 0 64. 4

. ATL
. 64. 8 0. 0 0. 0 64. 8

. ATL
. 64. 8 0. 0 0. 0 64. 8 SO

. ATL
.

78. 1 32. 0 0. 0 110. 2

SO

. ATL
. 110. 6 0. 0 0. 0 110. 6

SO

. ATL
. 110. 6 0. 0 0. 0 110. 6 HIDHES T

61. 4 87. 2 0. 0 146. 6

HIDHES T 149. 0 0. 0 0. 0 149. 0

HIDHES T 149. 0 0. 0 0. 0 149. 0 SO

. HES T

205. 8 0. 0 0. 0 205. 8

SO

. HES T 205. 8 0. 0 0. 0 205. 8

SO

. HES T 205. 8 0. 0 0. 0 205. 8 CENTRAL

8. 0 31. 8 0. 0 39. 8

CENTRA L 39. 4 0. 0 0. 0 39. 4

CENTRAL 39. 4 0. 0 0. 0 39. 4 NO

.

NO

.

NO

. CNTRL 58. 8 0.0

. 0. 0 58. 8

CNTRL 58. 8 0. 0 0. 0 58. 8

CNTRL 58. 8 0. 0 0. 0 58. 8 HES T

60. 7 11. 9 0. 0 72. 7

HES T 72. 8 0. 0 0. 0 72. 8

HES T 72. 8 0. 0 0. 0 72. 8 NO

NO

NO . HES T 44. 6 0. 0 0. 0 44. 6

. HES T 44. 6 0. 0 0. 0 44. 6

. HES T 44. 6 0. 0 0. 0 44. 6 U S TOTA

L 576. 5 207. 0 0. 0 783. 5

U S TOTAL 784. 9 0. 0 0. 0 784. 9

U S TOTAL 784. 9 0. 0 0. 0 784. 9SIZ E CUSS : 150-20 0 TABLE 2 7 — INDUSTRIA

LBOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0
ANNUALIZE

DCOST S (10** 6 198 5 $ )

BAS E CAS E NEHENG . NAT . 6A S 8. 4 RESI OOI L 4. 1 COA L 0. 0 TOTA L 12. 5

OPTIO N CAS E 1 NEHENG . NAT . GAS 12. 5 RESI DOI L 0. 0 COA L 0. 0 TOTA L 12. 5

OPTIO N CAS E 2 NEHENG . NAY . GAS 12. 5 RESI DOI L 0. 0 COA L 0. 0 TOTA L 12. 5 N.Y./N.J . 19. 7 4. 1 0. 0 23. 7

N.Y./N.J . 24. 0 0. 0 0. 0 24. 0

N.Y./N.J . 24. 0 0. 0 0. 0 24. 0 MI D

MI D

HI D . ATL . 29. 4 27. 8 0. 0 57. 2

. ATL . 57. 4 0. 0 0. 0 57. 4

. ATL . 57. 4 0. 0 0. 0 57. 4 SO

SO

SO . ATL . 72. 9 10. 1 0. 0 83. 0

. ATL . 83. 1 0. 0 0. 0 63. 1

. ATL . 83. 1 0. 0 0. 0 83. 1 HIDHES T

31. 4 67. 5 0. 0 98. 9

HIDHES T 99. 0 0. 0 0. 0 99. 0

HIDHES T 99. 0 0. 0 0. 0 99. 0 SO . HES T

182. 3 0. 0 0. 0 182. 3

SO . HES T 162. 3 0. 0 0. 0 182. 3

SO . HES T 182. 3 0. 0 0. 0 182. 3 CENTRA

L 20. 5 8. 0 0. 0 28. 5

CENTRA L 26. 4 0. 0 0. 0 28. 4

CENTRA L 28. 4 0. 0 0. 0 28. 4 NO .

NO .

NO . CNTR

L 33. 4 0. 0 0. 0 33. 4

CNTR L 33. 4 0. 0 0. 0 33. 4

CNTR L 33. 4 0. 0 0. 0 33. 4 HES T

49. 4 0. 0 0. 0 49. 4

HES T 49. 4 0. 0 0. 0 49. 4

HES T 49. 4 0. 0 0. 0 49. 4 NO . HES T

48. 4 0. 0 0. 0 48. 4

NO . HES T 48. 4 0. 0 0. 0 48. 4

NO . HES T 48. 4 0. 0 0. 0 48. 4 U S TOTA

L 495. 7 121. 6 0. 0 617. 3

U S TOTA L 618. 1 0. 0 0. 0 618. 1

U S TOTA L 618. 1 0. 0 0. 0 618. 1SIZ E CUSS : 200-25 0 TABL E 2 8 — INDUSTRIA

L BOILE

RNSP S REGIONA

L IMPACT S B

YBOILE

RSIZE , 1986-199 0

ANNUALIZE

DCOST S (10** 6 198 5 $ ) e •• » .i

BAS E

NAT . GA S RESI DOI L COA L TOTA L CAS E

NEH ENG . 5. 5 0. 0 0. 0 5. 5

OPTIO N CAS E 1

NAT . GA S RESI DOI L COA L TOTA L NEH EN6 . 5. 5 0. 0 0. 0 5. 5

OPTIO N CAS E 2

NAY . GA S RESI OOI L COA L TOTA L NEH ENG . 5. 5 0. 0 0. 0 5. 5 N

N

N Y

Y

Y ./N.J . 5. 6 5. 6 0. 0 11. 2

./N.J . 5. 6 5. 6 0. 0 11. 2

./N.J . 11. 2 0. 0 0. 0 11. 2 MID . ATL .

13. 9 24. 5 0. 0 38. 4

HID . ATL . 38. 6 0. 0 0. 0 38. 6

HID . ATL . 38. 6 0. 0 0. 0 38. 6 SO

SO

S O . ATL . 33. 3 18. 4 0. 0 51. 7

. ATL . 52. 0 0. 0 0. 0 52. 0

. ATL . 52. 0 0. 0 0. 0 52. 0 HIDHES T

8. 6 58. 4 0. 0 67. 0

MIDHES T 68. 3 0. 0 0. 0 68. 3

MIDHES T 68. 3 0. 0 0. 0 68. 3 SO . HES T

140. 3 0. 0 0. 0 140. 3

- - - SO . HES T 140. 3 0. 0 0. 0 140. 3

SO . HES T 140. 3 0. 0 0. 0 140. 3 CENTRA L

0. 0 11. 6 0. 0 11. 6

CENTRAL 11. 5 0. 0 0. 0 11. 5

CENTRA L 11. 5 0. 0 0. 0 11. 5 NO .

NO .

NO . CNTR L 18. 6 0. 0 0. 0 18. 6

CNTR L 18. 6 0. 0 0. 0 18. 6

CNTR L 18. 6 0. 0 0. 0 18. 6 HES T

18. 2 0. 0 0. 0 18. 2

HES T

. 18. 2 0. 0 0. 0 18. 2

HES T 18. 2 0. 0

. 0. 0 18. 2 N

O

N O

N O HES T 14. 8 0. 0 0. 0 14. 8

. HES T 14. 8 0. 0 0. 0 14. 8

HES T 14. 8 0. 0 0. 0 14. 8 U S TOTA L

256. 9 116. 4 0. 0 377. 4

U S TOTA L 373. 4 5. 6 0. 0 379. 0

U S TOTA L 379. 0 0. 0 0. 0 379. 0SIZ E CUSS : > 25 0 TABL E 2 9 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0
ANNUALIZE

DCOST S (10** 6 198 5 $ )

BASE
NAT . GAS RESI DOI L COA L TOTA L : CAS E

NEHENG . 5. 0 7. 5 0. 0 12. 5

OPTIO N CAS E 1
NAT . GAS RESI DOI L COA L TOTA L NEHENG .

12. 7 0. 0 0. 0 12. 7

OPTIO N CAS E 2
NAT . 6AS RESIOOI L COA L TOTA L NEHENG .

12. 7 0. 0 0. 0 12. 7 N

N

N Y

Y

Y ./N.J . 12. 6 20. 3 0. 0 32. 9

./N.J . 12. 6 21. 1 0. 0 33. 7

./N.J . 33. 7 0. 0 0. 0 33. 7 MID . ATL .

34. 8 63. 1 0. 0 97. 9

MID . ATL . 98. 4 0. 0 0. 0 98. 4

MID . ATL . 98. 4 0. 0 0. 0 98. 4 SO . ATL .

145. 2 4. 7 0. 0 149. 9

SO . ATL . 150. 0 0. 0 0. 0 150. 0

SO . ATL . 150. 0 0. 0 0. 0 150. 0 MIDHES T

59. 8 125. 1 0. 0 164. 8

MIDHES T 184. 2 0. 0 0. 0 184. 2

MIDHES T 184. 2 0. 0 0. 0 184. 2 SO . HES T

343. 1 0. 0 0. 0 343. 1

SO . HES T 343. 1 0. 0 0. 0 343. 1

SO . HES T 343. 1 0. 0 0. 0 343. 1 CENTRA

L 38. 4 0. 0 0. 0 38. 4

CENTRA L 38. 4 0. 0 0. 0 38. 4

CENTRA L 36. 4 0. 0 0. 0 38. 4 NO .

NO .

NO . CNTR

L 35. 5 0. 0 23. 9 59. 4

CNTR L 35. 5 0. 0 23. 9 59. 4

CNTR L 58. 3 0. 0 0. 0 56. 3 HES T

63. 6 16. 1 0. 0 79. 7

HES T 80. 4 0. 0 0. 0

. 80. 4

HES T 80. 4 0. 0 0. 0 80. 4 N

O

N O

N O . HES T 73. 5 0. 0 0. 0 73. 5

. HES T 73. 5 0. 0 0. 0 73. 5

. HES T 73. 5 0. 0 0. 0 73. 5 U S TOTA

L 811. 4 236. 8 23. 9 1072. 1

U S TOTA L 1028. 7 21. 1 23. 9 1073. 7

U S TOTA L 1072. 6 0. 0 0. 0 1072. 6