Record Display for the EPA National Library Catalog

RECORD NUMBER: 173 OF 871

Main Title Comparison of West German and U.S. Flue Gas Desulfurization and Selective Catalytic Reduction Costs.
Author Emmel, T. E. ; Maibodi, M. ; Martinez, J. A. ;
CORP Author Radian Corp., Research Triangle Park, NC.;Environmental Protection Agency, Research Triangle Park, NC. Air and Energy Engineering Research Lab.
Publisher Apr 90
Year Published 1990
Report Number EPA-68-02-4286; EPA/600/7-90/009;
Stock Number PB90-206319
Additional Subjects United States ; Air pollution control ; Boilers ; Sulfur dioxide ; Nitrogen oxides ; Federal Republic of Germany ; Cost estimates ; Catalysis ; Combustion products ; Sorbents ; Calcium oxides ; Limestone ; Performance evaluation ; Design criteria ; Flue gas desulfurization ; Selective catalytic reduce ; Retrofitting ; Air pollution economics
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NTIS  PB90-206319 Some EPA libraries have a fiche copy filed under the call number shown. 07/26/2022
Collation 52p
Abstract
The report documents a comparison of the actual cost of retrofitting flue gas desulfurization (FGD) and selective catalytic reduction (SCR) on Federal Republic of German (FRG) boilers to cost estimating procedures used in the U.S. to estimate the retrofit of these controls on U.S. boilers. (NOTE: By the end of the 1980s, more than 45,000 MWe and, by early 1990, more than 34,000 MWe of coal- and oil-fired utility boilers in the FRG will have been retrofitted with FGD and SCR, respectively.). The estimated capital costs of FGD using U.S. procedures compared well to the reported capital cost for the 13 FRG boilers evaluated. The difference between the estimated and actual costs was -8 to 12%. However, there are significant design differences between the U.S. systems, built to comply with New Source Performance Standards (NSPS), and the FRG systems. These differences, which result in significantly lower capital costs on a dollar per kilowatt basis for the FRG systems, include: no spare absorber modules, large scrubber modules, and smaller sorbent and waste handling systems due to the low sulfur coals burned in the FRG. The estimated capital cost of SCR using the U.S. procedures also compared well to the reported capital costs for the nine FRG boilers evaluated. The difference was between -5 and 16%.