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首页> 外文期刊>Chemical Engineering Communications >Isomerization of n-butane:conversion as a function of sulfate loading on sulfated zirconia catalysts
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Isomerization of n-butane:conversion as a function of sulfate loading on sulfated zirconia catalysts

机译:正丁烷的异构化:转化率与硫酸化氧化锆催化剂上硫酸盐负载的关系

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摘要

Sulfur loading on a sulfated zirconia catalyst was studied as a function of H_2SO_4 concentration.The resulting catalytic activity was tested using the isomerization of n-butane as a reaction probe at 200 deg C.Optimum catalytic activity was observed for a catalyst prepared using 0.5 N H_2SO_4.The amount of carbon required to completely deactivate the catalyst was determined using a TGA/FTIR technique.For all of the catalysts synthesized in this study it was found that two active sulfate sites were poisoned by a single deposited carbon atom.Using this information,an active site composed of two coupled sulfate sites,perhaps a surface pyrosulfate site,is suggested.Using a TGA/FTIR technique it was found that the number of catalytically active sulfate sites never exceeded 14% of the total sulfate loading.These results were also supported by calorimetric studies.
机译:研究了硫酸化氧化锆催化剂上的硫载量与H_2SO_4浓度的关系。以正丁烷为反应探针在200℃下异构化测试了催化活性。以0.5 N制备的催化剂观察到最佳催化活性H_2SO_4。使用TGA / FTIR技术确定使催化剂完全失活所需的碳量。对于本研究中合成的所有催化剂,发现两个活性硫酸盐位点被单个沉积的碳原子毒化。建议使用一个由两个偶合硫酸盐位点组成的活性位点,也许是一个表面焦硫酸盐位点。使用TGA / FTIR技术发现,催化活性硫酸盐位点的数量从未超过总硫酸盐负荷的14%。量热研究也支持。

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