Gasification of Low-Grade Coal in a Dual Fluidized-Bed Steam Gasifier

被引:10
|
作者
Kern, Stefan [1 ]
Pfeifer, Christoph [1 ]
Hofbauer, Hermann [1 ]
机构
[1] Vienna Univ Technol, Inst Chem Engn, A-1060 Vienna, Austria
关键词
ash; industrial chemistry; carbon; combustion; energy conversion; TAR REMOVAL CATALYST; BIOMASS GASIFICATION; OLIVINE; CONVERSION; PYROLYSIS; PRODUCTS; CHAR; WOOD;
D O I
10.1002/ente.201300009
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
The gasification of a bituminous coal was performed in a dual fluidized-bed (DFB) steam gasifier at a fuel power of 90 kW(th). The main aim of these tests was to prove the suitability of the DFB system for cheap low-grade coals that are often delivered with a wide range of particle sizes and ash loads. The fine fraction in particular can become entrained in the gas stream and thus be responsible for changes in the system performance and gas quality. The selected gasifier bed material was olivine, with an applied particle size of 375 mu m, the steam-to-carbon ratio was 1.3 kg(H2O)kgC(-1), and the gasification temperature was 850 degrees C. In addition to standard online analysis of the main components of the product gas, impurities that included NH3, H2S, and tar were also examined.
引用
收藏
页码:253 / 264
页数:12
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