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Selective hydrogenation of acetylene through a short contact time reactor

机译:通过短接触时间反应器对乙炔进行选择性加氢

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摘要

A novel approach to the selective hydrogenation of acetylene involves a short contact time rector.A thin Pd/#gamma#-Al_2O_3 catalytic membrane (about 5 #mu#m thick) was observed to be void of minor defects.Forcing a dilute C_2H_2/H_2/Ar mixture through the layer produced high conversions coupled with high selectivity at high temperatures.The selectivity was observed to increase with temperature.A gas-dispersion model with derived kinetics was employed to explain the results.A solution to the corresponding coupled nonlinear differential equations resulted in a Peclet number of 64.5 and a contact time of 9.5 X 10~(-3) s through the reactor at 100 deg C.A critical thickness is predicted to exist for a maximum in ethylene concentration.A critical thickness is predicted to exist for a maximum in ethylene concentration.A value of 2.5#mu#m at 200 deg C is representative.Lastly,permeability experiments agree with modeling results to show that Knudsen diffusio is absent despite a narrow pore-size distribution.
机译:一种新型的乙炔选择性加氢方法涉及较短的接触时间反应器,观察到薄的Pd /#gamma#-Al_2O_3催化膜(约5#μ#m厚)没有小缺陷,迫使稀C_2H_2 /穿过该层的H_2 / Ar混合物在高温下产生高转化率并具有高选择性,观察到选择性随温度增加而增加,采用具有导出动力学的气体扩散模型来解释结果。相应的耦合非线性微分的解方程得出Peclet数为64.5,在100摄氏度CA下,通过反应器的接触时间为9.5 X 10〜(-3)s,对于乙烯浓度的最大值,存在临界厚度。最高的乙烯浓度。在200℃时的典型值为2.5#μm。最后,渗透率实验与模拟结果吻合,表明尽管孔壁狭窄,但没有Knudsen扩散。 ze分布。

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