Hydrogen and syngas production by catalytic biomass gasification

认领

导出

下载 Link by DOI

反馈

作者信息关键词期刊信息基础信息归属信息摘要

成果类型：

期刊论文

作者：

Peng, W. X.;Wang, L. S.;Mirzaee, M.;Ahmadi, H.;Esfahani, M. J.*;...

通讯作者：

Esfahani, M. J.;Fremaux, S.

作者机构：

[Peng, W. X.; Wang, L. S.] Cent South Univ Forestry & Technol, Sch Mat Sci & Engn, Changsha 410004, Hunan, Peoples R China.

[Peng, W. X.] Zhaniajie Xianzonglin Agr Sci & Technol Dev Co Lt, Zhangjiajie 427000, Peoples R China.

[Mirzaee, M.] Islamic Azad Univ, Omidiyeh Branch, Young Researchers & Elite Club, Omidiyeh 6373193719, Iran.

[Ahmadi, H.] Islamic Azad Univ, Fac Environm & Energy, Sci & Res Branch, Dept Energy Engn, Tehran 1477893855, Iran.

[Esfahani, M. J.] Islamic Azad Univ, Delijan Branch, Young Researchers & Elite Club, Delijan, Iran.

通讯机构：

[Esfahani, M. J.] I

[Fremaux, S.] E

Islamic Azad Univ, Delijan Branch, Young Researchers & Elite Club, Delijan, Iran.

Ecole Cent Paris, F-92290 Paris, France.

语种：

英文

关键词：

Fluidized bed;Hydrogen;Ni/CeO2/Al2O3;Syngas;Tar

期刊：

Energy Conversion and Management

ISSN：

0196-8904

年：

2017

卷：

135

页码：

270-273

DOI：

10.1016/j.enconman.2016.12.056

机构署名：

本校为第一机构

院系归属：

材料科学与工程学院

摘要：

Air-steam gasification of wood residue was explored in a research scale fluidized bed. Catalytic activity of two different kinds of metal catalysts (Ni/CeO2/Al2O3) with various catalyst loadings (20, 30, and 40%) was also investigated at various residence time (20, 40, and 60 min) and gasification temperature (750, 825, and 900 °C). Non-catalytic experiments were also carried out to determine the optimum conditions for tar cracking and hydrogen/syngas production. Results were revealed that the high temperature (&sim;900 °C) and high catalyst loading (&sim;40%) are favora...

反馈

产权有误：本人成果被他人认领

数据有误：数据基本信息有误

归属有误：成果的院系归属、机构署名归属有误

其他原因：

验证码：

看不清楚，换一个

确定

取消

成果认领

标题：

用户	作者	通讯作者	--
	请选择	请选择	--

确定

取消

Hydrogen and syngas production by catalytic biomass gasification

反馈

成果认领

提示

该栏目需要登录且有访问权限才可以访问