p. 1



# OAR Box

# 1828 Prepped byOllie Stewart



# Document

Number: 

# 282 ) ll-K
- 

# (I ) -9 5

Docket Number: 

# A-83-2 7

Printed 11/12/200811:12:58AM Sheet 282 of 325•f

199 0 PROJECTE DNE

W IHDUSTRIALFOSSI LFUEL-FIRE OBOILE R AI REMISSIONS , FUE LOEMAHD , ANDCOST S

NOTE S ON

IFCA M PROJECTION S (HIGHEROI LAN

D6A S PRICES )

PREPARE DFOR :
TH EU.S . ENVIRONMENTALPROTECTION AGENC Y

PREPARE DBY : ENERGYANDENVIRONMENTALANALYSIS , IHC . 165 5 HORT HFOR T MYERDRIVE ARLIHGTOH , VIRGINI A 2220 9 11/06/8 4 I 7C

U 3 

### > 

# C O I 

# r o

i T Jat' HOTE S O N IFCA M PROJECTIONS v * «*****••****••"*•«•*•*»•« *

1 . SUMMAR

YO F SEVE N SELECTE

D( A SUBSET O

F THE ) FIFT

HROUH D S0 2 HSP S IFCA

M RUNS
2 . BAS E CAS E

- S02 : CURREN

T NSP S

- PM : PROPOSE

DHSP S (4 9 F

R25103 )

- NOX : LE

A O RSC A REQUIRE

D( > 10 0 MMBTU/HR )
3 . OPTIO

N CAS E 1

- COMPLIANC

E FUEL S (100-25 0 MMBTU/HR) : 1.6 XS RESIDAN

D 1. 7 L BS02/MMBT

UCOA L

- COMPLIANCE FUEL S ( >25 0 MMBTU/HR) : 0.8 XS RESI DAN

D 1. 2 L BS02/MMBT

UCOA L

- NON-COMPLIANCE FUELS : MIN 50 XS0 2 REDUCTIO

N HITH 0. 9 L BS02/MMBT

UCEILIN

G
4 . OPTIO

N CAS E 2

- COMPLIANCE FUELS : 0.8 XS RESI DAN

D1. 2 L BS02/MMBT

U

- NON-COMPLIANCE FUELS : SAM E AS OX . 1
5 . OPTIO

N CAS E 3

- COMPLIANCE FUELS : 0.8 XS RESI D

- NON-COMPLIAHCE FUELS : SAM E AS O.C . 1
6 . OPTIO

N CAS E 4

- COMPLIANC

E FUELS : 0.3

XS RESI D

- NON-COMPLIANCE FUELS : 0. 6 L BS02/MMBT

UCEILIN

G
7 . OPTIO

N CAS E 5

- COMPLIANCE FUELS : 0.3 XS RESI D

- NON-COMPLIAHCE FUELS : CURREHT ELECTRI CUTILIT YNSP S 8 . OPTIO

N CAS E 6

- N OCOMPLIANC

E RESI DO

RCOA LTYPE S

- NON-COMPLIAHCE FUELS : 90XS0 2 REDUCTIO N

C OINDUSTRIA LBOILE RNE M SOURCE PERFORMANC

E STANDARDS ASSUMPTIOHS OPTIO HCAS E 1 (AR013 8 >

NATURA LGAS S0 2 CEILIN

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

G(LB/MMBTU )
DISTILLATE FUELOI L S0 2 CEILIN

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

G(LB/MMBTU )
RESIDUA LFUE LOI 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 BOILE RSIZE CATEGOR

Y(MMBTU/H

RHEA T INPUT )
30-5 0 50-7 5 75-10 0 100-15 0 150-20 0 200-25 0 >25 0

NON E NOH E HOH E

HOH E HOH E HOH E

HOH E HOH E HON E

NON E NON E NOH E HOH E HOH

E HON E NON E

NOH E HON E NON E

NOH E HON E NON E

NOH E HON E NON E NOH E NON

E NOH E HOH E

HOH E HOH E HOH E

HOH E HOH E NON E

NOH 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 NOH

E HOH E 0.2 0

HON E NON E 0.2 0

0.9 0 NOH E 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 NON

E NOH E 0.2 0

HOH E HOH E 0.2 0

0.9 0 NON E 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 NOHE

HOHE 0.2 0

HON E HOHE 0.2 0

0.9 0 HOHE 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 HOHE

HON E 0.3 0

NOHE 0.1 0 0.3 0

0.9 0 0.1 0 0.3 1

0.9 0 0.0 5 0.0 5 0.7 0

MANDATOR

YSCRUBBIN

GREGULATIONS
RESIDUA LFUE LOI L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

LREQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO USULFU REXEMPTIO

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

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

LREQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO USULFU REXEMPTIO

N (L BS02/MMBTU ) HOH E HOH E HOH E HOH E

HOH E HOH E HOH E HOH E HON

E NON E NON E NOH E

HOH E HOH E HOH E NON E NOH

E NON E NOH E NON E

NON E NON E NON E HOH E NON

E NON E NON E NON E

NON E NON E NON E NON E NOHE 50.0 0 HOHE 1.7 5

NOHE 50.0 0 HOHE 1.7 0 NON

E 50.0 0 NOHE 1.7 5

NON E 50.0 0 NOH E 1.7 0 NON

E 50.0 0 NON E 1.7 5

NON E 50.0 0 NOHE 1.7 0 HON

E 50.0 0 NON E 0.8 5

NON E 50.0 0 NON E 1.2 0INDUSTRIA LBOILE RNE M SOURC E PERFORMAHC

E STANDARDS ASSUMPTIONS OPTIO N CAS E 2 (AR013 2 )

NATURA LGAS S0 2 CEILIN

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

G(LB/MMBTU )
DISTILLATE FUELOI L S0 2 CEILIN

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

G(LB/MMBTU )
RESIDUA LFUE LOI L S0 2 CEILIN

G(LB/MMBTU ) P M CEILIH G(LB/MMBTU ) HO XCEILIH

G(LB/MMBTU )
COA L S0 2 CEILIH

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

- FO R<30 XC

U NO XCEILIN

G(LB/MMBTU ) 10-3 0 BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT )
30-5 0 50-7 5 75-10 0 100-15 0 150-20 0 200-25 0 >25 0

NON E NON E NOH E

NON E NON E HOH E

HOH E HOH E HOH E

NON E NOH E HOH E NON E NON

E NON E NON E

NON E NON E NON E

NON E HON E NOH E

HON E NON E NON E NON E HOH

E HOH E HOH E

HOH E HOH E NOH E

HOH E HOH E NOH E

HOH E HOH 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 NOH E 0.2 0

HON E NON E 0.2 0

0.9 0 NOH E 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 NON

E NOHE 0.2 0

HOHE HON E 0.2 0

0.9 0 NOHE 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 HOH

E NON E 0.2 0

NON E NON E 0.2 0

0.9 0 NOH E 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 HOHE

HOHE 0.3 0

NON E 0.1 0 0.3 0

0.9 0 0.1 0 0.3 1

0.9 0 0.0 5 0.0 5 0.7 0

MANDATOR

YSCRUBBIN

GREGULATIONS
RESIDUA LFUE LOI L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

LREQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO USULFU REXEMPTIO

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

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

LREQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO USULFU REXEMPTIO

N (L BS02/MMBTU ) HOH E HOH E HON E HOH E

NON E NOH E HON E HOH E HON

E HON E NON E NON E

NON E NON E NON E NON E HOH

E HOHE HOH E HOH E

HOH E HON E HON E NON E NON

E NON E NON E NON E

NON E NON E NON E NON E NOH

E 50.0 0 HOH E 0.8 5

HOH E 50.0 0 HON E 1.2 0 NON

E 50.0 0 NON E 0.8 5

NON E 50.0 0 NOH E 1.2 0 NON

E 50.0 0 NON E 0.8 5

NON E 50.0 0 NOH E 1.2 0 HOHE

50.0 0 NOHE 0.8 5

HON E 50.0 0 HOHE 1.2 0IHDUSTRIA LBOILE RHE M SOURCE PERFORMAHC

E STANDARDS ASSUMPTIONS OPTIO N CAS E 3 (AR013 3 )

NATURA LGAS S0 2 CEILIN

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

G(LB/MMBTU )
DISTILLATE FUELOI L S0 2 CEILIN

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

G(LB/MMBTU )
RESIDUA LFUELOI 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 CEILIH G(LB/MMBTU )

- FO R<30 XC

U HO XCEILIH

G(LB/MMBTU ) 10-3 0 BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT )
30-5 0 50-7 5 75-10 0 100-15 0 150-20 0 200-25 0 >25 0

NONE NON E HONE

NOHE NON E NONE

NON E NOHE HOHE

NON E NON E NON E NOHE NONE

NONE HOHE

HONE HON E HONE

NOHE HONE NONE

NONE NON E NONE HONE NONE

NOHE NONE

HOHE HOHE HOHE

HONE HOHE NONE

NONE NON E NON E HOHE NONE

NON E NONE

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E HOHE HONE

NONE 0.2 0

NOH E HOHE 0.2 0

0.9 0 HOH E 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 HOH E

HONE 0.2 0

NONE NONE 0.2 0

0.9 0 NONE 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 NOH E

HONE 0.2 0

NONE HOHE 0.2 0

0.9 0 NON E 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 NONE

NONE 0.3 0

NOH E 0.1 0 0.3 0

0.9 0 0.1 0 0.3 1

0.9 0 0.0 5 0.0 5 0.7 0

MANDATOR

YSCRUBBIH

GREGULATIONS l RESIDUA LFUE LOI L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

LREQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO HSULFU REXEMPTIO

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

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

LREQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO USULFU REXEMPTIO

N (L BS02/MMBTU ) NON E NON E NON E HOHE

HOHE HOHE NONE NON E NONE NOHE HOHE NOHE

HOHE HONE NON E HOHE HOHE

NONE NON E NONE

NONE NON E NOHE NOHE NOHE

NON E NON E NON E

NONE NON E NOHE NONE HOH E

50.0 0 NONE 0.8 5

NONE 50.0 0 NONE NONE NONE

50.0 0 NONE 0.8 5

NONE 50.0 0 NOH E HONE NONE

50.0 0 NONE 0.8 5

NON E 50.0 0 NON E NON E NONE 50.0 0 HON E 0.8 5

NOH E 50.0 0 HOH E NON EINDUSTRIA LBOILE R NE M SOURC E PERFORMAHC E STAHDARD S ASSUMPTION S OPTIO N CAS E 4 (AR014 4) tr.

NATURA LGA S S0 2 CEILIN G (LB/MMBTU ) P M CEILIN G (LB/MMBTU ) NOXCEILIN G (LB/MMBTU )

DISTILLAT E FUE LOI L S0 2 CEILIN G (LB/MMBTU ) P M CEILIN G (LB/MMBTU ) NOXCEILIN G (LB/MMBTU )

RESIDUA LFUE LOI 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 HO XCEILIH G (LB/MMBTU ) 10-3 0 BOILE R SIZ E CATEGOR Y(MMBTU/H R HEA TIHPUT )
30-5 0 50-7 5 75-10 0 100-15 0 150-20 0 200-25 0 >25 0

HON E NON E NON E

NON E NON E 

### Hon e

HOH E HOH E HOH E

HOH E NON E NON E HOH E HON E

NOH E HOH E

HON E NON E NOH E

HON E HOH E NOH E

NON E NOH E HON E HOH E HON E

NOH E HON E

HON E NON E NOH E

HOH E HOH E NOH E

HOH E HON E HOH E HOH E HOH E

HOH E NON E

NOH E HOH E HOH E

HOH E NON E NON E

NON E NON E NON E HON E NOH E

HON E 0.2 0

NON E NON E 0.2 0

0.6 0 NON E 0.3 1

0.6 0 0.0 5 0.2 0 0.6 0 NON E

NOH E 0.2 0

HOH E HOH E 0.2 0

0.6 0 HOH E 0.3 1

0.6 0 0.0 5 0.2 0 0.6 0 NOH E

NOH E 0.2 0

NOH E NON E 0.2 0

0.6 0 NON E 0.3 1

0.6 0 0.0 5 0.2 0 0.6 0 NON E

NOH E 0.3 0

HON E 0.1 0 0.3 0

0.6 0 0.1 0 0.3 1

0.6 0 0.0 5 0.0 5 0.7 0

MANDATOR

YSCRUBBIN G REGULATION S
RESIDUA L FUE L OI L S0 2 FLOOR (LB/MMBTU ) PERCEN

TS0 2 REMOVA

L REQUIRE D MINIMU M PERCEN

TS0 2 REMOVA

L REQUIRE D LOH SULFU R EXEMPTIO N (L B S02/MMBTU )

COA L S0 2 FLOOR (LB/MMBTU ) PERCEN

TS0 2 REMOVA

L REQUIRE D MINIMU M PERCENTS0 2 REMOVA L REQUIRE D LOH SULFU R EXEMPTIO N (L B S02/MMBTU ) NOH E HON E NON E NON E

NON E NON E HON E NON E NOH E

HOH E NON E NOH E

NON E NOH E HON E HON E NON E

NOH E HOH E HOH E

NON E NON E NON E NON E NON E

NOH E HOH E NON E

NON E NON E NON E NON E NOH E

HON E NOH E HOH E

HOH E HOH E HOH E NON E NOH E

HOH E HON E NON E

NON E NON E NOH E HOH E NON E

NOH E HOH E HON E

NON E NON E NON E NON E NON E

HON E NON E NON E

NOH E NON E NOH E NON EINDUSTRIA LBOILE RNE USOURCE PERFORMANC E STANDARDS ASSUMPTIONS OPTIO N CAS E 5 (AR013 4 )

NATURA LGAS S0 2 CEILIN

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

G(LB/MMBTU )
DISTILLATE FUELOI L S0 2 CEILIN

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

G(LB/MMBTU )
RESIDUA LFUE LOI 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 CEILIH G(LB/MMBTU )

- FO R<30 XC

U HO XCEILIH

G(LB/MMBTU ) 10-3 0 BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT )
30-5 0 50-7 5 75-10 0 100-15 0 150-20 0 200-25 0 >25 0

NOH E NON E NOH E

HOH E HOH E NON E

NON E NON E NON E

NOH E HOH E NON E NOH E HON

E NON E NON E

HOH E HON E NON E

NON E NON E NON E

NOH E HOH E HON E NON E NON

E NON E NON E

NOH E HOH E HOH E

HOH E HOH E HOH E

HOH E HON E HOH E HOH E HOH

E HOH E HOH E

NON E NOH E HOH E

HOH E HON E NOH E

HOH E NON E NOH E HOH E HON

E NON E 0.2 0

NOHE HON E 0.2 0

1.2 0 NON E 0.3 1

1.2 0 0.0 5 0.2 0 0.6 0 NOH

E HON E 0.2 0

NON E NON E 0.2 0

1.2 0 HON E 0.3 1

1.2 0 0.0 5 0.2 0 0.6 0 NOH

E NON E 0.2 0

NON E NON E 0.2 0

1.2 0 NON E 0.3 1

1.2 0 0.0 5 0.2 0 0.6 0 NOHE

HOHE 0.3 0

HOHE 0.1 0 0.3 0

1.2 0 0.1 0 0.3 1

1.2 0 0.0 5 0.0 5 0.7 0

MANDATOR

YSCRUBBIN

GREGULATIONS ) RESIDUA LFUELOI L S0 2 FLOO

R(LB/MMBTU ) PERCEN T 50 2 REMOVA

LREQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO USULFU REXEMPTIO

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

R(LB/MMBTU ) PERCEN T SO CREMOVA

LREQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO HSULFU REXEMPTIO

N (L BS02/MMBTU ) NOH E HON E NOH E HON E

NON E NON E NON E NON E HON

E NON E HON E NON E

HON E NON E NON E NON E NON

E NON E NON E NON E

NOH E HON E HOH E NON E NOH

E NON E NON E NOHE

NON E NOH E NON E NON E 0.6 0 90.0 0 70.0 0 0.3 5

0.6 0 90.0 0 70.0 0 NON E 0.6 0 90.0 0 70.0 0 0.3 5

0.6 0 90.0 0 70.0 0 NON E 0.6 0 90.0 0 70.0 0 0.3 5

0.6 0 90.0 0 70.0 0 NON E 0.6 0 90.0 0 70.0 0 0.3 5

0.6 0 90.0 0 70.0 0 NON EINDUSTRIA LBOILE RNE M SOURCE PERFORMANC

E STANDARDS ASSUMPTIONS OPTIO N CAS E 6 (AR013 7 )

NATURA LGAS S0 2 CEILIN

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

G(LB/MMBTU )
DISTILLATE FUE

LOI L S0 2 CEILIN

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

G(LB/MMBTU )
RESIDUA LFUE LOI 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 BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT )
30-5 0 50-7 5 75-10 0 100-15 0 150-20 0 200-25 0 >25 0

NON E NON E NON E

NON E NON E NOH E

HON E NON E NOH E

HOH E NON E NON E NON E NON

E NOH E NON E

NOH E HOH E HOHE

NON E NON E NON E

NOH E HOH E HOHE HON E NOH

E HOH E HOH E

NOH E HOH E HOH E

HOH E HOH E NOH E

HON E NON E NOH E NON E NOH

E HON E NON E

NOHE HON E HOHE

HON E HON E NON E

NON E NON E NOH E HOH E NON

E NON E 0.2 0

NOH E NON E 0.2 0

0.6 0 NON E 0.3 1

0.6 0 0.0 5 0.2 0 0.6 0 NOH

E HON E 0.2 0

HON E NON E 0.2 0

0.6 0 NON E 0.3 1

0.6 0 0.0 5 0.2 0 0.6 0 NON

E NOHE 0.2 0

NON E NOH E 0.2 0

0.6 0 HOHE 0.3 1

0.6 0 0.0 5 0.2 0 0.6 0 HOHE

HON E 0.3 0

HON E 0.1 0 0.3 0

0.6 0 0.1 0 0.3 1

0.6 0 0.0 5 0.0 5 0.7 0

MANDATOR

YSCRUBBIN

GREGULATIONS
RESIDUA LFUE LOI L S0 2 FLOO

R(LB/MMBTU ) PERCEH T S0 2 REMOVA

LREQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO USULFU REXEMPTIO

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

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

LREQUIRE

D MINIMU M PERCEHT S0 2 REMOVA LREQUIRE

D LO USULFU REXEMPTIO

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

NON E NON E NON E NON E NOH

E HON E HON E HOHE

HOH E HON E NOHE HOH E NON

E NOH E HOH E HOH E

NON E NOH E HOH E NON E NON

E NON E NON E NON E

NON E NON E NON E NON E NON

E 90.0 0 HOH E 0.3 5

NON E 90.0 0 NOHE NON E NOH

E 90.0 0 HOHE 0.3 5

HON E 90.0 0 NOHE NOHE HOHE

90.0 0 HOH E 0.3 5

HOH E 90.0 0 HON E NON E NON

E 90.0 0 NON E 0.3 5

NON E 90.0 0 NON E HON ELIS T O F TABLE S

DESCRIPTIO

N O F TABL E TABLE HUMBE R

FUE LDEMAN D

- NUMBE RO F UNIT S 1

- BTUS O

F FUE LCONSUMPTIO

N 2
POLLUTAN

T EMISSIONS 3
COST S 4
NO XONL Y

- CONTRO

LCOST S 5

- EMISSIONS 6 NATIONA LIMPACT S B

YSIZ E (MMBTU/HR )

- 10-5 0 7

- 50-7 5 8

- 75-10 0 9

- 100-15 0 1 0

- 150-20 0 11

- 200-25 0 1 2

- > 25 0 1 3

- > 10 0 1 4

- 100-25 0 1 5

- > 5 0 1 6

- TOTA L1 7

REGIONA LIMPACT S

- S0 2 EMISSIONS 100-15 0 MMBTU/H

R1 8 150-20 0 MMBTU/H

R1 9 200-25 0 MMBTU/H

R2 0 > 25 0 MMBTU/H

R2 1

- FOSSI LFUE

LDEMAN D 100-15 0 MMBTU/H

R2 2 150-20 0 MMBTU/H

R2 3 200-25 0 MMBTU/H

R2 4 > 25 0 MMBTU/H

R2 5

- ANNUALIZE

DCOST S 100-15 0 MMBTU/H

R2 6 150-20 0 MMBTU/H

R2 7 200-25 0 MMBTU/H

R2 8 > 25 0 MMBTU/H

R2 9TABL E 1 — 199 0 FUE

LDEMAN D (HUMBE RO F UHITS )

10-5 0 BOILE RSIZ E(MMBTU/HR ) 50-10 0100-15 0150-20 0200-25 0 > 25 0 TOTA L
"TOTAL * TH E BAS E OPTIO H OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
NATURA LGAS TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
COA L TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N CAS E CAS E CAS E CAS E CAS E CAS E CAS E 1 2 3 4 5 6
AN DOI L CAS E CAS E 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 3 4 5 6

1 2 3 4 5 6 141 2 141 2 141 2 141 2 141 2 141 2 141 2

125 1 125 1 125 1 125 1 125 1 125 1 125 1

16 1 16 1 16 1 16 1 16 1 16 1 16 1 577
.

577
. 577
. 577
. 577
. 577
. 577
.

398

. 398

. 398

. 398

. 398

. 398

. 398

.

179
. 179
. 179
. 179
. 179
. 179
. 179
. 271
.

271
. 271
. 271
. 271
. 271
. 271
.

212
. 217
. 239
. 254
. 254
. 254
. 254
.

5 9
. 5 4
. 3 2
. 17
. 1 7
. 1 7
. 1 7
. 135
.

135
. 135
. 135
. 135
. 135
. 135
.

5 5
. 7 1
. 7 1
. 115
. 115
. 115
. 120
.

80

. 64

. 64

. 20

. 20

. 20

. 15

. 6 2

.

6 2

. 6 2

. 6 2

. 6 2

. 6 2

. 6 2

.

2 1

. 26

. 26

. 49

. 49

. 49

. 49

.

4 1
. 3 6
. 3 6
. 1 3
. 1 3
. 1 3
. 1 3
. 136 .

136 . 136 . 136 . 136 . 136 . 136 .

70 . 70 . 70 . 86 . 86 . 86 . 86 .

66 . 66 . 66 . 50 . 50 . 50 . 50 . 2593 .

2593 . 2593 . 2593 . 2593 . 2593 . 2593 .

2007 . 2033 . 2055 . 2153 . 2153 . 2153 . 2158 .

586 . 560 . 538 . 440 . 440 . 440 . 435 .TABLE 2 — 199 0 FUE

LDEMAN D (10**1 2 BTUS )

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 OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
NATURA L GAS TH E BAS E OPTIO N OPTIO N OPTIO N 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 CAS E OPTIO N CAS E 1 2 3 4 5 6

1 2 3 4 5 6
RESIDUA L FUE L OI L TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO H OPTIO N
COA L TH E BAS E OPTIO H OPTIO H OPTIO H OPTIO N 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 CAS E CAS E 1 2 3 4 5 6

1 2 3 4 5 6 132 .

132 . 132 . 132 . 132 . 132 . 132 .

86 . 86 . 86 . 86 . 66 . 86 . 86 .

9 . 9 . 9 . 9 . 9 . 9 . 9 .

36 . 36 . 36 . 36 . 36 . 36 . 36 . 136 .

136 . 136 . 136 . 136 . 136 . 136 .

59 . 59 . 59 . 59 . 59 . 59 . 59 .

6 . 6 . 6 . 6 . 6 . 6 . 6 .

72 . 72 . 72 . 72 . 72 . 72 . 72 . 129 . 1

129 . 1 129 . 1 129 . 1 129 . ] 129 . 1 129 . I

82 . . 92 . 105 . 117 . 117 . 117 . 117 .

7 . 0 . 0 . 0 . 0 . 0 . 0 .

40 . 37 . 23 . 12 . 12 . 12 . 12 . 41 .

56 . 56 . 88 . 88 . 88 . 94 .

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

70 . 55 . 55 . 23 . 23 . 23 . 17 . 67 .

67 . 67 . 67 . 67 . 67 . 67 .

19 . 24 . 24 . 50 . 50 . 50 . 50 .

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

48 . 43 . 43 . 17 . 17 . 17 . 17 . 191 .

191 . 191 . 191 . 191 . 191 . 191 .

65 . 65 . 65 . 90 . 90 . 90 . 90 .

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

126 . 126 . 126 . 101 . 101 . 101 . 101 . 76 6

76 6 76 6 76 6 76 6 76 6 76 6

35 2 38 2 39 6 49 0 49 0 49 0 49 6

2 2 1 5 1 5 1 5 1 5 1 5 1 5

39 2 36 9 35 6 26 1 26 1 26 1 25 5TABL E 3 — 199 0 EMISSION 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 S0 2 TH E BAS E OPTION OPTION OPTION OPTION OPTIO H OPTION

> M TH E BAS E OPTIO N OPTION OPTION OPTION OPTION OPTIO N
IO X TH E BAS E OPTION OPTION OPTION OPTION OPTION OPTION
>M1 0 TH E BAS E OPTION OPTION OPTION OPTION OPTION CAS E

CAS E CAS E CAS E CAS E CAS E CAS E

CAS E CAS E CAS E CAS E CAS E CAS E CAS E

CAS E CAS E CAS E CAS E CAS E CAS E CAS E

CAS E CAS E CAS E CAS E CAS E CAS E OPTION CAS E 1 2 3 4 5 6

1 2 3 4 5 6

1 2 3 4 5 6

1 2 3 4 5 6 68 .

68 . 68 . 68 . 68 . 68 . 68 .

11 . 11 . 11 . 11 . 11 . 11 . 11 .

13 . 13 . 13 . 13 . 13 . 13 . 13 .

8 . 8 . 8 . 8 . 8 . 8 . 6 . 121 .

121 . 121 . 121 . 121 . 121 . 121 .

19 , 19 . 19 . 19 . 19 . 19 . 19 .

23 . 23 . 23 . 23 . 23 . 23 . 23 .

14 . 14 . 14 . 14 . 14 . 14 . 14 . 74 .

24 . 11 . 4 . 3 . 3 . 2 .

2 .

17 . 16 . 14 . 12 . 12 . 12 . 12 .

2 . 108 .

37 . 25 . 7 . 5 . 5 . 2 .

23 . 20 . 20 . 15 . 15 . 15 . 14 . 86 .

29 . 20 . 5 . 4 . 3 . 2 .

15 . 14 . 14 . 9 . 9 . 9 . 9 . 59 .

58 . 58 . 30 . 22 . 19 . 10 .

2 . 2 . 2 . 2 . 2 . 2 . 2 .

43 . 43 . 43 . 37 . 37 . 37 . 37 .

2 . 2 . 2 . 2 . 2 . 2 . 2 . 51 5

33 7 30 4 23 5 22 3 21 9 20 5

3 6 3 5 3 5 3 4 3 4 3 4 3 4

13 4 12 9 12 7 10 9 10 9 10 9 10 8

2 8 2 7 2 7 2 6 2 6 2 6 2 6IUALIZE DCOST S TH E BAS E CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E
'ITA LCOST S TH E BAS E CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E - 1CVI 3 4 5 6



### - 1 2 3 4 5 6 10-5 0
TOTA L 1322. 7 1322. 7 1322. 7 1322. 7 1322. 7 1322. 7 1322. 7
TOTA L 1584. 9 1584. 9 1584. 9 1564. 9 1584. 9 1584. 9 1584. 9 TABLE 4 ~ 199 0 COST S

(10**6 , $1982 )
BOILE RSIZE 50-10 0

1159. 6 1159. 6 1159. 6 1159. 6 1159. 6 1159. 6 1159. 6

1881. 4 1881. 4 1881. 4 1881. 4 1881. 4 1881. 4 1881. 4 100-15 0

1008. 0 1013. 0 1008. 7 1010. 6 1010. 8 1010. 9 1011. 2

1294. 3 . 1231. 4 1021. 1 684. 2 883. 9 884. 3 884. 3 (MMBTU/HR )

150-20 0

837. 6 836. 1 843. 7 832. 1 832. 6 832. 7 829. 4

1521. 2 1296. 6 1300. 4 777. 6 777. 8 777. 8 696. 9 200-25 0

493. 1 499. 7 504. 4 500. 4 500. 8 500. 9 501. 1

919. 9 844. 5 838. 8 495. 2 495. 3 495. 3 495. 4 > 25 0

1386. 3 1386. 5 1386. 5 1411. 1 1412. 4 1413. 6 1415. 0

2189. 4 2189. 5 2189. 5 1920. 2 1908. 6 1920. 8 1909. 2 TOTA

L

6207. 3 6217. 7 6225. 6 6236. 6 6238. 9 6240. 4 6239. 0

9391. 2 9028. 2 8816. 1 7543. 5 7531. 8 7544. 5 7452. 1TABL E 5 — 199 0 NO

XCONTRO

L ANNUALIZE

DCOST S (10**6 , $1982 )

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 OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
NATURA LGAS TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
COA L TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N CAS E CAS E CAS E CAS E CAS E CAS E CAS E 1 2 3 4 5 6
AN DOI L CAS E CAS E 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 3 4 5 6

1 2 3 4 5 6 -4. 1

-4. 1 -4. 1 -4. 1 -4. 1 -4. 1 -4. 1

-4. 0 -4. 0 -4. 0 -4. 0 -4. 0 -4. 0 -4. 0

-0. 1 -0. 1 -0. 1 -0. 1 -0. 1 -0. 1 -0. 1 -4. 9

-4. 9 -4. 9 -4. 9 -4. 9 -4. 9 -4. 9

-4. 2 -4. 2 -4. 2 -4. 2 -4. 2 -4. 2 -4. 2

-0. 6 -0. 6 -0. 6 -0. 6 -0. 6 -0. 6 -0. 6 -1. 4

-3. 5 -3. 8 -4. 1 -4. 1 -4. 1 -4. 1

2. 7 2. 4 1. 3 0. 6 0. 6 0. 6 0. 6 3. 6

1. 8 1. 8 -1. 0 -1. 0 -1. 0 -1. 7

-1. 1 -1. 8 -1. 8 -2. 7 -2. 7 -2. 7 -3. 0

4. 7 3. 6 3. 6 1. 8 1. 8 1. 8 1. 3 0. 4

0. 4 0. 4 5. 6 5. 6 5. 6 5. 6

2. 4 3. 0 3. 0 6. 6 6. 6 6. 6 6. 6

2. 9 2. 6 2. 6 1. 0 1. 0 1. 0 1. 0 -1. 9

-1. 9 -1. 9 -7. 7 -7. 7 -7. 7 -7. 7

-9. 6 -9. 6 -9. 6 -13. 7 -13. 7 -13. 7 -13. 7

7. 7 7. 7 7. 7 6. 0 6. 0 6. 0 6. 0 -5. 5

-10. 5 -11. 9 -26. 7 -26. 7 -26. 7 -27. 4

-22. 8 -26. 2 -26. 4 -35. 4 -35. 4 -35. 4 -35. 6

17. 4 15. 7 14. 6 8. 7 8. 7 8. 7 8. 3TABLE 6 — 199 0 NO

XEMISSIONS (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 OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
NATURA L GAS TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
COA L TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N CAS E CAS E CAS E CAS E CAS E CAS E CAS E 1 2 3 4 5 6
AN DOI L CAS E CAS E 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 3 4 5 6

1 2 3 4 5 6 13. 4

13. 4 13. 4 13. 4 13. 4 13. 4 13. 4

7. 6 7. 6 7. 6 7. 6 7. 6 7. 6 7. 6

5. 8 5. 8 5. 8 5. 8 5. 8 5. 8 5. 8 22. 6

22. 6 22. 6 22. 6 22. 6 22. 6 22. 6

4. 7 4. 7 4. 7 4. 7 4. 7 4. 7 4. 7

17. 9 17. 9 17. 9 17. 9 17. 9 17. 9 17. 9 17. 1

16. 0 13. 5 U. 5 U. 5 U. 5 U. 5

6. 7 6. 4 7. 4 8. 6 8. 6 8. 6 8. 6

10. 4 9. 6 6. 1 2. 9 2. 9 2. 9 2. 9 23. 0

20. 2 20. 1 14. 8 14. 8 14. 8 13. 7

3. 9 5. 3 5. 3 8. 4 8. 4 8. 4 8. 9

19. 1 14. 9 14. 8 6. 4 6. 4 6. 4 4. 8 15. 0

14. 2 14. 2 9. 4 9. 4 9. 4 9. 4

1. 9 2. 3 2. 3 4. 8 4. 8 4. 8 4. 8

13. 1 11. 9 11. 9 4. 6 4. 6 4. 6 4. 6 42. 6

42. 6 42. 6 36. 9 36. 9 36. 9 36. 9

6. 2 6. 2 6. 2 8. 6 8. 6 6. 6 6. 6

36. 4 36. 4 36. 4 28. 3 28. 3 28. 3 28. 3 133. 7

129. 2 126. 6 108. 6 108. 6 108. 6 107. 5

30. 9 32. 7 33. 6 42. 6 42. 6 42. 6 43. 1

102. 8 96. 5 93. 0 66. 0 66. 0 66. 0 64. 4TABL E 7 « IHDUSTRIA

LBOILE RHSP S HATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

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

FUE LDEMAN D (HUMBE RO F UHITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUE LDEMAN D (10"«1 2 BTUS ) NATURA LGAS DISTILLATE FUE

LOI L RESIDUA LFUE LOI L COA L "TOTAL "
EMISSIONS (10** 3 TOHS ) S0 2 P M HO X PMIO
EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M HO X PMIO * ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L "TOTAL " TH E BAS E CAS E

1251 . 161 . 1412 .

86 . 0 . 9 . 36 . 132 .

68. 4 10. 9 13. 4 8. 0

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

651. 3 U. 5 -4. 1 664. 0 1322. 7 OPTIO

N CAS E 1

1251 . 161 . 1412 .

86 . 0 . 9 . 36 . 132 .

68. 4 10. 9 13. 4 8. 0

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

651. 3 U. 5 -4. 1 664. 0 1322. 7 OPTIO

N CAS E 2

1251 . 161 . 1412 .

86 . 0 . 9 . 36 . 132 .

68. 4 10. 9 13. 4 8. 0

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

651. 3 U. 5 -4. 1 664. 0 1322. 7 OPTIO

N CAS E 3

1251 . 161 . 1412 .

66 . 0 . 9 . 36 . 132 .

68. 4 10. 9 13. 4 8. 0

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

651. 3 U. 5 -4. 1 664. 0 1322. 7 OPTIO

N CAS E 4

1251 . 161 . 1412 .

86 . 0 . 9 . 36 . 132 .

68. 4 10. 9 13. 4 8. 0

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

651. 3 U. 5 -4. 1 664. 0 1322. 7 OPTIO

N CAS E 5

1251 . 161 . 1412 .

86 . 0 . 9 . 36 . 132 .

68. 4 10. 9 13. 4 8. 0

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

651. 3 U. 5 -4. 1 664. 0 1322. 7 OPTIO

N CAS E 6

1251 . 161 . 1412 .

86 . 0 . 9 . 36 . 132 .

68. 4 10. 9 13. 4 8. 0

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

651. 3 U. 5 -4. 1 664. 0 1322. 7
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL " 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X "TOTAL " 1524 . 31 . 30 . 1585 . 1524 .

31 . 30 . 1585 . 1524 .

31 . 30 . 1585 . 1524 .

31 . 30 . 1585 . 1524 .

31 . 30 . 1585 . 1524 .

31 . 30 . 1585 . 1524 .

31 . 30 . 1585 .TABL E 8 — IHDUSTRIA

LBOILE RHSP S HATIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

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

FUE LDEMAH D (HUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUE LDEMAN D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUE

LOI L RESIDUA LFUE LOI L COA L "TOTAL "
EMISSIONS (10"" 3 TONS ) 80 2 P M NO X PMIO
EMISSIONS ( XCHANG

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

DCOST S (10**6 , $1982 ) BOILE R FG OAN DP M NO X FUE L "TOTAL " TH E BAS E CAS E

291 . U l . 402 .

38 . 0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

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

351. 5 13. 2 -2. 9 360. 1 721. 9 OPTIO

N CAS E 1

291 . 

### Ul . 402 .

38 . 0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

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

351. 5 13. 2 -2. 9 360. 1 721. 9 OPTIO

N CAS E 2

291 . U l . 402 .

38 . 0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

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

351. 5 13. 2 -2. 9 360. 1 721. 9 OPTIO

N CAS E 3

291 . U l . 402 .

38 . 0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

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

351. 5 13. 2 -2. 9 360. 1 721. 9 OPTIO

N CAS E 4

291 . U l . 402 .

38 . 0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

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

351. 5 13. 2 -2. 9 360. 1 721. 9 OPTIO

N CAS E 5

291 . U l . 402 .

38 . 0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

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

351. 5 13. 2 -2. 9 360. 1 721. 9 OPTIO

N CAS E 6

291 . U l . 402 .

38 . 0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

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

351. 5 13. 2 -2. 9 360. 1 721. 9
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL " 

### 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X "TOTAL " 1084 . 34 . 10 . 1127 . 1084 .

34 . 10 . 1127 . 1084 .

34 . 10 . 1127 . 1084 .

34 . 10 . 1127 . 1084 .

34 . 10 . 1127 . 1084 .

34 . 10 . 1127 . 1084 .

34 . 10 . 1127 .TABLE 9 ~

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

FUELDEMAN

D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUE LDEMAN D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUE

LOI L RESIOUA LFUE LOI L COA L "TOTAL "
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M HO X PMIO
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L "TOTAL "
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL "
CAPITA LCOST S (10**6 , $1982 ) BOILE R ! FG DAN DP M NO X "TOTAL "

- . INDUSTRIA LBOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE ,

TH E BAS E CAS E

107 . 68 . 175 .

20 . 0 . 2 . 31 . 54 .

54. 6 8. 6 9. 4 6. 3

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

213. 8 9. 0 -1. 9 216. 8 437. 7

0. 0

725 . 24 . 5 . 754 . OPTIO

N CAS E 1

107 . 68 . 175 .

20 . 0 . 2 . 31 . 54 .

54. 6 8. 6 9. 4 6. 3

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

213. 8 9. 0 -1. 9 216. 8 437. 7

0. 0

725 . 24 . 5 . 754 . OPTIO

N CAS E 2

107 . 68 . 175 .

20 . 0 . 2 . 31 . 54 .

54. 6 8. 6 9. 4 6. 3

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

213. 8 9. 0 -1. 9 216. 8 437. 7

0. 0

725 . 24 . 5 . 754 . OPTIO

N CAS E 3

107 . 68 . 175 .

20 . 0 . 2 . 31 . 54 .

54. 6 8. 6 9. 4 6. 3

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

213. 8 9. 0 -1. 9 216. 8 437. 7

0. 0

725 . 24 . 5 . 754 . 1986-199 0

OPTIO N CAS E 4

107 . 68 . 175 .

20 . 0 . 2 . 31 . 54 .

54. 6 8. 6 9. 4 6. 3

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

213. 8 9. 0 -1. 9 216. 6 437. 7

0. 0

725 . 24 . 5 . 754 . OPTIO

N CAS E 5

107 . 68 . 175 .

20 . 0 . 2 . 31 . 54 .

54. 6 8. 6 9. 4 6. 3

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

213. 8 9. 0 -1. 9 216. 8 437. 7

0. 0

725 . 24 . 5 . 754 . -

OPTIO N CAS E 6

107 . 68 . 175 .

20 . 0 . 2 . 31 . 5* .

54. 6 8. 6 9. 4 6. 3

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

213. 8 9. 0 -1. 9 216. 8 437. 7

0. 0

725 . 24 . 5 . 754 .TABLE 1 0 ~ INDUSTRIA LBOILE RHSP S HATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

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

FUE LDEMAN D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUE LDEMAN D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUE

LOI L RESIDUA LFUE LOI L COA L "TOTAL "
EMISSIONS (10«» 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS ( XCHAHG

E S0 2 P M HO X PMIO
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L "TOTAL " FRO M BAS E CASE ) TH E BAS E CAS E

212 . 59 . 271 .

82 . 0 . 7 . 40 . 129 .

74. 0 1. 8 17. 1 1. 8

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

354. 5 22. 6 1. 3 629. 5 1008. 0 OPTIO

N CAS E 1

217 . 54 . 271 .

92 . 0 . 0 . 37 . 129 .

24. 2 1. 0 16. 0 1. 0

-67. 3 -44. 4 -6. 4 -44. 4

343. 1 20. 6 -1. 1 650. 3 1013. 0 OPTIO

N CAS E 2

239 . 32 . 271 .

105 . 0 . 0 . 23 . 129 .

11. 2 0. 9 13. 5 0. 9

-84. 9 -50. 0 -21. 1 -50. 0

301. 7 12. 6 -2. 5 696. 9 1008. 7 OPTIO

N CAS E 3

254 . 17 . 271 .

117 . 0 . 0 . 12 . 129 .

3. 8 0. 8 U. 5 0. 8

-94. 9 -55. 6 -32. 7 -55. 6

270. 9 14. 2 -3. 6 729. 0 1010. 6 OPTIO

N CAS E 4

254 . 17 . 271 .

117 . 0 . 0 . 12 . 129 .

2. 7 0. 8 U. 5 0. 8

-96. 4 -55. 6 -32. 7 -55. 6

270. 9 14. 1 -3. 6 729. 4 1010. 8 OPTIO

N CAS E 5

254 . 17 . 271 .

117 . 0 . 0 . 12 . 129 .

2. 5 0. 8 U . 5 0. 8

-96. 6 -55. 6 -32. 7 -55. 6

270. 9 14. 5 -3. 6 729. 0 1010. 9 OPTIO

N CAS E 6

254 . 17 . 271 .

117 . 0 . 0 . 12 . 129 .

1. 6 0. 8 U . 5 0. 8

-97. 8 -55. 6 -32. 7 -55. 6

270. 9 14. 7 -3. 6 729. 0 1011. 2
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL " 0. 0 0. 5 0. 1 0. 3 0. 3 0. 3 0. 3
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X "TOTAL " 1196 . 79 . 20 . 1294 . 1145 .

72 . 15 . 1231 . 964 .

43 . 15 . 1021 . 834 .

36 . 14 . 864 . 834 .

36 . 14 . 884 . 834 .

36 . 14 . 884 . 834 .

36 . 14 . 884 .TABL E 11 — IHDUSTRIA

LBOILE RHSP S HATIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

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

FUE LDEMAN D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUE LDEMAN D (10**1 2 BTUS ) HATURA LGAS DISTILLATE FUELOI L RESIDUA LFUE LOI L COA L "TOTAL "
EHISSIOHS (10*» 3 TOHS ) S0 2 P M HO X PMIO
EMISSIOMS ( XCHAHG

E FRO M BAS E CASE ) SO C P M NO X PMIO
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG OAN DP M NO X FUEL "TOTAL " TH E BAS E CAS E

55 . 80 . 135 .

41 . 0 . 0 . 70 . U l .

107. 8 1. 3 23. 0 1. 2

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

365. 9 40. 2 3. 6 427. 9 837. 6 OPTIO

N CAS E 1

71 . 64 . 135 .

56 . 0 . 0 . 55 . U l .

36. 9 1. 1 20. 2 1. 1

-65. 8 -15. 4 -12. 2 -8. 3

320. 2 31. 9 1. 8 482. 1 836. 1 OPTIO

N CAS E 2

71 . 64 . 135 .

56 . 0 . 0 . 55 . U l .

25. 2 1. 1 20. 1 1. 1

-76. 6 -15. 4 -12. 6 -8. 3

320. 2 33. 9 1. 8 487. 8 843. 7 OPTIO

N CAS E 3

115 . 20 . 135 .

88 . 0 . 0 . 23 . U l .

7. 1 0. 8 14. 8 0. 8

-93. 4 -38. 5 -35. 7 -33. 3

221. 4 23. 0 -1. 0 588. 7 832. 1 OPTIO

N CAS E 4

115 . 20 . 135 .

88 . 0 . 0 . 23 . U l .

5. 1 0. 8 14. 6 0. 8

-95. 3 -38. 5 -35. 7 -33. 3

221. 4 23. 5 -1. 0 588. 7 832. 6 OPTIO

N CAS E 5

115 . 20 . 135 .

88 . 0 . 0 . 23 . U l .

4. 7 0. 8 14. 8 0. 8

-95. 6 -38. 5 -35. 7 -33. 3

221. 4 23. 6 -1. 0 588. 7 832. 7 OPTIO

N CAS E 6

120 . 15 . 135 .

94 . 0 . 0 . 17 . U l .

2. 3 0. 7 13. 7 0. 7

-97. 9 -46. 2 -40. 4 -41. 7

204. 6 18. 8 -1. 7 607. 7 829. 4
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL " 0. 0 -0. 2 0. 7 -0. 7 -0. 6 -0. 6 -1. 0
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X "TOTAL " 1369 . 140 .CVI 1521 . 1173 .

112 . 12 . 1297 . 1173 .

116 . 12 . 1300 . 714 .

53 . 11 . 778 . 714 .

53 . 11 . 778 . 714 .

53 . 11 . 778 . 646 .

40 . 11 . 697 .TABL E 1 2 INDUSTRIA

LBOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

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

FUE LDEMAN D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUE LDEMAN D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUELOI L RESIDUA LFUE LOI L COA L "TOTAL "
EMISSIONS (10"» 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS ( XCHANG

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

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUEL "TOTAL " TH E BAS E CAS E

21 . 41 . 62 .

19 . 0 . 0 . 48 . 67 .

85. 5 0. 8 15. 0 0. 8

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

223. 7 26. 4 0. 4 242. 5 493. 1 OPTIO

N CAS E 1

26 . 36 . 62 .

24 . 0 . 0 . 43 . 67 .

28. 8 0. 8 14. 2 0. 8

-66. 3 0. 0 -5. 3 0. 0

210. 5 23. 8 -0. 4 265. 9 499. 7 OPTIO

N CAS E 2

26 . 36 . 62 .

24 . 0 . 0 . 43 . 67 .

20. 1 0. 8 14. 2 0. 8

-76. 5 0. 0 -5. 3 0. 0

209. 6 23. 5 -0. 4 271. 6 504. 4 OPTIO

N CAS E 3

49 . 13 . 62 .

50 . 0 . 0 . 17 . 67 .

5. 2 0. 5 9. 4 0. 5

-93. 9 -37. 5 -37. 3 -37. 5

141. 9 18. 5 -5. 6 345. 6 500. 4 OPTIO

N CAS E 4

49 . 13 . 62 .

50 . 0 . 0 . 17 . 67 .

3. 7 0. 5 9. 4 0. 5

-95. 7 -37. 5 -37. 3 -37. 5

141. 9 18. 8 -5. 6 345. 6 500. 8 OPTIO

N CAS E 5

49 . 13 . 62 .

50 . 0 . 0 . 17 . 67 .

3. 4 0. 5 9. 4 0. 5

-96. 0 -37. 5 -37. 3 -37. 5

141. 9 18. 9 -5. 6 345. 6 500. 9 OPTIO

N CAS E 6

49 . 13 . 62 .

50 . 0 . 0 . 17 . 67 .

2. 4 0. 5 9. 4 0. 5

-97. 2 -37. 5 -37. 3 -37. 5

141. 9 19. 2 -5. 6 345. 6 501. 1
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL " 0. 0 1. 3 2. 3 1. 5 1. 6 1. 6 1. 6
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X "TOTAL " 824 . 88 . 8 . 920 . 760 .

77 . 8 . 844 . 754 .

77 . 8 . 839 . 446 .

41 . 8 . 495 . 446 .

41 . 8 . 495 . 446 .

41 . 8 . 495 . 446 .

41 . 8 . 495 .TABLE 1 3 « IHDUSTRIA LBOILE RHSP S NATIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) > 25 0

FUE LOEMAH D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUELDEMAN

D (10**1 2 BTUS ) NATURA LGA S DISTILLATE FUE

LOI L RESIDUA LFUE LOI L COA L "TOTAL "
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS ( XCHAHG

E FRO M BAS E CASE ) S0 2 P M HO X PMIO
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG OAN DP M NO X FUEL "TOTAL " TH E BAS E CAS E

70 . 66 . 136 .

65 . 0 . 0 . 126 . 191 .

58. 6 2. 2 42. 6 2. 2

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

558. 2 63. 0 -1. 9 767. 1 1386. 3 OPTIO

N CAS E 1

70 . 66 . 136 .

65 . 0 . 0 . 126 . 191 .

57. 8 2. 2 42. 6 2. 2

-1. 4 0. 0 0. 0 0. 0

558. 2 63. 1 -1. 9 767. 1 1386. 5 OPTIO

N CAS E 2

70 . 66 . 136 .

65 . 0 . 0 . 126 . 191 .

57. 8 2. 2 42. 6 2. 2

-1. 4 0. 0 0. 0 0. 0

558. 2 63. 1 -1. 9 767. 1 1386. 5 OPTIO

N CAS E 3

86 . 50 . 136 .

90 . 0 . 0 . 101 . 191 .

29. 5 1. 9 36. 9 1. 9

-49. 7 -13. 6 -13. 4 -13. 6

496. 1 87. 4 -7. 7 835. 4 1411. 1 OPTIO

N CAS E 4

86 . 50 . 136 .

90 . 0 . 0 . 101 . 191 .

22. 2 1. 9 36. 9 1. 9

-62. 1 -13. 6 -13. 4 -13. 6

494. 1 87. 1 -7. 7 838. 9 1412. 4 OPTIO

N CAS E 5

86 . 50 . 136 .

90 . 0 . 0 . 101 . 191 .

19. 1 1. 9 36. 9 1. 9

-67. 4 -13. 6 -13. 4 -13. 6

496. 1 89. 9 -7. 7 835. 4 1413. 6 OPTIO

N CAS E 6

86 . 50 . 136 .

90 . 0 . 0 . 101 . 191 .

9. 7 1. 9 36. 9 1. 9

-83. 4 -13. 6 -13. 4 -13. 6

494. 1 69. 6 -7. 7 838. 9 1415. 0
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL " 0. 0 0. 0 0. 0 1. 8 1. 9 2. 0 2. 1
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X "TOTAL " 1981 . 168 . 20 . 2189 . 1981 .

188 . 20 . 2189 . 1981 .

188 . 20 . 2189 . 1695 .

205 . 20 . 1920 . 1684 .

205 . 20 . 1909 . 1695 .

206 . 20 . 1921 . 1684 .

206 . 20 . 1909 .TABLE 1 4 INDUSTRIA LBOILE RHSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) > 10 0

FUE LDEMAN D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUE LDEMAN D (10»»1 2 BTUS ) NATURA LGAS DISTILLATE FUE

LOI L RESIDUA LFUE LOI L COA L "TOTAL "
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS ( XCHANG

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

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L "TOTAL " TH E BAS E CAS E

358 . 246 . 604 .

207 . 0 . 7 . 284 . 498 .

325. 9 6. 1 97. 7 6. 0

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

1502. 4 152. 2 3. 4 2067. 0 3725. 1 OPTIO

N CAS E 1

384 . 220 . 604 .

237 . 0 . 0 . 261 . 498 .

147. 7 5. 1 93. 0 5. 1

-54. 7 -16. 4 -4. 8 -15. 0

1432. 0 139. 5 -1. 5 2165. 4 3735. 4 OPTIO

N CAS E 2

406 . 198 . 604 .

250 . 0 . 0 . 248 . 498 .

114. 3 5. 0 90. 4 5. 0

-64. 9 -18. 0 -7. 5 -16. 7

1389. 6 133. 2 -3. 0 2223. 4 3743. 3 OPTIO

N CAS E 3

504 . 100 . 604 .

345 . 0 . 0 . 153 . 498 .

45. 6 4. 0 72. 6 4. 0

-86. 0 -34. 4 -25. 7 -33. 3

1130. 3 143. 0 -17. 8 2498. 7 3754. 3 OPTIO

N CAS E 4

504 . 100 . 604 .

345 . 0 . 0 . 153 . 498 .

33. 7 4. 0 72. 6 4. 0

-89. 7 -34. 4 -25. 7 -33. 3

1128. 3 143. 6 -17. 8 2502. 5 3756. 7 OPTIO

N CAS E 5

504 . 100 . 604 .

345 . 0 . 0 . 153 . 498 .

29. 7 4. 0 72. 6 4. 0

-90. 9 -34. 4 -25. 7 -33. 3

1130. 3 146. 9 -17. 8 2498. 7 3758. 1 OPTIO

N CAS E 6

509 . 95 . 604 .

351 . 0 . 0 . 147 . 498 .

16. 0 3. 9 71. 5 3. 9

-95. 1 -36. 1 -26. 8 -35. 0

1111. 6 142. 3 -18. 5 2521. 2 3756. 7
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL " 0. 0 0. 3 0. 5 0. 8 0. 8 0. 9 0. 8
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X "TOTAL " 5371 . 494 . 60 . 5925 . 5059 .

449 . 55 . 5562 . 4872 .

423 . 54 . 5350 . 3689 .

335 . 53 . 4077 . 3678 .

335 . 53 . 4066 . 3689 .

336 . 53 . 4078 . 3610 .

323 . 53 . 3986 .TABLE 1 5 INDUSTRIA LBOILE RNSP S HATIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

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

FUELDEMAN

D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUE LDEMAN D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUE

LOI L RESIDUA LFUE LOI L COA L "TOTAL "
EMISSIONS (10«« 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS {•/. CHANG

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

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L "TOTAL " TH E BAS E CAS E

288 . 180 . 468 .

142 . 0 . 7 . 158 . 307 .

267. 3 3. 9 55. 1 3. 8

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

944. 2 89. 2 5. 3 1299. 9 2338. 7 OPTIO

N CAS E 1

314 . 154 . 468 .

172 . 0 . 0 . 135 . 307 .

89. 9 2. 9 50. 4 2. 9

-66. 4 -25. 6 -8. 5 -23. 7

873. 9 76. 3 0. 3 1398. 4 2348. 9 OPTIO

N CAS E 2

336 . 132 . 468 .

185 . 0 . 0 . 122 . 307 .

56. 5 2. 8 47. 8 2. 8

-78. 9 -28. 2 -13. 2 -26. 3

831. 5 70. 1 -1. 1 1456. 3 2356. 8 OPTIO

N CAS E 3

418 . 50 . 468 .

255 . 0 . 0 . 52 . 307 .

16. 1 2. 1 35. 7 2. 1

-94. 0 -46. 2 -35. 2 -44. 7

634. 2 55. 7 -10. 1 1663. 4 2343. 2 OPTIO

N CAS E 4

418 . 50 . 468 .

255 . 0 . 0 . 52 . 307 .

U. 5 2. 1 35. 7 2. 1

-95. 7 -46. 2 -35. 2 -44. 7

634. 2 56. 5 -10. 1 1663. 7 2344. 2 OPTIO

N CAS E 5

418 . 50 . 468 .

255 . 0 . 0 . 52 . 307 .

10. 6 2. 1 35. 7 2. 1

-96. 0 -46. 2 -35. 2 -44. 7

634. 2 57. 0 -10. 1 1663. 4 2344. 5 OPTIO

N CAS E 6

423 . 45 . 468 .

261 . 0 . 0 . 46 . 307 .

6. 3 2. 0 34. 6 2. 0

-97. 6 -48. 7 -37. 2 -47. 4

617. 5 52. 7 -10. 8 1682. 3 2341. 7
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL "
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN OP M NO X "TOTAL " 0. 0 0. 4 0. 8 0. 2 0. 2 0. 2 0. 1

390 . 306 . 40 . 735 . 3077 .

261 . 34 . 3372 . 2891 .

235 . 34 . 3160 . 1994 .

130 . 33 . 2157 . 1994 .

130 . 33 . 2157 . 1994 .

130 . 33 . 2157 . 1926 .

117 . 33 . 2077 .TABLE 1 6 — IHDUSTRIA

LBOILE RHSP S HATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) > 5 0

FUELDEMAN

D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUELDEMAN

D (10»»1 2 BTUS ) NATURA LGAS DISTILLATE FUE

LOI L RESIDUA LFUE LOI L COA L "TOTAL "
EMISSIONS (10»« 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS ( XCHANG

E S0 2 P M NO X PMIO
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUEL "TOTAL " FRO M BAS E CASE ) TH E BAS E CAS E

756 . 425 . 1181 .

266 . 0 . 13 . 355 . 634 .

446. 9 25. 5 120. 3 20. 1

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

2067. 8 174. 4 -1. 4 2643. 9 4884. 6 OPTIO

N . CAS E 1

782 . 399 . 1181 .

296 . 0 . 6 . 332 . 634 .

268. 7 24. 5 115. 6 19. 2

-39. 9 -3. 9 -3. 9 -4. 5

1997. 4 161. 6 -6. 4 2742. 3 4894. 9 OPTIO

N CAS E 2

804 . 377 . 1181 .

309 . 0 . 6 . 319 . 634 .

235. 3 24. 4 113. 0 19. 1

-47. 3 -4. 3 -6. 1 -5. 0

1955. 0 155. 4 -7. 8 2800. 3 4902. 8 OPTIO

N CAS E 3

902 . 279 . 1181 .

404 . 0 . 6 . 225 . 634 .

166. 6 23. 4 95. 2 18. 1

-62. 7 -8. 2 -20. 9 -10. 0

1695. 7 165. 2 -22. 6 3075. 6 4913. 8 OPTIO

N CAS E 4

902 . 279 . 1181 .

404 . 0 . 6 . 225 . 634 .

154. 7 23. 4 95. 2 18. 1

-65. 4 -8. 2 -20. 9 -10. 0

1693. 7 165. 7 -22. 6 3079. 4 4916. 2 OPTIO

N CAS E 5

902 . 279 . 1181 .

404 . 0 . 6 . 225 . 634 .

150. 7 23. 4 95. 2 18. 1

-66. 3 -8. 2 -20. 9 -10. 0

1695. 7 169. 1 -22. 6 3075. 6 4917. 7 OPTIO

N CAS E 6

907 . 274 . 1181 .

410 . 0 . 6 . 219 . 634 .

137. 0 23. 3 94. 1 18. 0

-69. 3 -8. 6 -21. 8 -10. 4

1677. 0 164. 5 -23. 3 3098. 1 4916. 2
AHNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL " 0. 0 0. 2 0. 4 0. 6 0. 6 0. 7 0. 6
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN OP M NO X "TOTAL " 7179 . 552 . 75 . 7806 . 6867 .

507 . 70 . 7443 . 6681 .

481 . 69 . 7231 . 5498 .

393 . 68 . 5959 . 5486 .

393 . 68 . 5947 . 5498 .

394 . 68 . 5960 . 5418 .

381 . 68 . 5867 .TABLE 1 7 —

BOILE RSIZ E (MMBTU/HR ) TOTA L

FUE LDEMAN D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L "TOTAL "
FUE LDEMAN D (10»"1 2 BTUS ) NATURA LGA S DISTILLATE FUE

LOI L RESIDUA LFUE LOI L COA L "TOTAL "
EHISSIOH S (10** 3 TONS ) S0 2 P M NO X PMIO
EHISSIOH S ( XCHAHG

E FRO M BAS E CASE ) SO C P M NO X PMIO J AHNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAM ) P M HO X FUE L "TOTAL "
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL "
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X "TOTAL " INDUSTRIA LBOILE RHSP S NATIONA

LIMPACT S B

YBOILE RSIZE ,

TH E BAS E CAS E

2007 . 586 . 2593 .

352 . 0 . 22 . 392 . 766 .

515. 2 36. 4 133. 7 28. 2

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

2719. 1 185. 9 -5. 5 3307. 9 6207. 3

0. 0

8703 . 583 . 105 . 9391 . OPTIO

N CAS E 1

2033 . 560 . 2593 .

382 . 0 . 15 . 369 . 766 .

337. 0 35. 4 129. 2 27. 2

-34. 6 -2. 7 -3. 4 -3. 5

2648. 7 173. 1 -10. 5 3406. 3 6217. 7

0. 2

8391 . 537 . 100 . 9028 . OPTIO

N CAS E 2

2055 . 538 . 2593 .

396 . 0 . 15 . 356 . 766 .

303. 6 35. 2 126. 6 27. 0

-41. 1 -3. 3 -5. 3 -4. 3

2606. 3 166. 9 -11. 9 3464. 2 6225. 6

0. 3

8205 . 512 . 99 . 8816 . OPTIO

N CAS E 3

2153 . 440 . 2593 .

490 . 0 . 15 . 261 . 766 .

235. 0 34. 2 108. 6 26. 1

-54. 4 -6. 0 -18. 8 -7. 4

2347. 0 176. 7 -26. 7 3739. 5 6236. 6

0. 5

7022 . 424 . 98 . 7544 . 1986-199 0

OPTIO N CAS E 4

2153 . 440 . 2593 .

490 . 0 . 15 . 261 . 766 .

223. 0 34. 2 108. 6 26. 1

-56. 7 -6. 0 -18. 8 -7. 4

2345. 0 177. 2 -26. 7 3743. 4 6238. 9

0. 5

7011 . 423 . 98 . 7532 . OPTIO

N CAS E 5

2153 . 440 . 2593 .

490 . 0 . 15 . 261 . 766 .

219. 0 34. 2 108. 6 26. 1

-57. 5 -6. 0 -18. 8 -7. 4

2347. 0 180. 5 -26. 7 3739. 5 6240. 4

0. 5

7022 . 425 . 98 . 7544 . OPTIO

N CAS E 6

2158 . 435 . 2593 .

496 . 0 . 15 . 255 . 766 .

205. 3 34. 2 107. 5 26. 0

-60. 2 -6. 0 -19. 6 -7. 8

2328. 3 176. 0 -27. 4 3762. 1 6239. 0

0. 5

6943 . 412 . 98 . 7452 . 1



### -

•

-SIZ E CUSS : 100-15 0 TABLE 1 8 ~ IHDUSTRIA LBOILE RHSP S REGIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
S0 2 EHISSIOH S (SHOR T TOHS )

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

NE U EHG . 1. 0 0. 0 0. 0 1. 0

OPTIO HCAS E 1
NAT . GAS RESI DOI L COA L TOTA L NE

M EHG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 2
NAT . GAS RESI DOI L COA L TOTA L NE

U EHG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 3
NAT . GAS RESI DOI L COA L TOTA L NE

U EHG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 4

J NAT . GAS RESI DOI L COA L TOTA L NE

U EHG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 5
NAT . GAS RESI DOI L COA L TOTA L HE

H ENG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 6
NAT . GAS RESI DOI L COA L TOTA L HE

U ENG . 1. 0 0. 0 

# ?: 8 N

H

H

N

N

N

H Y

Y

Y

Y

Y

Y

. Y ./N.J . 1. 0 791. 0 0. 0 792. 0

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

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

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

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

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

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

1. 0 1318. 0 6278. 0 7597. 0

MID . ATL . 2. 0 0. 0 3098. 0 3099. 0

MID . ATL . 3. 0 0. 0 338. 0 341. 0

MID . ATL . 3. 0 0. 0 234. 0 237. 0

MID . ATL . 3. 0 0. 0 156. 0 159. 0

MID . ATL . 3. 0 0. 0 156. 0 159. 0

MID . ATL . 3. 0 0. 0 108. 0 111. 0 SO . ATL .

1. 0 5800. 0 20314. 0 26114. 0

SO . ATL . 2. 0 0. 0 8424. 0 8426. 0

SO . ATL . 3. 0 0. 0 3693. 0 3696. 0

SO . ATL . 4. 0 0. 0 718. 0 722. 0

SO . ATL . 4. 0 0. 0 624. 0 629. 0

SO . ATL . 4. 0 0. 0 431. 0 435. 0

SO . ATL . 4. 0 0. 0 144. 0 148. 0 MIDWES T

2. 0 3515. 0 18675. 0 22193. 0

MIDMES T 4. 0 0. 0 6838. 0 6842. 0

MIDMES T 5. 0 0. 0 2367. 0 2372. 0

MIDMES T 5. 0 0. 0 1638. 0 1644. 0

MIOHES T 5. 0 0. 0 1092. 0 1098. 0

MIDMES T 5. 0 0. 0 1092. 0 1098. 0

MIDMES T 5. 0 0. 0 1009. 0 1014. 0 SO . HES T

10. 0 0. 0 5477. 0 5487. 0

SO . HES T 10. 0 0. 0 1352. 0 1363. 0

SO . HES T 10. 0 0. 0 1352. 0 1363.0 .

SO . WES 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

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

L 1. 0 0. 0 6218. 0 6219. 0

CENTRA L 1. 0 0. 0 982. 0 984. 0

CENTRA L 1. 0 0. 0 676. 0 678. 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

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

L 2. 0 0. 0 3224. 0 3226. 0

NO . CNTR

L 2. 0 0. 0 1964. 0 1966. 0

HO . CNTR

L 2. 0 0. 0 1352. 0 1354. 0

NO . CNTR

L 2. 0 0. 0 936. 0 938. 0

HO . CNTR

L 2. 0 0. 0 624. 0 626. 0

NO . CNTR

L 2. 0 0. 0 624. 0 626. 0

NO . CNTR

L 2. 0 0. 0 216. 0 218. 0 HES T

3. 0 0. 0 1014. 0 1017. 0

HES T 3. 0 0. 0 1014. 0 1017. 0

HES T 3. 0 0. 0 1014. 0 1017. 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

HES T 3. 0 

# 8: 8 3. 0 HO . HES T

2. 0 0. 0 1345. 0 1347. 0

NO . HES T 2. 0 0. 0 491. 0 493. 0

NO . HES T 2: 0 0. 0 338. 0 340. 0

NO . HES T 2. 0 0. 0 234. 0 236. 0

NO . HES T 2. 0 0. 0 156. 0 158. 0

NO . HES T 2. 0 0. 0 156. 0 158. 0

NO . HES T 2. 0 0. 0 54. 0 56. 0 U S TOTA

L 25. 0 11424. 0 62545. 0 73993. 0

U S TOTA L 28. 0 0. 0 24164. 0 24192. 0

U S TOTA L 32. 0 0. 0 11131. 0 11162. 0

U S TOTA L 35. 0 0. 0 3761. 0 3796. 0

U S TOTA L 35. 0 0. 0 2653. 0 2688. 0

U S TOTA L 35. 0 0. 0 2459. 0 2494. 0

U S TOTA L 35. 0 0. 0 1531. 0 1566. 0SIZ E CLASS : 150-20 0 TABLE 1 9 ~ IHDUSTRIA LBOILE RHSP S REGIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
S0 2 EHISSIOH S (SHOR T TOHS )

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

NEH ENG . 1. 0 0. 0 0. 0 1. 0

OPTIO HCAS E 1
HAT . GAS RESI OOI L COA L TOTA L NE

U ENG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 2
NAT . GAS RESI DOI L COA L TOTA L NE

U EHG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 3
NAT . GAS RESI DOI L COA L TOTA L NE

U EHG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 4
NAT . GAS RESI OOI L COA L TOTA L ; NEH ENG .

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

OPTIO N CAS E 5
NAT . GAS RESI DOI L COA L TOTA L NE

U ENG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 6
NAT . GAS RESI DOI L COA L TOTA L NE

U ENG . 1. 0 0. 0 0. 0 1. 0 N

N

N

N

N

N

N Y ./N.J . 1. 0 0. 0 1966. 0 1967. 0

Y

Y

Y

Y

Y

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

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

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

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

,/N.J . 1. 0 0. 0 0. 0 1. 0

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

1. 0 0. 0 8414. 0 6415. 0

MIO . ATL . 1. 0 0. 0 4662. 0 4663. 0

MID . ATL . 1. 0 0. 0 3?27. 0 3328. 0

MIO . ATL . 2. 0 0. 0 1512. 0 1514. 0

MID . ATL . 2. 0 0. 0 1008. 0 1010. 0

MID . ATL . 2. 0 0. 0 1008. 0 1010. 0

MID . ATL . 2. 0 0. 0 697. 0 699. 0 SO . ATL .

0. 0 0. 0 27373. 0 27373. 0

SO . ATL . 0. 0 0. 0 10155. 0 10155. 0



### so : ATL . 0. 0 0. 0 6990. 0 6990. 0

SO . ATL . 3. 0 0. 0 1449. 0 1452. 0

SO . ATL . 3. 0 0. 0 1260. 0 1263. 0

SO . ATL . 3. 0 0. 0 870. 0 872. 0

SO . ATL . 3. 0 0. 0 290. 0 293. 0 MIOHES T

0. 0 0. 0 24628. 0 24626. 0

MIDHES T 0. 0 0. 0 11583. 0 11583. 0

MIOHES T 0. 0 0. 0 7974. 0 7974. 0

MIDHES T 3. 0 0. 0 1891. 0 1894. 0

MIDWES T 3. 0 0. 0 1260. 0 1264. 0

MIDHES T 3. 0 0. 0 1260. 0 1264. 0

MIDHES T 3. 0 0. 0 1164. 0 1167. 0 SO . HES T

7. 0 0. 0 23070. 0 23077. 0

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

SO . HES T H. O 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

SO . HES T 11. 0 0. 0 0. 0 H. O

SO . HES T 11. 0 0. 0 0. 0 H. O CEHTRA

L 0. 0 0. 0 11622. 0 11622. 0

CEHTRA L 1. 0 0. 0 1587. 0 1587. 0

CEHTRA L 1. 0 0. 0 1092. 0 1093. 0

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

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

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

CEHTRA L 2. 0 0. 0 0. 0 2. 0 NO . CNTR

L 0. 0 0. 0 4955. 0 4955. 0

NO . CNTR

L 0. 0 0. 0 3829. 0 3829.- 0

NO . CNTR

L 0. 0 0. 0 2840. 0 2840. 0

NO . CNTR

L 1. 0 0. 0 378. 0 380. 0

NO . CNTR

L 1. 0 0. 0 252. 0 254. 0

NO . CNTR

L 1. 0 0. 0 252. 0 254. 0

NO . CNTR

L 1. 0 0. 0 87. 0 89. 0 HES T

2. 0 0. 0 1092. 0 1094. 0

HES T 2. 0 0. 0 1092. 0 1094. 0

HES T 2. 0 0. 0 1092. 0 1094. 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

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

1. 0 0. 0 4684. 0 4685. 0

HO . HES T 1. 0 0. 0 3967. 0 3968. 0

NO . HES T 1. 0 0. 0 1891. 0 1892. 0

NO . HES T 1. 0 0. 0 1891. 0 1892. 0

NO . HES T 1. 0 0. 0 1260. 0 1261. 0

NO . HES T 1. 0 0. 0 1260. 0 1261. 0

NO . HES T 3. 0 0. 0 0. 0 3. 0 U S TOTA

L 12. 0 0. 0 107804. 0 107816. 0

U S TOTA L 17. 0 0. 0 36873. 0 36890. 0

U S TOTA L 17. 0 0. 0 25206. 0 25223. 0

U S TOTA L 26. 0 0. 0 7121. 0 7148. 0

U S TOTA L 26. 0 0. 0 5042. 0 5068. 0

U S TOTA L 26. 0 0. 0 4651. 0 4677. 0

U S TOTA L 28. 0 0. 0 2239. 0 2267. 0SIZ E CUSS : 200-25 0 TABLE 2 0 — INDUSTRIA

LBOILE RHSP S REGIOHA

LIMPACT S B

YBOILE RSIZE , 1986-1.99 0
S0 2 EHISSIOHS (SHOR T TONS )

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

NE UEHG . 0. 0 0. 0 0. 0 0. 0

OPTIO N CAS E 1
HAT . GAS RESI DOI L COA L TOTA L HE

UENG . 0. 0 0. 0 0. 0 0. 0

OPTIO N CAS E 2
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 0. 0 0. 0 0. 0

OPTIO N CAS E 3
NAT . GAS RESI OOI L COA L TOTA L NE

UENG . 0. 0 0. 0 0. 0 0. 0

OPTIO N CAS E 4 i HAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 0. 0 0. 0 0. 0

OPTIO HCAS E 5
HAT . GAS RESI DOI L COA L TOTA L NE

UEHG . 0. 0 0. 0 0. 0 0. 0

OPTIO N CAS E 6
NAT . GAS RESI DOI L COA L TOTA L NE

HENG . 0. 0 0. 0 0. 0 0. 0 N

N

N

N

N

H

N Y./H.J . 0. 0 0. 0 1264. 0 1264. 0

Y./H.J . 0. 0 0. 0 612. 0 612. 0

Y./N.J . 0. 0 0. 0 421. 0 422. 0

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

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

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

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

0. 0 0. 0 5943. 0 5943. 0

MID . ATL . 0. 0 0. 0 3634. 0 3634. 0

MID . ATL . 0. 0 0. 0 2744. 0 2744. 0

MID . ATL . 0. 0 0. 0 2139. 0 2139. 0

MID . ATL . 0. 0 0. 0 1426. 0 1426. 0

MID . ATL . 0. 0 0. 0 1426. 0 1426. 0

MID . ATL . 0. 0 0. 0 986. 0 986. 0 SO . ATL .

0. 0 0. 0 16606. 0 16606. 0

SO . ATL . 0. 0 0. 0 6256. 0 6256. 0

SO . ATL . 0. 0 0. 0 4307. 0 4307. 0

SO . ATL . 1. 0 0. 0 1118. 0 1120. 0

SO . ATL . 1. 0 0. 0 972. 0 974. 0

SO . ATL . 1. 0 0. 0 671. 0 672. 0

SO . ATL . 1. 0 0. 0 224. 0 225. 0 MIDHES T

0. 0 0. 0 25523. 0 25523. 0

MIDHES T 0. 0 0. 0 7888. 0 7888. 0

MIDHES T 0. 0 0. 0 5430. 0 5430. 0

MIDHES T 2. 0 0. 0 1945. 0 1946. 0

MIDHES T 2. 0 0. 0 1296. 0 1298. 0

MIDHES T 2. 0 0. 0 1296. 0 1298. 0

MIDHES T 2. 0 0. 0 1197. 0 1199. 0 SO . HES T

4. 0 0. 0 28066. 0 28070. 0

SO . HES T 4. 0 0. 0 8160. 0 8164. 0

SO . HES T 4. 0 0. 0 5617. 0 5622. 0

SO .

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

HES T 8. 0 0. 0 0. 0 6. 0 CENTRA

L 0. 0 0. 0 5460. 0 5460. 0

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

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

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

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

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

CENTRA L 1. 0 0. 0 0. 0 1. 0 HO . CNTR

L 0. 0 0. 0 2623. 0 2623. 0

NO . CNTR

L 0. 0 0. 0 2244. 0 2244. 0

NO . CNTR

L 0. 0 0. 0 1545. 0 1545. 0

NO . CNTR

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

NO . CNTR

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

NO . CNTR

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

NO . 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

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

HES T 1. 0 0. 0 HO .

HO .

HO .

NO .

HO .

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

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

HES T 1. 0 0. 0 U S TOTA

L 6. 0 0. 0 85484. 0 85490. 0

U S TOTA L 7. 0 0. 0 28794. 0 26801. 0

U S TOTA L 7. 0 0. 0 20064. 0 20071. 0

U S TOTA L 15. 0 0. 0 5202. 0 5217. 0

U S TOTA L 15. 0 0. 0 3695. 0 3710. 0

U S TOTA L 15. 0 0. 0 3393. 0 3408. 0

U S TOTA L 15. 0 0. 0 2407. 0 2422. 0SIZ E CUSS : > 25 0 TABL E 2 1 — INDUSTRIA

L BOILE RNSP S REGIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
S0 2 EMISSIOMS (SHOR T TOHS )

BAS E
NAT . GAS RESIOOI L COA L TOTA L CAS E

NEH ENG . 1. 0 0. 0 0. 0 1. 0

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

H ENG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 2
NAT . GAS RESI DOI L COA L TOTA L NE

H ENG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 3
NAT . GAS RESIOOI L COA L TOTA L NE

U ENG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 4 > NAT . GA S RESIOOI L COA L TOTA L NE

U ENG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 5
NAT . GA S RESIDOI L COA L TOTA L HE

H ENG . 1. 0 0. 0 0. 0 1. 0

OPTIO N CAS E 6
NAT . GAS RESIDOI L COA L TOTA L HE

H ENG . 1. 0 0. 0 0. 0 1. 0 N

H

N

N

N

N

N .Y./N.J . 0. 0 0. 0 1690. 0 1691. 0

.Y./N.J . 0. 0 0. 0 1581. 0 1582. 0

.Y./N.J . 0. 0 0. 0 1581. 0 1582. 0

.Y./N.J . 0. 0 0. 0 1311. 0 1311. 0

.Y./N.J . 0. 0 0. 0 874. 0 874. 0

.Y./N.J . 0. 0 0. 0 874. 0 874. 0

.Y./N.J . 0. 0 0. 0 604. 0 605. 0 HID . ATL .

1. 0 0. 0 6082. 0 6083. 0

HID . ATL . 1. 0 0. 0 6031. 0 6032. 0

MID . ATL . 1. 0 0. 0 6031. 0 6032. 0

MID . ATL . 1. 0 0. 0 4216. 0 4217. 0

MID . ATL . 1. 0 0. 0 2965. 0 2966. 0

MID . ATL . 1. 0 0. 0 2965. 0 2966. 0

MID . ATL . 1. 0 0. 0 2051. 0 2052. 0 SO . ATL .

1. 0 0. 0 10886. 0 10887. 0

SO . ATL . 1. 0 0. 0 10886. 0 10887. 0

SO . ATL . 1. 0 0. 0 10886. 0 10887. 0

SO . ATL . 3. 0 0. 0 4606. 0 4609. 0

SO . ATL . 3. 0 0. 0 3901. 0 3904. 0

SO . ATL . 3. 0 0. 0 2798. 0 2801. 0

SO . ATL . 3. 0 0. 0 938. 0 940. 0 MIDHES T

3. 0 0. 0 9331. 0 9334. 0

MIDHES T 3. 0 0. 0 9331. 0 9334. 0

MIDHES T 3. 0 0. 0 9331. 0 9334. 0

MIDHES T 3. 0 0. 0 6460. 0 6464. 0

MIOHES T 3. 0 0. 0 4307. 0 4310. 0

MIDUES T 3. 0 0. 0 4307. 0 4310. 0

MIDHES T 3. 0 0. 0 3977. 0 3980. 0 SO . HES T

6. 0 0. 0 21231. 0 21238. 0

SO . HES T 6. 0 0. 0 21231. 0 21238. 0

SO . HES T 6. 0 0. 0 21231. 0 21238. 0

SO . HES T 11. 0 0. 0 7537. 0 7548. 0

SO . HES T 11. 0 0. 0 6554. 0 6565. 0

SO . HES T 11. 0 0. 0 4522. 0 4533. 0

SO . HES T 11. 0 0. 0 1038. 0 1049. 0 CEHTRA

L 1. 0 0. 0 1893. 0 1894. 0

CENTRA L 1. 0 0. 0 1893. 0 1894. 0

CENTRA L 1. 0 0. 0 1893. 0 1694. 0

CENTRA L 1. 0 0. 0 1311. 0 1312. 0

CEHTRA L 1. 0 0. 0 874. 0 875. 0

CEHTRA L 1. 0 0. 0 874. 0 875. 0

CENTRA L 1. 0 0. 0 138. 0 139. 0 NO . CNTR

L 1. 0 0. 0 3854. 0 3855. 0

HO . CNTR

L 1. 0 0. 0 3854. 0 3855. 0

NO . CNTR

L 1. 0 0. 0 3854. 0 3655. 0

NO . CNTR

L 2. 0 0. 0 1404. 0 1406. 0

NO . CNTR

L 2. 0 0. 0 936. 0 938. 0

NO . CNTR

L 2. 0 0. 0 936. 0 938. 0

NO . CNTR

L 2. 0 0. 0 325. 0 326. 0 HES T

3. 0 0. 0 1014. 0 1018. 0

HES T 3. 0 0. 0 1014. 0 1018. 0

HES T 3. 0 0. 0 1014. 0 1018. 0

HES T 3. 0 0. 0 702. 0 706. 0

HES T 3. 0 0. 0 468. 0 472. 0

HES T 3. 0 0. 0 468. 0 472. 0

HES T 3. 0 0. 0 162. 0 166. 0 NO . HES T

2. 0 0. 0 2559. 0 2561. 0

HO . HES T 2. 0 0. 0 1919. 0 1922. 0

NO . HES T 2. 0 0. 0 1919. 0 1922. 0

NO . HES T 2. 0 0. 0 1919. 0 1922. 0

NO . HES T 2. 0 0. 0 1280. 0 1282. 0

NO . HES T 2. 0 0. 0 1280. 0 1282. 0

NO . HES T 2. 0 0. 0 444. 0 446. 0 U S TOTA

L 20. 0 0. 0 58542. 0 58562. 0

U S TOTA L 20. 0 0. 0 57742. 0 57762. 0

U S TOTA L 20. 0 0. 0 57742. 0 57762. 0

U S TOTA L 27. 0 0. 0 29468. 0 29495. 0

U S TOTA L 27. 0 0. 0 22159. 0 22186. 0

U S TOTA L 27. 0 0. 0 19024. 0 19051. 0

U S TOTA L 27. 0 0. 0 9677. 0 9704. 0SIZ E CUSS : 100-15 0

BAS E CAS E NE M ENG . HAT . GAS 2683. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2683. 0

OPTIO N CAS E 1 HEHENG . NAT . GA S 2683. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2683. 0

OPTIO N CAS E 2 NE UENG . NAT . GAS 2683. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2683. 0

OPTIO N CAS E 3 NE UENG . NAT . GA S 2683. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2683. 0

OPTIO N CAS E 4 iNE UENG . NAT . GA S 2683. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2683. 0

OPTIO N CAS E 5 NEHENG . HAT . GA S 2683. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2683. 0

OPTIO N CAS E 6 HEHEHG . HAT . GA S 2683. 0 RESIDOI L0. 0 COA L0. 0 TOTA L2683. 0 N

N

N

N

N

N

N TABLE

•Y./N.J . 2683. 0 493. 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

.Y./N.J . 3176. 0 0. 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

•Y./N.J . 3176. 0 0. 0 0. 0 3176. 0 2 2 —

INDUSTRIA

LBOILE R

MID . ATL . 4928. 0 821. 0 4490. 0 10238. 0

MID . ATL . 5749. 0 0. 0 4490. 0 10238. 0

MID . ATL . 9527. 0 0. 0 712. 0 10238. 0

MID . ATL . 9527. 0 0. 0 712. 0 10238. 0

MID . ATL . 9527. 0 0. 0 712. 0 10238. 0

MID . ATL . 9527. 0 0. 0 712. 0 10238. 0

MIO . ATL . 9527. 0 0. 0 712. 0 10238. 0 FOSSI L

SO . ATL . 3833. 0 3614. 0 10238. 0 17684. 0

SO . ATL . 5475. 0 0. 0 12209. 0 17684. 0

SO . ATL . 9910. 0 0. 0 7775. 0 17684. 0

SO . ATL . 14837. 0 0. 0 2847. 0 17684. 0

SO . ATL . 14837. 0 0. 0 2847. 0 17684. 0

SO . ATL . 14837. 0 0. 0 2847. 0 17684. 0

SO . ATL . 14837. 0 0. 0 2847. 0 17664. 0 NSP S REGIONA L IMPACT S
FUE LDEMAN D

MIDHES T 7884. 0 2190. 0 12866. 0 22940. 0

MIDHES T 13031. 0 0. 0 9910. 0 22940. 0

MIDHES T 17958. 0 0. 0 4982. 0 22940. 0

MIDHES T 17958. 0 0. 0 4982. 0 22940. 0

MIDHES T 17958. 0 0. 0 4982. 0 22940. 0

MIOHES T 17958. 0 0. 0 4982. 0 22940. 0

MIDMES T 17958. 0 0. 0 4982. 0 22940. 0 (10*» 9

SO . HES T 34766. 0 0. 0 2847. 0 37613. 0

SO . HES T 34766. 0 0. 0 2847. 0 37613. 0

SO . HES T 34766. 0 0. 0 2847. 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

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

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

YBOILE R
BTUS )

CENTRA L 3942. 0 0. 0 2245. 0 6187. 0

CENTRA L 4763. 0 0. 0 1424. 0 6187. 0

CENTRA L 4763. 0 0. 0 1424. 0 6187. 0

CENTRA L 6187. 0 0. 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

CENTRA L 6187. 0 0. 0 0. 0 6187. 0 SIZE , 1986 -

HO . CHTR

L 6023. 0 0. 0 3340. 0 9362. 0

NO . CNTR

L 6515. 0 0. 0 2847. 0 9362. 0

HO . CHTR

L 6515. 0 0. 0 2847. 0 9362. 0

NO . CNTR

L 6515. 0 0. 0 2847. 0 9362. 0

NO . CNTR

L 6515. 0 0. 0 2847. 0 9362. 0

NO . CNTR

L 6515. 0 0. 0 2847. 0 9362. 0

HC . CNTR

L 6515. 0 0. 0 2847. 0 9362. 0 199 0

HES T 9089. 0 0. 0 2135. 0 11224. 0

HES T 9089. 0 0. 0 2135. 0 11224. 0

HES T 9089. 0 0. 0 2135. 0 11224. 0

HES T 11224. 0 0. 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

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

5968. 0 0. 0 1533. 0 7501. 0

NO . HES T 6789. 0 0. 0 712. 0 7501. 0

NO . HES T 6769. 0 0. 0 712. 0 7501. 0

NO . HES T 6789. 0 0. 0 712. 0 7501. 0

NO . WES T 6789. 0 0. 0 712. 0 7501. 0

NO . HES T 6789. 0 0. 0 712. 0 7501. 0

NO . HES T 6789. 0 0. 0 712. 0 7501. 0 

### i

«

- U S TOTA L 81797. 0 7118. 0 39694. 0 128608. 0

U S TOTA L 92035. 0 0. 0 36573. 0 128608. 0

U S TOTA L 105175. 0 0. 0 23433. 0 128608. 0 

### j
U S TOTA L 116508. 0 0. 0 12100. 0 ; 126608. 0 } 

### i US TOTA L | 116506. 0 j 0. 0 >.. 12100. 0 j 128608. 0 i
'
U S TOTA L 116508. 0 0. 0 12100. 0 128608. 0

, U S TOTA L 116508. 0 0. 0 12100. 0 128608. 0SIZ E CUSS : 150-20 0 TABL E 2 3 — INDUSTRIA

LBOILE RNSP S REGIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
FOSSI LFUE

L DEMAN D(10»* 9 BTUS )

BAS E CAS E NE UENG . HAT . GAS 2070. 0 RESI OOI L0. 0 COA L0. 0 TOTA L2070.0 .

OPTIO HCAS E 1 HEHENG . NAT . GAS 2070. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2070. 0

OPTIO N CAS E 2 NE UENG . NAT . GAS 2070. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2070. 0

OPTIO N CAS E 3 HEHEHG . NAT . GAS 2070. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2070. 0

OPTIO N CAS E 4 ; NEHENG . NAT . GAS 2070. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2070. 0

OPTIO N CAS E 5 NE UENG . HAT . GAS 2070. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2070. 0

OPTIO N CAS E 6 NE UENG . NAT . GAS 2070. 0 RESI DOI L0. 0 COA L0. 0 TOTA L2070. 0 N

N

N

N

N

N

N .Y./N.J . 2529. 0 0. 0 1380. 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

.Y./H.J . 3909. 0 0. 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

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

2453. 0 0. 0 7358. 0 9811. 0

MID . ATL . 2453. 0 0. 0 7358. 0 9811. 0

MID . ATL . 2453. 0 0. 0 7358. 0 9811. 0

MID . ATL . 5212. 0 0. 0 4599. 0 9811. 0

MID . ATL . 5212. 0 0. 0 4599. 0 9811. 0

MID . ATL . 5212. 0 0. 0 4599. 0 9811. 0

MID . ATL . 5212. 0 0. 0 4599. 0 9811. 0 SO . ATL .

0. 0 0. 0 14717. 0 14717. 0

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

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

SO . ATL . 6968. 0 0. 0 5749. 0 14717. 0

SO . ATL . 8968. 0 0. 0 5749. 0 14717. 0

SO . ATL . 8968. 0 0. 0 5749. 0 14717. 0

SO . ATL . 8968. 0 0. 0 5749. 0 14717. 0 MIDWES T

0. 0 0. 0 16786. 0 16786. 0

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

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

MIDHES T 11038. 0 0. 0 5749. 0 16786. 0

MIDHES T 11038. 0 0. 0 5749. 0 16786. 0

MIDWES T 11038. 0 0. 0 5749. 0 16786. 0

MIDWES T 11038. 0 0. 0 5749. 0 16786. 0 SO . WES T

24835. 0 0. 0 10348. 0 35182. 0

SO . UES T 35182. 0 0. 0 0. 0 35182. 0

SO . WES T 35182. 0 0. 0 0. 0 35182.0 .

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

SO . WES T 35182. 0 0. 0 0. 0 35182. 0

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

SO . WES T 35182. 0 0. 0 0. 0 35182. 0 CEHTRA

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

CEHTRA L 2759. 0 0. 0 2300. 0 5059. 0

CENTRA L 2759. 0 0. 0 2300. 0 5059. 0

CENTRA L 5059. 0 0. 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

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

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

HO . CHTR

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

NO . CHTR

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

NO . CNTR

L 4829. 0 0. 0 1150. 0 5979. 0

1
HO . CHTR

L 4829. 0 0. 0 1150. 0 5979. 0

NO . CNTR

L 4829. 0 0. 0 1150. 0 5979. 0

NO . CNTR

L 4829. 0 0. 0 1150. 0 5979. 0 HES T

6209. 0 0. 0 2300. 0 8508. 0

WES T 6209. 0 0. 0 2300. 0 8508. 0

WES T 6209. 0 0. 0 2300. 0 8508. 0

WES T 8508. 0 0. 0 0. 0 8508. 0

WES T 8508. 0 0. 0 0. 0 8508. 0

WES T 8508. 0 0. 0 0. 0 8508. 0

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

2759. 0 0. 0 6439. 0 9198. 0

NO . HES T 3449. 0 0. 0 5749. 0 9198. 0

NO . UES T 3449. 0 0. 0 5749. 0 9198. 0

NO . HES T 3449. 0 0. 0 5749. 0 9198. 0

NO . HES T 3449. 0 0. 0 5749. 0 9198. 0

NO . HES T 3449. 0 0. 0 5749. 0 9198. 0

NO . HES T 9198. 0 0. 0 91981 0 U S TOTA

L 40854. 0 0. 0 70365. 0 111219. 0

U S TOTA L 56031. 0 0. 0 55188. 0 111219. 0

U S TOTA L 56031. 0 0. 0 55188. 0 111219. 0

U S TOTA L 88224. 0 0. 0 22995. 0 111219. 0

U S TOTA L 88224. 0 0. 0 22995. 0 111219. 0

U S TOTA L 88224. 0 0. 0 22995. 0 111219. 0

U S TOTA L 93973. 0 0. 0 17246. 0 111219. 0SIZ E CUSS : 200-25 0 TABLE 2 4 — INDUSTRIA

LBOILE RNSP S REGIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
FOSSI LFUE

LDEMAH D(10«« 9 BTUS )

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

NE W ENG . 887. 0 0. 0 0. 0 887. 0

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

W ENG . 887. 0 0. 0 0. 0 887. 0

OPTIO N CAS E 2
NAT . GAS RESI DOI L COA L TOTA L HE

W ENG . 887. 0 0. 0 0. 0 887. 0

OPTIO N CAS E 3
HAT . GAS RESI DOI L COA L TOTA L HEHEHG .

887. 0 0. 0 0. 0 887. 0

OPTIO N CAS E 4
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 887. 0 0. 0 0. 0 887. 0

OPTIO N CAS E 5
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 887. 0 0. 0 0. 0 687. 0

OPTIO N CAS E 6
NAT . GAS RESI DOI L COA L TOTA L NE

HENG . 887. 0 0. 0 0. 0 887. 0 N

N

N

N

N

N

N .Y./N.J . 887. 0 0. 0 887. 0 1774. 0

.Y./N.J . 887. 0 0. 0 887. 0 1774. 0

.Y./N.J . 887. 0 0. 0 887. 0 1774. 0

.Y./N.J . 1774. 0 0. 0 0. 0 1774. 0

.Y./N.J . 1774. 0 0. 0 0. 0 1774. 0

.Y./N.J . 1774. 0 0. 0 0. 0 1774. 0

.Y./N.J . 1774. 0 0. 0 0. 0 1774. 0 HID . ATL .

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

MID . ATL . 0. 0 0. 0 6504. 0 6504. 0

MID . ATL . 0. 0 0. 0 6504. 0 6504. 0

MID . ATL . 0. 0 0. 0 6504. 0 6504. 0

MID . ATL . 0. 0 0. 0 6504. 0 6504. 0

MID . ATL . 0. 0 0. 0 6504. 0 6504. 0

MID . ATL . 0. 0 0. 0 6504. 0 6504. 0 SO . ATL .

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

SO . ATL . 0. 0 0. 0 9067. 0 9067. 0

SO . ATL . 0. 0 0. 0 9067. 0 9067. 0

SO . ATL . 4632. 0 0. 0 4435. 0 9067. 0

SO . ATL . 4632. 0 0. 0 4435. 0 9067. 0

SO . ATL . 4632. 0 0. 0 4435. 0 9067. 0

SO . ATL . 4632. 0 0. 0 4435. 0 9067. 0 MIDHES T

0. 0 0. 0 11432. 0 11432. 0

MIDWES T 0. 0 0. 0 11432. 0 11432. 0

MIDWES T 0. 0 0. 0 11432. 0 11432. 0

MIDWES T 5519. 0 0. 0 5913. 0 11432. 0

MIDMES T 5519. 0 0. 0 5913. 0 11432. 0

MIDHES T 5519. 0 0. 0 5913. 0 11432. 0

MIDHES T 5519. 0 0. 0 5913. 0 11432. 0 SO . HES T

11925. 0 0. 0 14487. 0 26411. 0

SO . HES T 14585. 0 0. 0 11826. 0 26411. 0

SO . HES T 14585. 0 0. 0 11826. 0 26411.0 .

SO . HES T 26411. 0 0. 0 0. 0 26411. 0

SO . UES T 26411. 0 0. 0 0. 0 26411. 0

SO . HES T 26411. 0 0. 0 0. 0 26411. 0

SO . HES T 26411. 0 0. 0 0. 0 26411. 0 CEHTRA

L 0. 0 0. 0 1971. 0 1971. 0

CEHTRA L 1971. 0 0. 0 0. 0 1971. 0

CEHTRA L 1971. 0 0. 0 0. 0 1971. 0

CEHTRA L 1971. 0 0. 0 0. 0 1971. 0

CEHTRA L 1971. 0 0. 0 0. 0 1971. 0

CEHTRA L 1971. 0 0. 0 0. 0 1971. 0

CEHTRA L 1971. 0 0. 0 0. 0 1971. 0 HO . CHTR

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

NO . CNTR

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

NO . CNTR

L 0. 0 0. 0 3252. 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

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

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

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

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

NO . HES T 2661. 0 0. 0 0. 0 2661. 0

NO . HES T 2661. 0 0. 0 0. 0 2661. 0

NO . HES T 2661. 0 0. 0 0. 0 2661. 0

NO . HES T 2661. 0 0. 0 0. 0 2661. 0

NO . HES T 2661. 0 0. 0 0. 0 2661. 0

NO . HES T 2661. 0 0. 0 0. 0 2661. 0 U S TOTA

L 19414. 0 0. 0 47600. 0 67014. 0

U S TOTA L 24046. 0 0. 0 42968. 0 67014. 0

U S TOTA L 24046. 0 0. 0 42968. 0 67014. 0

U S TOTA L 50162. 0 0. 0 16852. 0 67014. 0

U S TOTA L 50162. 0 0. 0 16852. 0 67014. 0

U S TOTA L 50162. 0 0. 0 16852. 0 67014. 0

U S TOTA L 50162. 0 0. 0 16852. 0 67014. 0SIZ E CUSS : > 25 0 TABL E 2 5 — INDUSTRIA

LBOILE RNSP S REGIONA

LIMPACT S B

YBOILE RSIZE , 1986-1990 . FOSSI LFUE

L DEMAN D(10"» 9 BTUS )

BAS E CAS E NEHENG . NAT . GAS 1993. 0 RESI DOI L0. 0 COA L0. 0 TOTA L1993. 0

OPTIO N CAS E 1 NE UENG . HAT . GAS 1993. 0 RESI DOI L0. 0 COA L0. 0 TOTA L1993. 0

OPTIO HCAS E 2 NE UEHG . HAT . GAS 1993. 0 RESI OOI L0. 0 COA L0. 0 TOTA L1993. 0

OPTIO HCAS E 3 HE UENG . NAT . GAS 1993. 0 RESI DOI L0. 0 COA L0. 0 TOTA L1993. 0

OPTIO HCAS E 4 NEHENG . NAT . GAS 1993. 0 RESI DOI L0. 0 COA L0. 0 TOTA L1993. 0

OPTIO N CAS E 5 NE UENG . NAT . GA S 1993. 0 RESI DOI L0. 0 COA L0. 0 TOTA L1993. 0

OPTIO N CAS E 6 NE UENG . NAT . GA S 1993. 0 RESI DOI L0. 0 COA L0. 0 TOTA L1993. 0 N

N

N

N

N

N

N •Y./N.J . 1424. 0 0. 0 3986. 0 5409. 0

.Y./N.J . 1424. 0 0. 0 3986. 0 5409. 0

.Y./N.J . 1424. 0 0. 0 3986. 0 5409. 0

.Y./N.J . 1424. 0 0. 0 3986. 0 5409. 0

.Y./N.J . 1424. 0 0. 0 3986. 0 5409. 0

.Y./N.J . 1424. 0 0. 0 3986. 0 5409. 0

.Y./N.J . 1424. 0 0. 0 3986. 0 5409. 0 MID . ATL .

2135. 0 0. 0 14804. 0 16940. 0

MID . ATL . 2135. 0 0. 0 14804. 0 16940. 0

MID . ATL . 2135. 0 0. 0 14804. 0 16940. 0

MID . ATL . 3416. 0 0. 0 13523. 0 16940. 0

MID . ATL . 3416. 0 0. 0 13523. 0 16940. 0

MID . ATL . 3416. 0 0. 0 13523. 0 16940. 0

MID . ATL . 3416. 0 0. 0 13523. 0 16940. 0 SO . ATL .

3559. 0 0. 0 22918. 0 26477. 0

SO . ATL . 3559. 0 0. 0 22918. 0 26477. 0

SO . ATL . 3559. 0 0. 0 22918. 0 26477. 0

SO . ATL . 8683. 0 0. 0 17794. 0 26477. 0

SO . ATL . 8683. 0 0. 0 17794. 0 26477. 0

SO . ATL . 8663. 0 0. 0 17794. 0 26477. 0

SO . ATL . 6683. 0 0. 0 17794. 0 26477. 0 MIDWES T

11388. 0 0. 0 19644. 0 31032. 0

MIDWES T 11388. 0 0. 0 19644. 0 31032. 0

MIDHES T 11388. 0 0. 0 19644. 0 31032. 0

MIDWES T 11388. 0 0. 0 19644. 0 31032. 0

MIDWES T 11388. 0 0. 0 19644. 0 31032. 0

MIDWES T 11388. 0 0. 0 19644. 0 31032. 0

MIDWES T 11388. 0 0. 0 19644. 0 31032. 0 SO . HES T

21068. 0 0. 0 44698. 0 65766. 0

SO . HES T 21068. 0 

## o. o 44698. 0 65766. 0

SO . HES T 21068. 0 0. 0 44698. 0 65766. 0

SO . HES T 35872. 0 0. 0 29894. 0 65766. 0

SO . HES T 35872. 0 0. 0 29894. 0 65766. 0

SO . WES T 35872. 0 0. 0 29894. 0 65766. 0

SO . WES T 35872. 0 0. 0 29894. 0 65766. 0 CENTRA

L 2705. 0 0. 0 3986. 0 6690. 0

CENTRA L 2705. 0 0. 0 3986. 0 6690. 0

CENTRA L 2705. 0 0. 0 3986. 0 6690. 0

CENTRA L 2705. 0 0. 0 3986. 0 6690. 0

CENTRA L 2705. 0 0. 0 3986. 0 6690. 0

CENTRA L 2705. 0 0. 0 3986. 0 6690. 0

CENTRA L 2705. 0 0. 0 3986. 0 6690. 0 NO . CNTR

L 2135. 0 0. 0 8114. 0 10249. 0

NO . CNTR

L 2135. 0 0. 0 8114. 0 10249. 0

NO . CHTR

L 2135. 0 0. 0 8114. 0 10249. 0

HO . CNTR

L 5979. 0 0. 0 4271. 0 10249. 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 5979. 0 0. 0 4271. 0 10249. 0 HES T

11388. 0 0. 0 2135. 0 13523. 0

HES T 11388. 0 0. 0 2135. 0 13523. 0

HES T 11388. 0 0. 0 2135. 0 13523. 0

HES T 11388. 0 0. 0 2135. 0 13523. 0

HES T 11388. 0 0. 0 2135. 0 13523. 0

HES T 11388. 0 0. 0 2135. 0 13523. 0

HES T 11388. 0 0. 0 2135. 0 13523. 0 NO . UES T

7402. 0 0. 0 5836. 0 13239. 0

HO . HES T 7402. 0 0. 0 5836. 0 13239. 0

NO . HES T 7402. 0 0. 0 5836. 0 13239. 0

NO . UES T 7402. 0 0. 0 5836. 0 13239. 0

NO . HES T 7402. 0 0. 0 5836. 0 13239. 0

HO . HES T 7402. 0 0. 0 5836. 0 13239. 0

NO . HES T 7402. 0 0. 0 5836. 0 13239. 0 U S TOTA

L 65196. 0 0. 0 126122. 0 191318. 0

U S TOTA L 65196. 0 0. 0 126122. 0 191318. 0

U S TOTA L 65196. 0 0. 0 126122. 0 191318. 0

U S TOTA L 90250. 0 0. 0 101068. 0 191318. 0

U S TOTA L 90250. 0 0. 0 101068. 0 191318. 0

U S TOTA L 90250. 0 0. 0 101068. 0 191318. 0

U S TOTA L 90250. 0 0. 0 101066. 0 191316. 0SIZ E CUSS : 100-15 0 TABLE 2 6 — IHDUSTRIA

LBOILE RHSP S REGIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
ANNUALIZE

DCOST S (10»« 6 198 2 $ )

BAS E CAS E

NAT . GA S RESI DOI L COAL TOTAL NE UENG .

22. 6 0. 0 0. 0 22.6 .

OPTIO N CAS E 1

NAT . GA S RESI DOI L COAL TOTA L NE HENG .

22. 6 0. 0 0. 0 22. 6

OPTIO N CAS E 2

NAT . GA S RESI OOI L COA L TOTA L NE UENG .

22. 6 0. 0 0. 0 22. 6

OPTIO N CAS E 3

NAT . GA S RESI DOI L COAL TOTA L NE HENG .

22. 6 0. 0 0. 0 22. 6

OPTIO N CAS E 4

NAT . GA S RESI DOI L COAL TOTA L ' NE HENG .

22. 6 0. 0 0. 0 22. 6

OPTION CAS E 5

NAT . GA S RESI DOI L COA L TOTAL NE HENG .

22. 6 0. 0 0. 0 22. 6

OPTIO N CAS E 6

NAT . GA S RESI DOI L COAL TOTAL NE UENG .

22. 6 0. 0 0. 0 22. 6 N

N

N .

N .

N

N

N Y

Y

Y

Y

Y

.Y

• Y ./N.J . 21. 4 3. 8 0. 0 25. 3

./N.J . 25. 3 0. 0 0. 0 25. 3

./N.J . 25. 3 0. 0 0. 0 25. 3

./H.J . 25. 3 0. 0 0. 0 25. 3

,/N.J . 25. 3 0. 0 0. 0 25. 3

./N.J . 25. 3 0. 0 0. 0 25. 3

./N.J . 25. 3 0. 0 0. 0 25. 3 MID . ATL .

39. 9 7. 4 36. 0 83. 3

MID . ATL . 47. 3 0. 0 36. 9 84. 2

MIO . ATL . 77. 0 0. 0 5. 3 82. 3

MID . ATL . 77. 0 0. 0 5. 5 82. 6

MIO . ATL . 77. 0 0. 0 5. 5 82. 6

MID . ATL . 77. 0 0. 0 5. 5 82. 6

MID . ATL . 77. 0 

# 8: 8
82. 6 SO . ATL .

35. 2 30. 1 80. 2 145. 6

SO . ATL . 50. 3 0. 0 98. 5 148. 8

SO . ATL . 86. 1 0. 0 62. 1 148. 2

SO . ATL . 124. 4 0. 0 22. 7 147. 2

SO . ATL . 124. 4 0. 0 22. 7 147. 2

SO . ATL . 124. 4 0. 0 22. 8 147. 2

SO . ATL . 124. 4 0. 0 22. 9 147. 3 MIDHES T

68. 9 20. 0 101. 4 190. 3

MIDHES T 112. 8 0. 0 77. 9 190. 7

MIDHES T 150. 9 0. 0 37. 8 188^ 7

MIDHES T 150. 9 0. 0 40. 2 191. 1

MIDHES T 150. 9 0. 0 40. 3 191. 2

MIDHES T 150. 9 0. 0 40. 3 191. 2

MIDWES T 150. 9 0. 0 40. 3 191. 2 SO . WES T

261. 6 0. 0 21. 2 282. 8

SO . WES T 261. 6 0. 0 21. 7 283. 3

SO . HES T 261. 6 0. 0 21. 7 283.3 -

SO . HES T 282. 4 0. 0 0. 0 282. 4

SO . UES T 282. 4 0. 0 0. 0 282. 4

SO . UES T 282. 4 0. 0 0. 0 262. 4

SO . HES T 282. 4 0. 0 0. 0 282. 4 CENTRAL

32. 1 0. 0 16. 0 48. 1

CENTRAL 38. 0 0. 0 10. 4 48. 4

CENTRAL 38. 0 0. 0 10. 5 48. 4

CENTRAL 48. 1 0. 0 0. 0 48. 1

CENTRAL 48. 1 0. 0 0. 0 48. 1

CENTRAL 48. 1 0. 0 0. 0 48. 1

CENTRAL 48. 1 0. 0 0. 0 40. 1 HO .

HO .

NO .

NO .

NO .

NO .

HO . CHTR L 45. 3 0. 0 20. 6 65. 9

CHTR L 48. 7 0. 0 17. 2 65. 9

CHTR L 48. 7 0. 0 17. 2 65. 9

CHTR L 48. 7 0. 0 19. 0 67. 7

CNTR L 48. 7 0. 0 19. 0 67. 7

CHTR L 48. 7 0. 0 19. 1 67. 8

CHTR L 48. 7 0. 0 19. 2 67.' ' HES T

71. 3 0. 0 15. 5 86. 8

HES T 71. 3 0. 0 15. 5 86. 8

HES T 71. 3 0. 0 15. 5 86. 8

HES T 86. 5 0. 0 0. 0 86. 5

HES T 86. 5 0. 0 0. 0 86. 5

HES T 86. 5 0. 0 0. 0 86. 5

HES T 66. 5 0. 0 0. 0 Sf<.5 H

O

HO

H O

N O

N O

N O

N O . HES T 46. 1 0. 0 11. 2 57. 3

. UES T 51. 9 0. 0 5. 1 57. 0

. HES T 51. 9 0. 0 5. 1 57. 1

. HES T 51. 9 0. 0 5. 3 57. 2

. HES T 51. 9 0. 0 5. 3 57. 2

. HES T 51. 9 0. 0 5. 3 57. 2

. HES T 51. 9 0. 0 5. 3 57. 3 U S TOTA L

644. 4 61. 4 302. 1 1008. 0

U S TOTAL 729. 8 0. 0 283. 3 1013. 0

U S TOTAL 833. 5 0. 0 175. 2 1008. 7

U S TOTA L 917. 9 0. 0 92. 7 1010. 6

U S TOTA L 917. 9 0. 0 92. 9 1010. 8

U S TOTA L 917. 9 0. 0 93. 0 1010. 9

U S TOTA L 917. 9 0. 0 93. 2 

### ton . ?.SIZ E CUSS : 150-20 0 TABLE 2 7 — IHDUSTRIA

LBOILE RHSP S REGIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
ANNUALIZE

DCOST S (10** 6 198 2 $ )

BAS E CAS E

NAT . GA S RESI DOI L COAL TOTAL HE UENG .

16. 0 0. 0 0. 0 16 . Q

OPTIO N CAS E 1

NAT . GA S RESI DOI L COAL TOTAL NE UENG .

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

OPTIO HCAS E 2

HAT . GA S RESI DOI L COA L TOTA L NE HENG .

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

OPTION CAS E 3

NAT . GA S RESI DOI L COAL TOTA L NE HENG .

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

OPTION CAS E 4
J NAT . GA S RESI OOI L COAL TOTAL HE HEHG .

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

OPTION CAS E 5

NAT . GA S RESI DOI L COAL TOTAL HE HEHG .

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

OPTION CAS E 6

NAT . GA S RESI DOI L COAL TOTAL HE HEHG .

16. 0 0. 0 0. 0 16. 0 N

N

N

N

N

N

N Y

Y

Y

Y

Y

Y

Y ./H.J . 19. 2 0. 0 11. 4 30. 6

./N.J . 29. 9 0. 0 0. 0 29. 9

./N.J . 29. 9 0. 0 0. 0 29. 9

./N.J . 29. 9 0. 0 0. 0 29. 9

./N.J . 29. 9 0. 0 0. 0 29. 9

./N.J . 29. 9 0. 0 0. 0 29. 9

./N.J . 29. 9 0. 0 0. 0 29. 9 HID . ATL .

19. 3 0. 0 56. 2 75. 5

MID . ATL . 19. 3 0. 0 57. 3 76. 5

MID . ATL . 19. 3 0. 0 58. 5 77. 8

MID . ATL . 40. 6 0. 0 36. 4 77. 0

MID . ATL . 40. 6 0. 0 36. 5 77. 1

MID . ATL . 40. 6 0. 0 36. 5 77. 1

MID . ATL . 40. 6 0. 0 36. 6 77. 2 SO . ATL .

0. 0 0. 0 114. 6 114. 6

SO . ATL . 0. 0 0. 0 116. 3 116. 3

SO . ATL . 0. 0 0. 0 119. 2 119. 2

SO . ATL . 70. 5 0. 0 46. 9 117. 4

SO . ATL . 70. 5 0. 0 46. 9 117. 4

SO . ATL . 70. 5 0. 0 47. 0 117. 5

SO . ATL . 70. 5 0. 0 47. 1 117. 6 MIDHES T

0. 0 0. 0 133. 3 133. 3

MIDHES T 0. 0 0. 0 136. 4 136. 4

MIDUES T 0. 0 0. 0 138. 7 138. 7

MIDUES T 86. 4 0. 0 47. 2 133. 6

MIDHES T 66. 4 0. 0 47. 4 133. 7

MIDHES T 66. 4 0. 0 47. 4 133. 7

MIDHES T 86. 4 0. 0 47. 4 133. 7 SO . UES T

181. 1 0. 0 79. 0 260. 1

SO . HES T 254. 6 0. 0 0. 0 254. 6

SO . HES T 254. 6 0. 0 0. 0 254. 6

SO . HES T 254. 6 0. 0 0. 0 254. 6

SO . HES T 254. 6 0. 0 0. 0 254. 6

SO . HES T 254. 6 0. 0 0. 0 254. 6

SO . HES T 254. 6 0. 0 0. 0 254. 6 CEHTRA L

0. 0 0. 0 38. 0 38. 0

CEHTRAL 19. 9 0. 0 17. 0 37. 0

CENTRAL 19. 9 0. 0 17. 1 37. 1

CENTRAL 35. 9 0. 0 0. 0 35. 9

CENTRAL 35. 9 0. 0 0. 0 35. 9

CENTRAL 35. 9 0. 0 0. 0 35. 9

CENTRAL 35. 9 0. 0 0. 0 35. 9 HO .

HO .

HO .

HO .

NO .

NO .

NO . CNTR L 0. 0 0. 0 40. 8 40. 8

CNTR L 0. 0 0. 0 41. 1 41. 1

CNTR L 0. 0 0. 0 41. 1 41. 1

CNTR L 32. 1 0. 0 7. 7 39. 7

CNTR L 32. 1 0. 0 7. 7 39. 8

CNTR L 32. 1 0. 0 7. 7 39. 8

CNTR L 32. 1 0. 0 7. 8 39. 8 HES T

44. 6 0. 0 17. 1 61. 7

HES T 44. 6 0. 0 17. 1 61. 7

HES T 44. 6 0. 0 17. 1 61. 7

HES T 60. 5 0. 0 0. 0 60. 5

HES T 60. 5 0. 0 0. 0 60. 5

HES T 60. 5 0. 0 0. 0 60. 5

HES T 60. 5 0. 0 0. 0 60. 5 N

O

H O

N O

N O

HO

N O

N O . HES T 19. 7 0. 0 47. 3 67. 0

. HES T 24. 7 0. 0 42. 0 66. 7

. HES T 24. 7 0. 0 43. 0 67. 7

. HES T 24. 7 0. 0 43. 0 67. 7

. HES T 24. 7 0. 0 43. 2 67. 8

. HES T 24. 7 0. 0 43. 2 67. 8

. HES T 64. 2 

# 8: 8
64. 2 U S TOTA L

299. 9 0. 0 537. 7 837. 6

U S TOTA L 408. 9 0. 0 427. 2 836. 1

U S TOTA L 408. 9 0. 0 434. 8 843. 7

U S TOTA L 650. 9 0. 0 181. 2 832. 1

U S TOTA L 650. 9 0. 0 181. 7 832. 6

U S TOTA L 650. 9 0. 0 181. 8 832. 7

U S TOTA L 690. 5 0. 0 829 '.- .

### Ti-

-

SIZ E CUSS : 200-25 0 TABL E 2 8 — IHDUSTRIA

LBOILE RHSP S REGIOHA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
ANNUALIZE

DCOST S (10*« 6 198 2 $ )

BAS E

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

NEH ENG . 6. 9 0. 0 0. 0 6. 9

OPTION CAS E 1

NAT . GA S RESI DOI L COAL TOTAL NEH EHG .

6. 9 0. 0 0. 0 6. 9

OPTIO N CAS E 2

NAT . GA S RESI DOI L COAL TOTA L NEH EHG .

6. 9 0. 0 0. 0 6. 9

OPTION CAS E 3

NAT . GA S RESI DOI L COAL TOTA L NE

U ENG . 6. 9 0. 0 0. 0 6. 9

OPTION CAS E 4

HAT . GA S RESI DOI L COAL TOTAL i NE U ENG .

6. 9 0. 0 0. 0 6. 9

OPTION CAS E 5

HAT . GA S RESI DOI L COAL TOTAL NE

U ENG . 6. 9 0. 0 0. 0 6. 9

OPTION CAS E 6

NAT . GA S RESI DOI L COAL TOTAL NEH ENG . 6. 9 0. 0 N .

H

N .

N .

N

N

N Y

Y

Y

Y

Y

Y

Y ./N.J . 6. 9 0. 0 7. 1 13. 9

./H.J . 6. 9 0. 0 7. 4 14. 2

./H.J . 6. 9 0. 0 7. 4 14. 3

,/H.J . 13. 7 0. 0 0. 0 13. 7

./H.J . 13. 7 0. 0 0. 0 13. 7

./H.J . 13. 7 0. 0 0. 0 13. 7

./N.J . 13. 7 0. 0 0. 0 13. 7 HID

MI D

MID

MID

MID

MI D

MI D . ATL . 0. 0 0. 0 49. 2 49. 2

. ATL . 0. 0 0. 0 49. 7 49. 7

. ATL . 0. 0 0. 0 50. 6 50. 6

. ATL . 0. 0 0. 0 51. 8 51. 8

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

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

. ATL . 0. 0 0. 0 52. 1 52. 1 S O

S O

S O

S O

S O

SO

S O . ATL . 0. 0 0. 0 67. 2 67. 2

. ATL . 0. 0 0. 0 68. 2 68. 2

. ATL . 0. 0 0. 0 70. 0 70. 0

. ATL . 36. 4 0. 0 34. 3 70. 7

. ATL . 36. 4 0. 0 34. 3 70. 7

. ATL . 36. 4 0. 0 34. 4 70. 8

. ATL . 36. 4 0. 0 34. 5 70. 9 MIOHES T

0. 0 0. 0 83. 0 83. 0

MIDHES T 0. 0 0. 0 87. 9 87. 9

MIDHES T 0. 0 0. 0 89. 5 89. 5

MIDUES T 43. 2 0. 0 46. 0 89. 2

MIDWES T 43. 2 0. 0 46. 2 89. 4

HIDWES T 43. 2 0. 0 46. 2 89. 4

MIDHES T 43. 2 

### 46°: f 89. 4 SO . HES T

87. 9 0. 0 107. 5 195. 3

SO . UES T 107. 5 0. 0 88. 3 195. 8

SO . UES T 107. 5 0. 0 88. 6 196. 1 .

SO . UES T 191. 6 0. 0 0. 0 191. 6

SO . HES T 191. 6 0. 0 0. 0 191. 6

SO . HES T 191. 6 0. 0 0. 0 191. 6

SO . HES T 191. 6 0. 0 0. 0 191. 6 CEHTRAL

0. 0 0. 0 14. 9 14. 9

CEHTRAL 14. 2 0. 0 0. 0 14. 2

CEHTRAL 14. 2 0. 0 0. 0 14. 2

CEHTRAL 14. 2 0. 0 0. 0 14. 2

CENTRAL 14. 2 0. 0 0. 0 14. 2

CENTRAL 14. 2 0. 0 0. 0 14. 2

CENTRAL 14. 2 0. 0 0. 0 14. 2 NO .

NO .

NO .

NO .

NO .

NO .

NO . CNTR L 0. 0 0. 0 21. 8 21. 8

CNTR L 0. 0 0. 0 21. 9 21. 9

CNTR L 0. 0 0. 0 22. 0 22. 0

CNTR L 21. 5 0. 0 0. 0 21. 5

CHTR L 21. 5 0. 0 0. 0 .21. 5

CNTR L 21. 5 0. 0 0. 0 21. 5

CNTR L 21. 5 0. 0 0. 0 21. 5 WES T

21. 9 0. 0 0. 0 21. 9

HES T 21. 9 0. 0 0. 0 21. 9

HES T 21. 9 0. 0 0. 0 21. 9

HES T 21. 9 0. 0 0. 0 21. 9

HES T 21. 9 0. 0 0. 0 21. 9

HES T 21. 9 0. 0 0. 0 21. 9

HES T 21. 9 0. 0 0. 0 21. 9 NO . HES T

19. 0 0. 0 0. 0 19. 0

NO . HES T 19. 0 0. 0 0. 0 19. 0

HO . HES T 19. 0 0. 0 0. 0 19. 0

NO . HES T 19. 0 0. 0 0. 0 19. 0

NO . HES T 19. 0 0. 0 0. 0 19. 0

NO . HES T 19. 0 0. 0 0. 0 19. 0

NO . HES T 19. 0 0. 0 0. 0 19. 0 U S TOTA L

142. 4 0. 0 350. 7 493. 1

U S TOTA L 176. 3 0. 0 323. 5 499. 7

U S TOTA L 176. 3 0. 0 328. 1 504. 3

U S TOTA L 368. 3 0. 0 132. 1 500. 4

U S TOTA L 368. 3 0. 0 132. 5 500. 8

U S TOTA L 368. 3 0. 0 132. 6 500. 9

U S TOTA L 368. 3 0. 0 

# Jo 3 

# ?: ?

### -__» -

SIZ E CUSS : > 25 0 TABLE 2 9 ~ INDUSTRIA LBOILE RNSP S REGIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
ANNUALIZE

DCOST S (10** 6 198 2 $ ) 

# S i

BAS E

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

NE UENG . 15. 7 0. 0 0. 0 15. 7

OPTIO N CAS E 1

NAT . GA S RESI DOI L COA L TOTA L NE UENG .

15. 7 0. 0 0. 0 15. 7

OPTIO N CAS E 2

NAT . GA S RESI DOI L COA L TOTA L NE UENG .

15. 7 0. 0 0. 0 15. 7

OPTION CAS E 3

NAT . GA S RESI DOI L COA L TOTA L NE HENG .

15. 7 0. 0 0. 0 15. 7

OPTIO N CAS E 4 ; NAT . GA S RESI DOI L COA L TOTA L NE UENG .

15. 7 0. 0 0. 0 15. 7

OPTIO N CAS E 5

NAT . GA S RESI DOI L COAL TOTA L NE HENG .

15. 7 0. 0 0. 0 15. 7

OPTIO N CAS E 6

NAT . GA S RESI DOI L COAL TOTAL NE HENG .

15. 7 0. 0 0. 0 15. 7 N .

N .

N

N

N

N

H Y

Y

Y

Y

.Y

.Y

.Y ./H.J . 12. 1 0. 0 29. 3 41. 4

./N.J . 12. 1 0. 0 29. 3 41. 4

./N.J . 12. 1 0. 0 29. 3 41. 4

./N.J . 12. 1 0. 0 29. 7 41. 8

./N.J . 12. 1 0. 0 29. 8 41. 9

./N.J . 12. 1 0. 0 29. 8 41. 9

,/N.J . 12. 1 0. 0 29. 8 41. 9 MID . ATL .

18. 1 0. 0 106. 1 124. 2

MID . ATL . 18. 1 0. 0 106. 1 124. 2

MID . ATL . 18. 1 0. 0 106. 1 124. 2

MID . ATL . 27. 7 0. 0 97. 1 124. 8

MID . ATL . 27. 7 0. 0 97. 4 125. 1

MID . ATL . 27. 7 0. 0 97. 4 125. 1

MID . ATL . 27. 7 

### 97: 2 125. 3 SO . ATL .

30. 7 0. 0 166. 5 197. 1

SO . ATL . 30. 7 0. 0 166. 5 197. 1

SO . ATL . 30. 7 0. 0 166. 5 197. 1

SO . ATL . 69. 9 0. 0 131. 3 201. 2

SO . ATL . 69. 9 0. 0 131. 4 201. 3

SO . ATL . 69. 9 0. 0 131. 7 201. 6

SO . ATL . 69. 9 0. 0 132. 2 202. 1 MIDUES T

91. 6 0. 0 139. 9 231. 5

MIDUES T 91. 6 0. 0 139. 9 231. 5

MIDWES T 91. 6 0. 0 139. 9 231. 5

MIDWES T 91. 6 0. 0 145. 4 237. 1

MIDUES T 91. 6 0. 0 146. 0 237. 6

MIDUES T 91. 6 0. 0 146. 0 237. 6

MIDHES T 91. 6 0. 0 146. 0 237. 7 SO . HES T

159. 7 0. 0 3i6. 5 476. 1

SO . HES T 159. 7 0. 0 316. 5 476. 1

SO . UES T 159. 7 0. 0 316. 5 476. 1

SO . HES T 262. 3 0. 0 223. 5 485. 8

SO . HES T 262. 3 0. 0 223. 3 485. 6

SO . HES T 262. 3 0. 0 224. 3 486. 5

SO . UES T 262. 3 0. 0 224. 7 466. 9 CEHTRA L

20. 4 0. 0 26. 4 46. 8

CEHTRA L 20. 4 0. 0 26. 4 46. 8

CEHTRA L 20. 4 0. 0 26. 4 46. 8

CENTRA L 20. 4 0. 0 28. 7 49. 0

CENTRAL 20. 4 0. 0 28. 8 49. 1

CENTRAL 20. 4 0. 0 28. 8 49. 1

CENTRAL 20. 4 0. 0 28. 5 4* . 9 HO .

NO .

NO .

NO .

NO .

NO .

NO . CNTR L 15. 8 0. 0 47. 9 63. 7

CNTR L 15. 8 0. 0 47. 9 63. 7

CNTR L 15. 8 0. 0 47. 9 63. 7

CNTR L 40. 5 0. 0 24. 3 64. 8

CNTR L 40. 5 0. 0 24. 4 64. 9

CNTR L 40. 5 0. 0 24. 4 64. 9

CHTR L 40. 5 O. O 24. 6 65. 1 HES T

81. 8 0. 0 14. 0 95. 8

HES T 81. 8 0. 0 14. 0 95. 8

HES T 81. 8 0. 0 14. 0 95. 8

HES T 61. 8 0. 0 14. 9 96. 7

WES T 81. 8 0. 0 15. 0 96. 8

HES T 81. 8 0. 0 15. 0 96. 8

HES T 81. 8 0. 0 15. 1 <?.

.•) HO . UES T

54. 8 0. 0 39. 3 94. 1

NO . UES T 54. 8 0. 0 39. 4 94. 2

NO . HES T 54. 8 0. 0 39. 4 94. 2

NO . HES T 54. 8 0. 0 39. 4 94. 2

NO . HES T 54. 8 0. 0 39. 6 94. 4

NO . UES T 54. 8 0. 0 39. 6 94. 4

NO . HES T 54. 8 0. 0 39. 8 <7't.6 U S TOTA L

500. 6 0. 0 865. 7 1386. 3

U S TOTAL . 500. 6 0. 0 685. 9 1386. 5

U S TOTA L 500. 6 0. 0 685. 9 1386. 5

U S TOTA L 676. 7 0. 0 734. 3 1411. 1

U S TOTA L 676. 7 0. 0 735. 7 1412. 4

U S TOTA L 676. 7 0. 0 736. 9 1413. 6

U S TOTA L 676. 7 0. 0 738. 2 1415. 0