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U.S. Department of Energy
Office of Scientific and Technical Information

Alternative process schemes for coal conversion. Progress report No. 3, June 1-August 31, 1979

Technical Report ·
DOI:https://doi.org/10.2172/5532215· OSTI ID:5532215
In coal gasification processes such as the flash hydropyrolysis or the Exxon catalytic process, methane is the major desired end product. However, methane is usually produced along with hydrogen and/or carbon monoxide. To obtain pipeline grade methane, it is necessary to develop economical methods of separating methane from hydrogen and/or carbon monoxide mixtures. The hydrogen and carbon monoxide are then recycled in the process. Several separation technologies such as absorption/stripping, cryogenic, clathrate formation have been examined. In this report, an absorption/stripping process calculation using propane as the absorption solvent for separation of methane from hydrogen and carbon monoxide has been performed. Detailed material and energy balances for the process as well as the dimensions of the absorber and the stripper are reported. Other major pieces of equipment such as heat exchangers pumps, and compressors were evaluated in order to determine the equivalent electrical energy of the process as approximately 13550 cal(e)/gm-mole methane produced. The purity of methane in the final stream is 96% by volume at 100/sup 0/F and 1000 psi. The present process appears to be a potential working process for methane separation in large quantity.
Research Organization:
Brookhaven National Lab., Upton, NY (USA)
DOE Contract Number:
EY-76-C-02-0016
OSTI ID:
5532215
Report Number(s):
BNL-51117
Country of Publication:
United States
Language:
English