A calcium oxide sorbent process for bulk separation of carbon dioxide. Quarterly progress report 11, April 1992--June 1992
This research project is investigating the technical feasibility of a high-temperature, high-pressure (HTHP) process for the bulk separation of CO{sub 2} from coal-derived gas. Phase I research, which utilized an electrobalance reactor, was completed during the previous quarter and final experimental results have been reported. Phase II research involves a switch from the electrobalance reactor to a laboratory-scale fixed-bed reactor having feed and product gas analysis capability. Initial effort during Phase II has been limited to project planning including the design and construction of the fixed-bed reactor, developing specifications for gas analysis, and ordering the gas chromatograph system. These activities are described in the present report.
- Research Organization:
- Louisiana State Univ., Baton Rouge, LA (United States). Dept. of Chemical Engineering
- Sponsoring Organization:
- USDOE, Washington, DC (United States)
- DOE Contract Number:
- AC21-89MC26366
- OSTI ID:
- 10124877
- Report Number(s):
- DOE/MC/26366-3233; ON: DE93007549
- Resource Relation:
- Other Information: PBD: Aug 1992
- Country of Publication:
- United States
- Language:
- English
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