Preparation and performance of the catalyst in the steam reforming of ethanol

Feng Wu; Yuan Liu; Jie Sun; Shi Chen; Guo Qing Wang

Preparation and performance of the catalyst in the steam reforming of ethanol

Feng Wu
, Yuan Liu^*
, Jie Sun
, Shi Chen
, Guo Qing Wang

^*此作品的通讯作者

材料学院

Beijing Institute of Technology

科研成果: 期刊稿件 › 文章 › 同行评审

1 引用（Scopus）

摘要

Catalytic production of hydrogen by steam reforming of ethanol has been studied on a series of CeO₂ promoted Ni/γ-Al₂O₃ catalyst. The catalysts all exhibited higher H₂ yield and CO₂ selectivity. The CH₄ selectivity and CO selectivity were kept under a low level. At 600°C the H₂ yield on the 16%Ni/CeO₂/-γ-Al₂O₃ can reach 4.8, the selectivity of CO₂, CO and CH₄ was 70.7%, 21% and 7%.

源语言	英语
页（从-至）	461-463+466
期刊	Gongneng Cailiao/Journal of Functional Materials
卷	36
期	3
出版状态	已出版 - 3月 2005

联合国可持续发展目标

此成果有助于实现下列可持续发展目标：

可持续发展目标 7 经济适用的清洁能源

其它文件与链接

链接到 Scopus 的出版物

引用此

@article{95eb2c810b8241628c7b08a3366ff157,

title = "Preparation and performance of the catalyst in the steam reforming of ethanol",

abstract = "Catalytic production of hydrogen by steam reforming of ethanol has been studied on a series of CeO2 promoted Ni/γ-Al2O3 catalyst. The catalysts all exhibited higher H2 yield and CO2 selectivity. The CH4 selectivity and CO selectivity were kept under a low level. At 600°C the H2 yield on the 16\%Ni/CeO2/-γ-Al2O3 can reach 4.8, the selectivity of CO2, CO and CH4 was 70.7\%, 21\% and 7\%.",

keywords = "Ethanol steam reforming, Hydrogen production, Ni-catalyst",

author = "Feng Wu and Yuan Liu and Jie Sun and Shi Chen and Wang, \{Guo Qing\}",

year = "2005",

month = mar,

language = "English",

volume = "36",

pages = "461--463+466",

journal = "Gongneng Cailiao/Journal of Functional Materials",

issn = "1001-9731",

publisher = "Journal of Functional Materials",

number = "3",

}

TY - JOUR

T1 - Preparation and performance of the catalyst in the steam reforming of ethanol

AU - Wu, Feng

AU - Liu, Yuan

AU - Sun, Jie

AU - Chen, Shi

AU - Wang, Guo Qing

PY - 2005/3

Y1 - 2005/3

N2 - Catalytic production of hydrogen by steam reforming of ethanol has been studied on a series of CeO2 promoted Ni/γ-Al2O3 catalyst. The catalysts all exhibited higher H2 yield and CO2 selectivity. The CH4 selectivity and CO selectivity were kept under a low level. At 600°C the H2 yield on the 16%Ni/CeO2/-γ-Al2O3 can reach 4.8, the selectivity of CO2, CO and CH4 was 70.7%, 21% and 7%.

AB - Catalytic production of hydrogen by steam reforming of ethanol has been studied on a series of CeO2 promoted Ni/γ-Al2O3 catalyst. The catalysts all exhibited higher H2 yield and CO2 selectivity. The CH4 selectivity and CO selectivity were kept under a low level. At 600°C the H2 yield on the 16%Ni/CeO2/-γ-Al2O3 can reach 4.8, the selectivity of CO2, CO and CH4 was 70.7%, 21% and 7%.

KW - Ethanol steam reforming

KW - Hydrogen production

KW - Ni-catalyst

UR - https://www.scopus.com/pages/publications/18744410669

M3 - Article

AN - SCOPUS:18744410669

SN - 1001-9731

VL - 36

SP - 461-463+466

JO - Gongneng Cailiao/Journal of Functional Materials

JF - Gongneng Cailiao/Journal of Functional Materials

IS - 3

ER -

Preparation and performance of the catalyst in the steam reforming of ethanol

摘要

联合国可持续发展目标

其它文件与链接

学术指纹

引用此