详细信息
Innovative Cu/Ni/Fe/γ-Al2O3/Al mesh-type catalyst and compact plate reactor design for steam reforming of dimethyl ether ( SCI-EXPANDED收录 CPCI-S收录)
文献类型:会议论文
英文题名:Innovative Cu/Ni/Fe/γ-Al2O3/Al mesh-type catalyst and compact plate reactor design for steam reforming of dimethyl ether
作者:Chu, Hualong[1];Zhang, Qi[2];Chu, Yameng[2];Ding, Qiang[1];Wang, Qiang[1];Xu, Hong[1];Zhang, Li[1]
机构:[1]East China Univ Sci & Technol, Sch Mech & Power Engn, State Key Lab Chem Engn, Shanghai 200237, Peoples R China;[2]East China Univ Sci & Technol, Sch Chem Engn, Shanghai 200237, Peoples R China
会议论文集:7th KACST-Oxford-Petrochemical-Research-Centre (KOPRC) Petrochemicals Forum on Decarbonizing Fossil Fuel
会议日期:JUL 24-26, 2017
会议地点:Royal Soc, London, ENGLAND
主办单位:Royal Soc
语种:英文
外文关键词:Hydrogen production; Mesh-type catalyst; Compact plate reactor; Self-reduction; Dimethyl ether (DME); Steam reforming (SR)
摘要:With the intensification of energy depletion and environmental crisis, the development of hydrogen energy is drawing more and more attention. On-site steam reforming of alcohols and ethers in small-size devices is an effective way to supply hydrogen in a decentralized manner. In this paper, a new mesh-type structured catalyst was developed, which has a uniform gamma-Al2O3 support layer on the surface of commercial aluminium mesh prepared by the anodic oxidation method. The compact plate reactor and test system were designed to match the new catalyst. The steam reforming performance of Cu-Ni and Cu-Ni-Fe catalysts and the hydrogen production capacity of the compact plate reactor were investigated at different temperatures and gas hourly space velocity (GHSV) using dimethyl ether (DME) as the feedstock. The experimental results showed that the two catalysts exhibited good self-reduction property. The concentration of carbon monoxide in the product can be significantly reduced for the Cu-Ni-Fe catalyst. When the GHSV was 18,000 ml/(g h) and the temperature was 400 degrees C, the DME conversion was 66%, and the hydrogen production capacity per unit reaction chamber can reach 76.5 ml/(min cm(3)). The catalyst developed in this paper also has the advantages of high bonding strength, flexible deformability, light weight and economy.
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