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Methane decomposition over Fe-based catalysts

机译:Fe基催化剂的甲烷分解

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Catalytic approach for methane decomposition can be seriously considered as a promising process for COx free hydrogen generation. In this study, catalytic methane decomposition was performed using Fe-based catalysts, and catalytic performance tests were carried out in a CH4:N-2 flow at 750 and 800 degrees C. The analyses of reaction products were carried out by a mass spectrometer. For the preparation of Fe-based catalysts, sol-gel method was utilized. Yttria (Y2O3) and alumina (Al2O3) were used as support materials. Theoretical molar ratios (Fe2O3/Y2O3/Al2O3) of the samples C1-C5 were 1:0:0, 1:1:0, 1:1:5, 2:1:4 and 3:1:6, respectively. The characterization analyses of fresh and spent catalysts were performed with XRD, SEM, TPR, TG-FTIR and BET surface analysis techniques. Surface basicity of catalysts was determined via CO2-TPD measurements. In the presence of Fe2O3/Y2O3 and Fe2O3/Y2O3/Al2O3 catalysts, methane conversions of 29% and 4% were achieved at 750 degrees C. Adding alumina into Fe2O3/Y2O3 catalyst leads to the formation of garnet type crystal structure which reduces catalytic activity. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:甲烷分解的催化方法可以严重被认为是Cox游离氢产生的有希望的方法。在该研究中,使用Fe基催化剂进行催化甲烷分解,并且在750和800℃下在CH 4:N-2流动中进行催化性能试验。通过质谱仪进行反应产物的分析。为了制备Fe基催化剂,使用溶胶 - 凝胶法。使用YTTRIA(Y2O3)和氧化铝(AL2O3)作为支撑材料。样品C1-C5的理论摩尔比(Fe 2 O 3 / Y 2 O 3 / Al2O3)分别为1:0:0,1:1:0,1:1:5,2:1:4和3:1:6。用XRD,SEM,TPR,TG-FTIR和BET表面分析技术进行新鲜和废催化剂的表征分析。通过CO2-TPD测量测定催化剂的表面碱度。在Fe 2 O 3 / Y 2 O 3和Fe 2 O 3 / Y 2 O 3 / Al 2 O 3催化剂存在下,在750℃下甲烷转化为29%和4%。将氧化铝加入Fe 2 O 3 / Y 2 O 3催化剂,导致石榴石型晶体结构的形成,从而降低催化活性。 (c)2020氢能源出版物LLC。 elsevier有限公司出版。保留所有权利。

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