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A study of the electrochemical hydrogenation of o-xylene in a PEM hydrogenation reactor

机译:PEM加氢反应器中邻二甲苯的电化学加氢研究

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In this study, we investigate the electrochemical hydrogenation of o-xylene in a proton exchange membrane hydrogenation reactor (PEMHR). The reactor was operated isothermally over the temperature range 20-68℃ and at a pressure of 1 atm in a semi-batch mode. Hydrogen was fed into the anode compartment and o-xylene into the cathode. The hydrogenation efficiency was investigated at different current densities and temperatures. Results obtained show that the hydrogenation efficiency increases with temperature but decreases with current density. At low current densities the hydrogenation efficiency approaches 100%. A zero dimensional model was used to fit the data and extract a rate constant for the hydrogenation reaction. The activation energy for this reaction was found to be 28 kJ/mole.
机译:在这项研究中,我们研究了质子交换膜加氢反应器(PEMHR)中邻二甲苯的电化学加氢。反应器在20-68℃的温度范围内等温运行,并在1atm的压力下以半间歇方式运行。将氢进料到阳极室中,将邻二甲苯进料到阴极中。在不同的电流密度和温度下研究了氢化效率。所得结果表明,氢化效率随温度增加而随电流密度下降。在低电流密度下,氢化效率接近100%。使用零维模型拟合数据并提取氢化反应的速率常数。发现该反应的活化能为28kJ /摩尔。

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