Record Display for the EPA National Library Catalog

RECORD NUMBER: 35 OF 36

OLS Field Name OLS Field Data
Main Title Shawnee flue gas desulfurization computer model users manual
Author Sudhoff, F. A. ; Torstrick, R. L.
Other Authors
Author Title of a Work
Torstrick, R. L.
CORP Author Tennessee Valley Authority, Muscle Shoals, AL. Div. of Energy Demonstrations and Technology.
Publisher U.S. Environmental Protection Agency, Industrial Environmental Research Laboratory ;
Year Published 1985
Report Number TVA/OP/EDT-84/37 ; EPA-600/8-85-006
Stock Number PB85-243111
OCLC Number 12415526
Subjects Flue gases--Desulfurization--Mathematical models ; Scrubber (Chemical technology)--Mathematical models
Additional Subjects Air pollution control equipment ; Economic analysis ; Calcium oxides ; Substitutes ; Industrial wastes ; Combustion products ; Adipic acid ; Scrubbers ; Flue gases ; Limestone scrubbing ; Flue gas desulfurization
Internet Access
Description Access URL
http://nepis.epa.gov/Exe/ZyPDF.cgi?Dockey=9100BYFE.PDF
Holdings
Library Call Number Additional Info Location Last
Modified
Checkout
Status
EKBD  EPA-600/8-85-006 Research Triangle Park Library/RTP, NC 04/16/2004
NTIS  PB85-243111 Most EPA libraries have a fiche copy filed under the call number shown. Check with individual libraries about paper copy. 01/01/1988
Collation 263 p. in various pagings : ill. ; 28 cm.
Abstract
The manual describes a Shawnee flue gas desulfurization (FGD) computer model and gives detailed instructions for its use. The model, jointly developed by Bechtel National, Inc. and TVA (in conjunction with the EPA-sponsored Shawnee test program), is capable of projecting preliminary design and economics for lime- and limestone-scrubbing FGD systems, including spray tower, turbulent contact absorber (TCA), and venturi/spray-tower scrubbing options. It may be used to project the effect on system design and economics of variations in required SO2 removal, scrubber operating parameters (gas velocity, liquid/gas ratio, alkali stoichiometry, and liquor holdtime in slurry recirculation tanks), reheat temperature, and scrubber bypass. It may also be used to evaluate alternative waste disposal methods or additives (MgO or adipic acid) on costs for the selected process. Although the model is not intended to project the economics of an individual system to a high degree of accuracy, it allows prospective users to quickly project comparative design and costs for limestone and lime case variations on a common design and cost basis.
Notes
Distributed to depository libraries in microfiche. "March 1985." Bibliography: p. 91-94. Final. Prepared for U.S. Environmental Protection Agency, Office of Research and Development.