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K2O对Pt/γ-Al2O3上CO选择性氧化反应的助催效应

Selective Oxidation of CO in Hydrogen-rich Stream over K2O-promoted Pt/γ-Al2O3 Catalyst

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【作者】 严菁马建新

【Author】 YAN Jing~1,MA Jian-xin~(2*) (1.Institute of Industrial Catalysis ECUST, Shanghai 200237, China; 2.Clean Energy Automotive Engineering Center, Tongji University, Shanghai 200092, China)

【机构】 华东理工大学工业催化研究所同济大学新能源汽车工程中心 上海200237上海200092

【摘要】 采用等体积浸渍法制备Pt/γ-Al2O3催化剂,通过添加K2O考察其对改善富氢气氛中CO选择性氧化性能的影响。结果表明,当加入K2O的质量分数为0.034,且采取在负载Pt后再添加的方式时,可显著改善催化剂的低温活性,在120°C时CO转化率可达90%。降低富氢气中CO浓度有助于提高CO转化率。O2/CO增加也可提高CO转化率,但O2/CO的增加并不能提高CO氧化的选择性。为了同时得到CO高转化率和CO氧化高选择性,O2/CO(V∶V)为1.0~1.8。用BET、XRD和CO-TPD等表征方法说明了K2O的助催效应。

【Abstract】 γ-Al2O3 supported Pt-K2O catalysts for CO selective oxidation were prepared by using incipient wet impregnation. The catalytic performance of the K2O promoted Pt/γ-Al2O3 catalysts in the selective oxidation of CO in hydrogen rich stream were studied. The results showed that when the K2O content was 0.034, the activity of catalyst was improved significantly with the CO conversion of 90% at 120 °C. The decrease of CO concentration in hydrogen stream was preferred for obtaining higher conversion of CO at lower temperature. The increase of O2/CO ratio resulted in the increase of CO conversion, while the (decrease) of O2/CO did not always increase the selectivity of CO to CO2. In order to obtain high conversion and higher selectivity, the O2/CO ratio ranged from 1.0 to 1.8 is desired. The promotion effect of K2O was characterized by BET, XRD and CO-TPD.

  • 【文献出处】 华东理工大学学报 ,Journal of East China University of Science and Technology , 编辑部邮箱 ,2004年02期
  • 【分类号】TM911
  • 【被引频次】6
  • 【下载频次】115
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