Hydrogen Production by Raw Biomass Gasification in Supercritical Water with a Fluidization Bed System
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Hydrogen Production by Raw Biomass Gasification in Supercritical Water with a Fluidization Bed System
Vol. 43, Issue 2, Pages: 111-115(2009)
作者机构:
西安交通大学动力工程多相流国家重点实验室,西安,710049
作者简介:
基金信息:
DOI:
CLC:TK91
Online First:10 February 2009,
Published:2009
稿件说明:
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吕友军, 金辉, 郭烈锦, et al. Hydrogen Production by Raw Biomass Gasification in Supercritical Water with a Fluidization Bed System[J]. 2009, 43(2): 111-115.
DOI:
吕友军, 金辉, 郭烈锦, et al. Hydrogen Production by Raw Biomass Gasification in Supercritical Water with a Fluidization Bed System[J]. 2009, 43(2): 111-115.DOI:
Hydrogen Production by Raw Biomass Gasification in Supercritical Water with a Fluidization Bed System
A fluidization bed reactor is proposed for supercritical water gasification of biomass
and for reducing reactor plugging. The mixture of corn cobs and sodium carboxymethylcellulose is gasified for hydrogen production in the new supercritical water fluidization bed system with temperature range 550-650 ℃ and pressure of 25 MPa. The influences of the main parameters such as gasification time
temperature
flow rate
and feedstock concentration on the gasification process are studied. The results from experiments show that the temperature has a significant effect on gasification
and higher temperature is in favor of gasification. Smaller flow rate
which means longer reactor residence time
favors to hydrogen production. Gasification performance of the feedstock is rapidly decreased as increasing the concentration. Biomass feedstock of 18% in concentration is gasified stably during long-term operation and the reactor plugging is not observed.
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