文献类型：期刊文献

英文题名：Research of the combined reforming of bio-oil model compound for hydrogen production

作者：Xu, Qingli[1];Feng, Peng[1];Huang, Kai[2];Xin, Shanzhi[3];Wei, Ting[1];Liao, Lifang[1];Yan, Yongjie[1]

机构：[1]East China Univ Sci & Technol, Res Ctr Biomass Energy, Minist Educ, Key Lab Coal Gasificat & Energy Chem Engn, Shanghai 200237, Peoples R China;[2]Guangxi Acad Sci, Guangxi Key Lab Biorefinery, Natl Engn Res Ctr Nonfood Biorefinery, Nanning, Peoples R China;[3]Jianghan Univ, Hubei Key Lab Ind Fume & Dust Pollut Control, Wuhan, Hubei, Peoples R China

年份：2020

卷号：39

期号：2

外文期刊名：ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY

收录：;EI(收录号：20193207272517);WOS:【SCI-EXPANDED(收录号:WOS:000478377500001)】；

基金：National Natural Science Foundation of China, Grant/Award Number: 21376084; Key Laboratory of Particle Astrophysics, Institute of High Energy Physics, Grant/Award Number: 2017CFB370; Opening Project of State Key Laboratory of Non-Food Biomass and Enzyme Technology and Hubei Science and Technology Department Project; Guangdong Provincial Key Laboratory of New and Renewable Energy Research and Development, Grant/Award Number: Y909kn1001

语种：英文

外文关键词：bio-oil; CO2 reforming; combined-reforming; hydrogen; steam reforming

摘要：The combination of steam and CO2 reforming of bio-oil is proposed in this article. The combined reforming can make good use of the advantages of steam reforming and CO2 reforming. The results indicate that H-2 yield, potential H-2 yield, and H-2/CO were 60.23, 81.97, and 2.77%, respectively, at the condition of 700 degrees C and bio-oil:CO2:H2O = 1:0.5:1.5. Bio-oil:CO2:H2O has a significant effect on the H-2 yield, potential H-2 yield, and H-2/CO in the process of combined reforming. A different ratio of H-2/CO can be obtained by adjusting the proportion of bio-oil:CO2:H2O, which can meet different industry requirements. The results of X-ray diffraction and scanning electron microscope analyses indicate that the catalyst deactivation was the result of a combination of carbon deposition and Ni grain sintering, and the carbon deposition was a main reason for the catalyst deactivation.