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Biomass Gasification Behavior in an Entrained Flow Reactor: Gas Product Distribution and Soot Formation
Author(s) -
Ke Qin,
Peter Arendt Jensen,
Weigang Lin,
Anker Degn Jensen
Publication year - 2012
Publication title -
energy and fuels
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.861
H-Index - 186
eISSN - 1520-5029
pISSN - 0887-0624
DOI - 10.1021/ef300960x
Subject(s) - soot , char , syngas , pyrolysis , carbon fibers , biomass (ecology) , residence time (fluid dynamics) , chemistry , yield (engineering) , combustion , product distribution , straw , chemical engineering , pulp and paper industry , materials science , organic chemistry , inorganic chemistry , hydrogen , catalysis , metallurgy , agronomy , geotechnical engineering , composite number , composite material , biology , engineering
Biomass gasification and pyrolysis were studied in a laboratory-scale atmospheric pressure entrained flow reactor. Effects of operating parameters and biomass types on the syngas composition were investigated. In general, the carbon conversion during biomass gasification was higher than 90% at the optimal conditions of 1400 °C with steam addition. The biomass carbon that was not converted to gas in the gasification process only appeared as soot particles in the syngas in all of the experiments, except for the two experiments performed at 1000 °C, where a very small amount of char was also left. In comparison to pyrolysis, lower yields of soot, H2, and CO were produced during gasification. The yield of soot could be reduced by a longer residence time, larger feeder air flow, lower oxygen concentration, higher excess air ratio, higher steam/carbon ratio, and higher reactor temperature. Changes in residence time, feeder air flow, and oxygen concentration did not show a noticeable influence on H2 and CO yield...

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