Hydrogen production by semicoke gasification with a supercritical water fluidized bed reactor

被引:55
|
作者
Cheng, Zening [1 ]
Jin, Hui [1 ]
Liu, Shanke [1 ]
Guo, Liejin [1 ]
Xu, Paling [1 ]
Su, Di [1 ]
机构
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xian 710049, Peoples R China
基金
中国国家自然科学基金;
关键词
Hydrogen production; Semicoke gasification; Supercritical water; Alkali catalysts; ENTRAINED FLOW GASIFICATION; CATALYTIC GASIFICATION; BIOMASS GASIFICATION; ORGANIC-COMPOUNDS; COAL; COKE; CHAR; COMBUSTION; ADSORPTION; SIMULATION;
D O I
10.1016/j.ijhydene.2016.06.075
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Semicoke powders with particle size less than 6 mm are by-products during the pyrolysis of coal. Direct combustion of semicoke powders is difficult due to the low volatile content. Supercritical water gasification might provide an efficient conversion method for semicoke powders. In order to determine the optimum conditions of gasification of semicoke with the supercritical water fluidized bed reactor, the influences of the main operating parameters including temperature (540-660 degrees C), feedstock concentration (10-30 wt%), flow rate of preheated water (40-80 g/min) and alkali catalysts (K2CO3, KOH, Na2CO3 and NaOH) were systematically investigated in this study. The results showed that semicoke-water slurry of 30 wt% was continuously transported into the reactor and stably gasified without plugging problems. Hydrogen yield of 85.90 mol/kg was obtained with the hydrogen molar fraction of 61.02%. In particular, carbon gasification efficiency of more than 95% was obtained under the conditions of 660 degrees C, 60 g/min flow rate of preheated water and 10 wt% feedstock concentration with 5 wt% K2CO3. (C) 2016 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:16055 / 16063
页数:9
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