Ni-Al2O3/Ni-foam catalyst with enhanced heat transfer for hydrogenation of CO2 to methane

被引:87
|
作者
Li, Yakun [1 ]
Zhang, Qiaofei [1 ]
Chai, Ruijuan [1 ]
Zhao, Guofeng [1 ]
Liu, Ye [1 ]
Lu, Yong [1 ]
Cao, Fahai [2 ]
机构
[1] E China Normal Univ, Sch Chem & Mol Engn, Shanghai Key Lab Green Chem & Chem Proc, Shanghai 200062, Peoples R China
[2] E China Univ Sci & Technol, Coll Chem Engn, Shanghai 200237, Peoples R China
关键词
heterogeneous catalysis; structured catalyst; methanation; foam; computational fluid dynamics simulation; SYNTHETIC NATURAL-GAS; GROUP-VIII METALS; CORE-SHELL CATALYSTS; AU/NI-FIBER CATALYST; CARBON-DIOXIDE; LOW-TEMPERATURE; SELECTIVE OXIDATION; NI/AL2O3; CATALYSTS; FOAM COMPOSITE; TO-PROPYLENE;
D O I
10.1002/aic.14935
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Monolithic Ni-Al2O3/Ni-foam catalyst is developed by modified wet chemical etching of Ni-foam, being highly active/selective and stable in strongly exothermic CO2 methanation process. The as-prepared catalysts are characterized by x-ray diffraction scanning electron microscopy, inductively coupled plasma atomic emission spectrometry, and H-2-temperature programmed reduction-mass spectrometry. The results indicate that modified wet chemical etching method is working efficiently for one-step creating and firmly embedding NiO-Al2O3 composite catalyst layer (approximate to 2 m) into the Ni-foam struts. High CO2 conversion of 90% and high CH4 selectivity of >99.9% can be obtained and maintained for a feed of H-2/CO2 (molar ratio of 4/1) at 320 degrees C and 0.1 MPa with a gas hourly space velocity of 5000 h(-1), throughout entire 1200 h test over 10.2 mL such monolithic catalysts. Computational fluid dynamics calculation and experimental measurement consistently confirm a dramatic reduction of hotspot temperature due to enhanced heat transfer. (c) 2015 American Institute of Chemical Engineers
引用
收藏
页码:4323 / 4331
页数:9
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