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Ni supported on the CaO modified attapulgite as catalysts for hydrogen production from glycerol steam reforming  ( SCI-EXPANDED收录 EI收录)  

文献类型:期刊文献

英文题名:Ni supported on the CaO modified attapulgite as catalysts for hydrogen production from glycerol steam reforming

作者:Feng, P.[1];Huang, K.[2];Xu, Q.[1,2];Qi, W.[3];Xin, S.[4];Wei, T.[1];Liao, L.[1];Yan, Y.[1]

机构:[1]East China Univ Sci & Technol, Res Ctr Biomass Energy, Key Lab Coal Gasificat & Energy Chem Engn, Minist Educ, Shanghai, Peoples R China;[2]Guangxi Acad Sci, Natl Engn Res Ctr Nonfood Biorefinery, Guangxi Key Lab Biorefinery, Nanning, Peoples R China;[3]Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou, Peoples R China;[4]Jianghan Univ, Hubei Key Lab Ind Fume & Dust Pollut Control, Wuhan, Peoples R China

年份:2020

卷号:45

期号:15

起止页码:8223

外文期刊名:INTERNATIONAL JOURNAL OF HYDROGEN ENERGY

收录:;EI(收录号:20200608134457);WOS:【SCI-EXPANDED(收录号:WOS:000523643400019)】;

基金:This project was financially supported by the National Natural Science Foundation of China (No.21376084), Guangxi Key Laboratory of Bio-refinery (GXKLB19-03) and Guangdong Provincial Key Laboratory of New and Renewable Energy Research and Development (Y909kn1001). The authors thank Research Center of Analysis and Test of East China University of Science and Technology for the help on the characterization.

语种:英文

外文关键词:Hydrogen; Steam reforming; Attapulgite; Ni catalysts; CaO

摘要:The Ni catalyst supported on CaO-modified attapulgite (CaO-ATP) were synthesized by wet impregnation method at a constant Ni metal loading (10 wt%). The catalyst was tested by carrying out a glycerin steam reforming reaction under the following conditions: 400-800 degrees C, W/G is 3, GHSV is 1 h(-1). Ni-CaO-ATP exhibited the highest hydrogen yield (85.30%) and glycerol conversion (93.71%) at 600 degrees C. The catalysts were characterized by N-2 adsorption/desorption, BET, XRD, H-2-TPR, TG and SEM. The results show that ATP has good resistance to carbon deposition. As an attapulgite modifier of Ni-CaO-ATP, CaO promotes the dispersion of the active component nickel species, which would promote the water gas shift reaction, leading to the improving of hydrogen yield. In addition, the addition of Ca would further enhance the inhibition of carbon deposition and prolong the life of the Ni -CaO-ATP catalyst. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.

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