Record Display for the EPA National Library Catalog


OLS Field Name OLS Field Data
Main Title Production of clean fuel gas from bituminous coal /
Author Curran, G. ; Clancey, J. ; Pasek, B. ; Pell., M.
Other Authors
Author Title of a Work
Curran, G. P.
CORP Author Consolidation Coal Co., Library, Pa. Research Div.
Publisher National Technical Information Service, U.S. Dept. of Commerce,
Year Published 1973
Report Number EPA/650-2-73-049; PB-232 695; EPA-EHSD-71-15; EPA-ROAP-21ADD-22
Stock Number PB-232 695
OCLC Number 14584424
Subjects Coal gasification. ; Coal--Desulfurization. ; Bituminous coal. ; Coal--Desulphurization
Additional Subjects Coal gasification ; Desulfurization ; Cost estimates ; Dolomite(Rock) ; Regeneration(Engineering) ; Manufactured gas ; Coal gas ; Cyclone separators ; Dust collectors ; Cost analysis ; Sorbents ; Fluidized bed processing ; Engineering drawings ; Flow charts ; Performance ; Bituminous coal ; Low sulfur fuels ; Claus process ; Particulates
Internet Access
Description Access URL
Library Call Number Additional Info Location Last
EJBD ARCHIVE EPA 650-2-73-049 Headquarters Library/Washington,DC 09/19/2011
EJBD  EPA 650-2-73-049 c.1 Headquarters Library/Washington,DC 05/17/2013
NTIS  PB-232 695 Most EPA libraries have a fiche copy filed under the call number shown. Check with individual libraries about paper copy. 01/01/1988
Collation xi, 237 pages : illustrations ; 28 cm
A process for the production of low-Btu gas from bituminous coals via fluid bed gasification is described. Coal processing consists of pretreatment, gasification, and final burnup. Hot fuel gas is desulfurized with half-calcined dolomite and cleaned of particulates in high-pressure drop cyclones. The sulfur acceptor is regenerated with steam and CO2. A liquid-phase Claus reactor is used to process the H2S in the regenerator offgas into elemental sulfur. Experimental data are presented which demonstrated feasibility of the major process steps. An economic evaluation of gas clean-up operations shows that regenerative use of acceptor is preferable to once-through, and that removal of particulates via cyclones, if feasible, is cheaper than water scrubbing with subsequent reheat. The cost of the gas desulfurization process including sorbent regeneration and sulfur recovery is of the order of 20 cents/MM Btu of product gas. (Modified author abstract)
Cover title. "Control systems Laboratory, National Environmental Research Center." "December 1973." Includes bibliographical references (pages 207-208). "PB 232 695." "EPA/650-2-73-049."