Preparation and Performance of Ce/Zr Mixed Oxides for Direct Conversion of Methane to Syngas
来源期刊：Journal of Rare Earths2007年第S1期
论文作者：魏永刚 王华 李孔斋 刘明春 敖先权
文章页码：110 - 114
摘 要：CexZr1-xO2 mixed oxides with different Ce/Zr ratios were prepared by coprecipitation. The characterizations of mixed oxides were studied by X-ray diffraction （XRD） and H2-TPR. And the performances were tested in a fixed-bed quartz reactor. The results indicated that lattice oxygen of CexZr1-xO2 could oxidate methane to syngas and the incorporation of zirconium into the ceria lattice could improve the O2- mobility. The Ce0.7Zr0.3O2 had the best activity in investigative temperature ranging from 600 to 900 ℃. Effects of reaction time on H2/CO ratio were studied at 850 ℃ when using Ce0.7Zr0.3O2 as catalyst. The results indicated that the ratio was closed to 2 values in the first 10 min, however, it rapidly increased with reaction time after >10 min. The possible reason was that the direct partial oxidation of methane reaction was dominant in the first 10 min. However, the methane pyrogenation was responsible for the rapid increase of H2/CO ratio after 10 min. Thus, if syngas with H2/CO ratio of 2 wanted to be obtained, the reaction time needed to be controlled.
魏永刚，王华，李孔斋，刘明春，敖先权
摘 要：CexZr1-xO2 mixed oxides with different Ce/Zr ratios were prepared by coprecipitation. The characterizations of mixed oxides were studied by X-ray diffraction （XRD） and H2-TPR. And the performances were tested in a fixed-bed quartz reactor. The results indicated that lattice oxygen of CexZr1-xO2 could oxidate methane to syngas and the incorporation of zirconium into the ceria lattice could improve the O2- mobility. The Ce0.7Zr0.3O2 had the best activity in investigative temperature ranging from 600 to 900 ℃. Effects of reaction time on H2/CO ratio were studied at 850 ℃ when using Ce0.7Zr0.3O2 as catalyst. The results indicated that the ratio was closed to 2 values in the first 10 min, however, it rapidly increased with reaction time after >10 min. The possible reason was that the direct partial oxidation of methane reaction was dominant in the first 10 min. However, the methane pyrogenation was responsible for the rapid increase of H2/CO ratio after 10 min. Thus, if syngas with H2/CO ratio of 2 wanted to be obtained, the reaction time needed to be controlled.
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