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Kinetic Investigation on Selective CO2 Hydrogenation to Formic Acid over Rhodium Hydrotalcite (Rh-HT) Catalyst
Kinetics and Catalysis ( IF 1.1 ) Pub Date : 2023-06-23 , DOI: 10.1134/s0023158423030060
Minaxi S. Maru , Sanwala Ram , Ram S. Shukla

Abstract

A heterogeneous catalyst, rhodium hydrotalcite (Rh-HT), was synthesized, characterized, and explored for kinetic studies for the hydrogenation of CO2 to formic acid using molecular hydrogen in an autoclave. The catalyst was efficient for the selective formation of formic acid at a moderate temperature with up to 5 catalytic cycles without any significant loss in catalytic activity. The detailed kinetic investigations were performed by determining the rate of formic acid formation as a function of time, catalyst amount, total pressure, partial pressure of CO2, partial pressure of H2, reaction volume, v/v ratio of the mixed solvent of methanol and water, agitation speed, and temperature in a wide range of variation. The rates were found to be dependent on all these parameters. The formic acid formation rate followed the first-order kinetics with respect to the partial pressures of CO2 and H2, and catalyst amount. The best reaction conditions obtained from the kinetic parametric optimisation were, 50 bar total pressure (1/1 p/p, CO2 and H2); 60°C temperature; a mixture of methanol:water solvent (5/1 v/v, 60 mL); 24 h time; and 500 rpm agitation speed to get a TON of 15840 for formic acid with no additional base. The thermodynamic performance of the heterogeneous catalyst Rh-HT was appreciably associated with highly negative entropy. The performance of the catalyst was effectively enhanced by the mixture of water and methanol as a solvent. The mechanistic routes for CO2 hydrogenation to formic acid are proposed and discussed based on the kinetic and experimental observations involving the role of the molecular effect of water used in the solvent.



中文翻译:

铑水滑石 (Rh-HT) 催化剂选择性 CO2 加氢制甲酸的动力学研究

摘要

合成、表征了一种非均相催化剂铑水滑石(Rh-HT),并探索了在高压釜中使用分子氢将CO 2加氢为甲酸的动力学研究。该催化剂可在中等温度下有效选择性地形成甲酸,最多可进行 5 次催化循环,而催化活性没有任何显着损失。通过确定作为时间、催化剂量、总压、CO 2 分压、H 2 分压的函数的甲酸形成速率来进行详细的动力学研究。、反应体积、甲醇和水混合溶剂的v/v比、搅拌速度和温度在宽范围内变化。发现速率取决于所有这些参数。甲酸形成速率遵循关于CO 2和H 2分压以及催化剂量的一级动力学。动力学参数优化得到的最佳反应条件为,50 bar总压(1/1 p/p,CO 2和H 2);60℃温度;甲醇:水溶剂的混合物(5/1 v/v,60 mL);24小时时间;和 500 rpm 搅拌速度,在没有额外碱的情况下得到 15840 的甲酸 TON。多相催化剂 Rh-HT 的热力学性能与高负熵显着相关。水和甲醇的混合物作为溶剂有效提高了催化剂的性能。基于涉及溶剂中水的分子效应的动力学和实验观察,提出并讨论了CO 2加氢生成甲酸的机理路线。

更新日期:2023-06-24
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