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Deducing kinetic constants for the hydrodechlorination of 4-chlorophenol using high adsorption capacity catalysts

机译:使用高吸附容量催化剂推导4-氯苯酚加氢脱氯的动力学常数

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摘要

Employing high surface area supports for catalytic hydrodechlorination can result in pronounced adsorption of reactants, intermediates and products. The influence of these sorption processes on the activity and selectivity upon 4-chlorophenol (4-CP) hydrodechlorination in aqueous solution has been studied using four commercial Pd/Al2O3 and Pd/AC catalysts at ambient pressure within the temperature range of 20-40°C ([4-CP]0=0.78-2.90mmolL-1, [catalyst]=1gL-1, 50NmLH2min-1). The adsorption capacity of the catalysts was independently evaluated. The Al2O3-based catalyst did not show any significant adsorption of those species whereas the activated carbon materials presented in all cases high uptakes (e.g. up to 2.4mmol4-CPgcat -1). In order to deduce true kinetic constants also for these catalysts, a kinetic model was developed, which accounts for the consecutive reaction and sorption processes in parallel. This expanded model resulted in a reasonable fit, can thus be used for comparison of different catalysts regardless their sorption capacity and allows predicting successfully the selectivity to the reaction products
机译:使用高表面积的载体进行催化加氢脱氯可导致反应物,中间体和产物的明显吸附。在环境压力为20-40°C的条件下,使用四种市售Pd / Al2O3和Pd / AC催化剂研究了这些吸附过程对水溶液中4-氯苯酚(4-CP)加氢脱氯的活性和选择性的影响。 C([4-CP] 0 = 0.78-2.90mmolL-1,[催化剂] = 1gL-1,50NmLH2min-1)。独立评估催化剂的吸附能力。基于Al 2 O 3的催化剂没有显示出那些物质的任何显着吸附,而在所有情况下,活性炭材料均呈现高吸收(例如,高达2.4mmol4-CPgcat -1)。为了也推导这些催化剂的真实动力学常数,开发了动力学模型,该模型考虑了平行的连续反应和吸附过程。该扩展模型可得出合理的拟合值,因此无论吸附能力如何均可用于比较不同的催化剂,并可以成功预测对反应产物的选择性

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