文献类型：期刊文献

英文题名：An investigation of efficient microstructured reactor with monolith Co/anodic γ-Al2O3/Al catalyst in Fischer-Tropsch synthesis

作者：Zhang, Li[1];Chu, Hualong[1];Qu, Hao[1];Zhang, Qi[2];Xu, Hong[1];Cao, Jun[1];Tang, Zhiyong[3];Xuan, Jin[4]

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;[3]Chinese Acad Sci, Shanghai Adv Res Inst, Key Lab Low Carbon Convers Sci & Engn, Shanghai 201210, Peoples R China;[4]Heriot Watt Univ, Sch Engn & Phys Sci, Edinburgh EH14 4AS, Midlothian, Scotland

年份：2018

卷号：43

期号：6

起止页码：3077

外文期刊名：INTERNATIONAL JOURNAL OF HYDROGEN ENERGY

收录：;EI(收录号：20180304652979);WOS:【SCI-EXPANDED(收录号:WOS:000426225000001)】；

基金：Work supported by the research grant (No. 16DZ2260600) from Science and Technology Commission of Shanghai Municipality, and the Fundamental Research Funds for the Central Universities" (222201717012, 222201718005)

语种：英文

外文关键词：Microstructured reactor; Fischer-Tropsch synthesis; Cobalt-based catalyst; Anodic gamma-Al2O3 plate

摘要：A new type of microstructured reactor was applied in Fischer-Tropsch synthesis (FTS). Monolith Co/anodic gamma-Al2O3 plate type catalyst was adopted in the microstructured reactor which has the advantage that the microchannel was achieved through the gap between the catalyst plates, not machining. The gamma-Al2O3 support was prepared on aluminum plate following the anodization method. And the cobalt was loaded on the anodic gamma-Al2O3 support by impregnation. The thickness, morphology, structure, reduction behavior and the catalytic performance of the catalyst were characterized by scanning electron microscope (SEM), energy dispersive spectrometer (EDS), X-ray diffraction (XRD), as well as the H-2 temperature-programmed reduction (H-2-TPR). The performance of the catalyst and the microstructured reactor was experimentally characterized in FTS. The CO conversion (19.42%) with 2.7% of CH4 selectivity and 95.77% of C5+ selectivity was obtained with the newly designed microstructured reactor at 220 degrees C and 2.0 MPa under a gas hourly space velocity (GHSV) of 5,000 h(-1). And the activity of the catalyst can be shown greatly in this microstructured reactor. Furthermore, the new developed microreactor is simpler in structure and easier to manufacture at low cost compared with the microchannel reactors requiring precise machining. And the deactivation catalyst after long period operation can be easily replaced for this kind of microstructured reactor. (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.