1. 西安建筑科技大学环境与市政工程学院,西安,710055
2. 西安交通大学动力工程多相流国家重点实验室,西安,710049
网络首发:2008-03-10,
纸质出版:2008
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闫秋会 1, 2, 郭烈锦 2, 等. 生物质/煤超临界水气化制氢的主要影响因素[J]. 西安交通大学学报, 2008,42(3):368-371.
闫秋会 1, 2, 郭烈锦 2, et al. Influence of Main Parameters on Hydrogen Production During Biomass/Coal Gasification in Supercritical Water[J]. 2008, 42(3): 368-371.
以羧甲基纤维素钠(CMC)/华亭烟煤的超临界水共气化制氢为例
考察了温度(350~700 ℃)、压力(20~35 MPa)和物料(CMC+煤)的质量分数w(1.1%~2.0%)等对生物质/煤共气化气体产物的影响.模拟和实验结果表明:得到的主要气体产物是H
2
、CO
2
和CH
4
产气中H
2
的摩尔分数随温度的升高而升高
但温度升高到一定值后
H
2
的摩尔分数(x(H
2
)=67%)保持不变; 随物料质量分数的增加
H
2
的摩尔分数减小
物料的温度和质量分数的变化对产气的作用远大于压力; 制氢的适宜温度为450~550 ℃、压力为25 MPa左右、w≥15%.提出后续实验应着重提高物料在反应器内的加热速率
筛选研究在较低温度下能有效催化产氢的Ni催化剂.
Crboxymethylcellulose(CMC)/Huating bituminous coal was considered to be an example of biomass/coal
and the effects of the reaction temperature(350-700 ℃)
pressure(20-35 MPa)and concentration of solution(1.1%-2.0%)on gaseous products during CMC/coal co-gasification in supercritical water were investigated. The simulation results and experimental data show that the main gaseous products are H
2
CO
2
and CH
4
. Moreover
hydrogen mole fraction increases with the reaction temperature but it is constant(67%)at a high temperature. Hydrogen mole fraction decreases with the concentration
and temperature and concentration have larger effec
ts on gaseous products than pressure. In addition the reasonable parameters for hydrogen production during CMC/coal co-gasification in supercritical water are 450-550 ℃
25 MPa
and the solution concentration≥ 15%. It is suggested that heating rate of feedstock in the reactor should be increased and Ni catalyst with good effects at low temperature should be studied in the future experiment.
肖军,段菁华,王华,等.低温热解生物质与煤共燃的污染性能和经济性能评价[J].再生资源研究,2003,2(1):28-33.
XIAO Jun, DUAN Jinghua, WANG Hua, et al. Pollution and economy evaluation of co-firing low-temperature pyrolyzed biomass with coal [J].Regenerative Resource Research, 2003,2(1):28-33.
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PHILLIP E S, SUDHAMA G, TAHMID I, et al. Reactions at supercritical water conditions: applications and fundamentals [J]. AIChE J, 1995, 41(7): 1 723-1778.
闫秋会,郭烈锦,梁兴,等.煤与生物质共超临界水催化气化制氢的实验研究 [J].西安交通大学学报,2005,39(5):454-457.
YAN Qiuhui,GUO Liejin,LIANG Xing,et al. Hydrogen production from co-gasification of coal and biomass in supercritical water by continuous flow thermal-catalytic reaction system [J].Journal of Xi'an Jiaotong University,2005,39(5):454-457.
郭烈锦,闫秋会,张西民.煤与生物质共超临界水催化气化制氢装置及方法:中国,10041633.8 [P]. 2007-01-03.
DUAN Z H, NANCY M, JONH H W. A general equation of state for supercritical fluid mixture and molecular dynamics simulation of mixture PVTX properties [J]. Geochimica et Cosmochimica Acta, 1996, 60(7): 1209-1216.
闫秋会,郭烈锦,张西民,等.超临界水中葡萄糖气化制氢的热力学分析 [J].化工学报, 2004,55(11):1916-1920.
YAN Qiuhui,GUO Liejin,ZHANG Ximin,et al. Thermodynamics analysis of hydrogen production by glucose gasification in supercritical water [J].Journal of Chemical Industry and Engineering, 2004,55(11):1916-1920.
裴爱霞.超/亚临界水中生物质气化制氢催化剂的实验研究及催化机理分析 [D].西安:西安交通大学能源与动力工程学院,2007.
ANTAL M J, ALLEN S, LICHWA J, et al. Hydrogen production from high-moisture content biomass in supercritical water [C]∥ Proceedings of the 1999 US DOE Hydrogen Program Review. Berkeley, USA: Department of Energy,1999.
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