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微通道反应器内富氢重整气中CO选择性甲烷化净化
引用本文:刘文跃;董新法;高军;林维明. 微通道反应器内富氢重整气中CO选择性甲烷化净化[J]. 华南理工大学学报(自然科学版), 2009, 37(12)
作者姓名:刘文跃  董新法  高军  林维明
作者单位:广州市天河区五山路381号华南理工大学;华南理工大学化学与化工学院
摘    要:将4Ni-2Ru/ZrO2双金属催化剂均匀涂布到微通道反应器中,运用CO选择性甲烷化方法来净化富氢重整气中的CO。考察了焙烧温度、催化剂的涂布方法和CTAB/Zr的比例对催化剂性能的影响。实验结果表明:CTAB/Zr=0.35、350 ℃焙烧所制备的催化剂表现出良好的低温活性。反应温度240 ℃时可将CO的出口浓度降低到11 ppm,在温度240~300 ℃、空速13000~20000 h-1的范围内CO的转化率都可达99%以上,CO2的转化率不超过7%。

收稿时间:2008-11-05
修稿时间:2009-02-19

Selective Catalytic Methanation of CO in Hydrogen-rich Gas by the Use of a Microchannel Reactor
LIU WenyueDONG XinfaGAO JunLIN Weiming. Selective Catalytic Methanation of CO in Hydrogen-rich Gas by the Use of a Microchannel Reactor[J]. Journal of South China University of Technology(Natural Science Edition), 2009, 37(12)
Authors:LIU WenyueDONG XinfaGAO JunLIN Weiming
Abstract:4Ni-2Ru/ZrO2 bimetallic catalyst was homogeneous coated on a microchannel reactor, and using CO selective methanation to purify hydrogen-rich gas. The effects of calcination temperature, coating method and the ratio of CTAB to Zr were examined. The results showed that: 4Ni-2Ru/ZrO2 catalyst displayed excellent performance in low temperature when calcination temperature was 350 ℃ and the ratio of CTAB to Zr was 0.35. CO concentration can be reduced to 11 ppm at 240 ℃, and CO conversion can reach above 99%,CO2 conversion was less than 7% from 240 ℃ to 300 ℃ even operating at a gas-hourly-space-velocity as high as 13000~20000 h-1.
Keywords:CO selective methanation  hydrogen-rich gas  microchannel reactor  CO removal
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