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Modeling and experimental studies on devolatilization yields from a bituminous coal

Journal Article · · Ind. Eng. Chem. Res.; (United States)
DOI:https://doi.org/10.1021/ie00071a034· OSTI ID:7042844
A laboratory-scale fixed bed reactor was set up to simulate conditions existing in the devolatilization zone of an air-blow, Lurgi-type, fixed bed coal gasifier. The effects of temperature (350-550/sup 0/C) and particle size (1-9 mm) on the devolatilization behavior of a bituminous coal in such a reactor were studied. The feed gas composition was chosen to approximate that entering the devolatilization zone from the gasification zone below in a commercial-scale fixed bed reactor. Similar studies were also carried out on a thermogravimetric analysis (TGA) reactor, for purposes of comparison. A semitheoretical model, describing the transport of the tar and gas species to the surface of the particle, and the subsequent evolution of these, is developed. The model takes into account the softening characteristics of bituminous coals upon heating. The volatiles yield predicted by the model is next compared with the experimental results, and the agreement appears quite good.
Research Organization:
Dept. of Chemical Engineering, Washington State Univ., Pullman, WA (US)
OSTI ID:
7042844
Journal Information:
Ind. Eng. Chem. Res.; (United States), Journal Name: Ind. Eng. Chem. Res.; (United States) Vol. 26:11; ISSN IECRE
Country of Publication:
United States
Language:
English