Main Title |
Economic evaluation of a sodium/limestone double-alkali FGD process / |
Author |
Stephenson, C. D. ;
Burnett, T. A. ;
Torstrick, R. L.
|
Other Authors |
|
CORP Author |
Tennessee Valley Authority, Chattanooga. Div. of Energy Demonstrations and Technology.;Environmental Protection Agency, Research Triangle Park, NC. Air and Energy Engineering Research Lab. |
Publisher |
U.S. Environmental Protection Agency, Air and Energy Engineering Research Laboratory, |
Year Published |
1984 |
Report Number |
EPA/600/7-84/096; TVA/OP/EDT-84/9 |
Stock Number |
PB85-169886 |
Subjects |
Flue gases--Desulfurization--Economic aspects
|
Additional Subjects |
Air pollution control ;
Cost analysis ;
Flue gases ;
Design criteria ;
Calcium carbonates ;
Pilot plants ;
Industrial wastes ;
Combustion products ;
Economic analysis ;
Double alkali scrubbing ;
Limestone scrubbing ;
Forced oxidation system ;
Flue gas desulfurization
|
Holdings |
Library |
Call Number |
Additional Info |
Location |
Last Modified |
Checkout Status |
NTIS |
PB85-169886 |
Some EPA libraries have a fiche copy filed under the call number shown. |
|
07/26/2022 |
|
Collation |
87 pages : illustrations ; 28 cm |
Abstract |
The report gives results of a comparison of results from a recent forced-oxidation limestone flue gas desulfurization (FGD) process evaluation and those from a conceptual design and economic evaluation of a sodium/limestone double-alkali FGD process, based on recent EPA-sponsored pilot-plant and prototype test work. For a 500-MW new power unit burning 3.5% sulfur coal and meeting the 1979 new source performance standards, the estimated capital investments in 1982 costs are $95 million ($190/kW) for the sodium/limestone double-alkali process and $103 million ($206/kW) for the forced-oxidation limestone process. Estimated first-year annual revenue requirements in 1984 costs for these processes are $26 million and $29 million (9.3 and 10.6 mills/kWh), respectively. Although the sodium/limestone double-alkali process appears to be about 8% lower in capital investment, given the accuracy associated with studies of this type (+ or - 10%), it is uncertain if the sodium/limestone double-alkali process has a lower capital investment. In terms of first-year and levelized annual revenue requirements, the sodium/limestone double-alkali process shows a 12% and 14% lower cost, respectively, than the forced-oxidation limestone process and (thus) is marginally less expensive. However, economics for the double-alkali process are more uncertain than those for the other. |
Notes |
Caption title. "October 1984." "EPA-600/7-84-096." Microfiche. |