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Methane Decomposition Kinetics over Fe2O3 Catalyst in Micro Fluidized Bed Reaction Analyzer
Geng, SL; Han, ZN; Hu, Y; Cui, YB; Yue, JR; Yu, J; Xu, GW; Geng, Sulong; Han, Zhennan; Hu, Yan
刊名INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
2018
卷号57期号:25页码:8413
关键词COX-FREE HYDROGEN MULTIWALLED CARBON NANOTUBES NATURAL-GAS DECOMPOSITION THERMAL-DECOMPOSITION ALUMINA CATALYSTS PRODUCE HYDROGEN NICKEL-CATALYSTS NI DEACTIVATION NANOFIBERS
ISSN号0888-5885
DOI10.1021/acs.iecr.8b00662
文献子类Article
英文摘要Micro fluidized bed (MFB) reactor offers a good way to determine the intrinsic kinetics of some reactions. For catalytic decomposition of methane (CMD), the hydrogen production rate appears much higher when catalyst is injected into an MFB reactor by pulse, in comparison with that via gas switching. The carbon nanotubes (CNTs) produced in an MFB were more dispersed than that in fixed bed. Therefore, the micro fluidized bed reaction analyzer (MFBRA) is proven to be an alternative tool for determining kinetics of methane decomposition and offering the values of higher reference for CMD in industrial fluidized beds. Kinetics of CMD and catalyst deactivation over Fe2O3 catalyst were studied using MFBRA at temperatures of 750-900 degrees C and partial pressures of methane of 0.22, 0.50, 0.75, and 1.0 atm. The reaction order and activation energy of CMD were estimated to be 2.27 and 50 kJ/mol, respectively.
WOS记录号WOS:000436910500006
内容类型期刊论文
源URL[http://ir.ipe.ac.cn/handle/122111/26741]  
专题中国科学院过程工程研究所
推荐引用方式
GB/T 7714
Geng, SL,Han, ZN,Hu, Y,et al. Methane Decomposition Kinetics over Fe2O3 Catalyst in Micro Fluidized Bed Reaction Analyzer[J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH,2018,57(25):8413, 8423.
APA Geng, SL.,Han, ZN.,Hu, Y.,Cui, YB.,Yue, JR.,...&Xu, Guangwen.(2018).Methane Decomposition Kinetics over Fe2O3 Catalyst in Micro Fluidized Bed Reaction Analyzer.INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH,57(25),8413.
MLA Geng, SL,et al."Methane Decomposition Kinetics over Fe2O3 Catalyst in Micro Fluidized Bed Reaction Analyzer".INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH 57.25(2018):8413.
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