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Title: A NOVEL CONCEPT FOR PREFERENTIAL PRODUCTION OF METHANE RICH SYNGAS FROM COAL GASIFICATION

Technical Report ·
OSTI ID:1028665

The overall objective of this multi-phase SBIR project is to develop a coal gasifier concept that yields higher methane (CH4) concentration in the syngas without compromising on the heating value of the syngas. Higher concentration of CH4 in syngas is desirable because it has higher calorific value (per unit mass) than any other hydrocarbon. In addition, utilization of the CH4 rich syngas in fuel cells facilitates better control of fuel cell stack temperature which improves power generation efficiency. However, existing commercial gasifiers predominantly produce CO and H2 rich syngas that contains minimal amount of CH4. In order to obtain high heating value syngas with preferential production of CH4, this proposal proposes to gasify coal in combination with a renewable, liquid, waste feedstock in a novel gasification process design. The proposed liquid feedstock is rich in oxygen which reduces amount of oxygen needed to carryout the gasification process and thus the cost. In addition, CPS conducted a 1-D kinetic and equilibrium calculation which showed that the renewable feedstock reduces tar formation, and helps in achieving higher heating value and CH4 in the syngas. In recent proof-of-concept experiments, we have determined that methanol (CH3OH) addition during steam gasification or coal pyrolysis enhances methane formation. We hypothesize that the tars released during coal devolatilization react with the methanol generated radicals to form low molecular weight hydrocarbons, primarily CH4 has been proved correct. It also appears that because the ratio of methanol to coal and steam to coal ratio was too high during the batch reactor experiments, significant fraction of tar was also converted to CO. Therefore, in order to achieve higher methane in a cost effective manner, experiments need to be done in a continuous flow reactor at isothermal temperatures where the ratio of the additive and steam needs to be carefully controlled.

Research Organization:
Creative Power Solutions (USA), Inc. 11010 N. Saguaro Blvd. Fountain Hills, AZ 85268
Sponsoring Organization:
USDOE Office of Science (SC)
DOE Contract Number:
SC0004188
OSTI ID:
1028665
Report Number(s):
DOE/SC00041-1
Country of Publication:
United States
Language:
English