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Selective oxidation of methane to methanol in oleum over Pd/C catalyst

机译:Pd / C催化剂上发烟硫酸中甲烷选择性氧化为甲醇

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摘要

The selective oxidation of methane to methanol over Pd/C catalysts generated from a PdCl2, precursor was investigated in oleum. Characterization of the catalysts was performed by X-ray diffraction, X-ray photo-electron spectroscopy, high-resolution transmission electron microscopy, and CO adsorption. The major product ill the oxidation reaction was methyl bisulfate, which was then hydrolyzed into methanol. Methane conversion of 23.6% with methanol selectivity of 69.5% and yield of 16.4% was achieved under the optimum conditions of 5% Pd/C, 30 mu mol Pd, reatction temperature 180 degrees C, methane pressure 4. 0 MPa, reaction time 4 h, and 50% sulfur trioxide concentration. After facile separation with the reactants and pretreatment, the catalyst could be reused several times with considerable stability. The selective oxidation of methane catalyzed by Pd/C catalysts in oleum possibly involved an electrophilic substitute mechanism. The catalystic performance was related to the Pd loading, dispersion, and particle size.
机译:在发烟硫酸中研究了由PdCl2前体生成的Pd / C催化剂上甲烷选择性氧化为甲醇的现象。通过X射线衍射,X射线光电子能谱,高分辨率透射电子显微镜和CO吸附来进行催化剂的表征。氧化反应的主要产物是硫酸氢甲酯,然后将其水解成甲醇。在5%Pd / C,30μmol Pd,反应温度180℃,甲烷压力4. 0 MPa,反应时间4的最佳条件下,甲烷转化率为23.6%,甲醇选择性为69.5%,产率为16.4%。 h,三氧化硫浓度为50%。与反应物轻松分离并进行预处理后,该催化剂可以稳定地重复使用几次。在发烟硫酸中,Pd / C催化剂催化的甲烷选择性氧化可能涉及亲电取代机理。催化性能与Pd的负载量,分散度和粒径有关。

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