Biomass Hydropyrolysis in a Pressurized Fluidized Bed Reactor

被引:59
|
作者
Dayton, David C. [1 ]
Carpenter, John [1 ]
Farmer, Justin [1 ]
Turk, Brian [1 ]
Gupta, Raghubir [1 ]
机构
[1] RTI Int, Ctr Energy Technol, Res Triangle Pk, NC 27709 USA
关键词
LIQUID FUEL; BIO-OILS;
D O I
10.1021/ef400355t
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Biomass pyrolysis and hydropyrolysis have been studied in a high-temperature, high-pressure fluidized bed reactor system. The reactor system can be operated at reaction temperatures up to 982 degrees C (1800 degrees F) and pressures up to 4 MPa (600 psi). Baseline biomass pyrolysis experiments with an inert heat transfer material were conducted at various pressures and hydrogen partial pressures to determine the effect of these variables on product yields and quality, defined by the amount of oxygen in the hydrocarbon-rich liquid product. Biomass hydropyrolysis was performed at temperatures between 375 and 400 degrees C at 2 MPa (300 psi) with selected hydroprocessing catalysts. The most promising catalyst was exposed to 2.9 kg of woody biomass for a total of 21.7 h time on stream over a 10 day period. The cumulative mass balance during this period was 83%, and the overall C-4(+) yield was 16 wt %. This corresponds to 31% of the energy in the input biomass feedstock recovered in the hydrocarbon-rich liquid that contained an average of 4.2 wt % oxygen on a dry basis.
引用
收藏
页码:3778 / 3785
页数:8
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