化学
催化作用
甲醇
动力学
动能
差速器(机械装置)
化学工程
物理化学
无机化学
热力学
有机化学
物理
量子力学
工程类
作者
Saman Khawaja,Muhammad R. Usman
摘要
Abstract The experimental data over CuO/ZnO/ZrO 2 catalyst for a wide range of operating conditions were used to develop the kinetics of the reaction CO 2 hydrogenation to methanol. Three kinetic models such as the power law model, the Graaf kinetic model, and the Park kinetic model were tested against the experimental data. Both the mechanistic models have been developed based on the Langmuir‐Hinshelwood‐Hougen‐Watson approach and are specific only to the methanol synthesis from CO/CO 2 hydrogenation. In an attempt to reduce the number of parameters in the two models, the abridged forms of these models were also tried. Overall, 25 kinetic rate equations were tested and the best‐fit kinetic rate expression with optimized parameters was worked out. Both the integral and differential methods of kinetic analysis were employed and their efficacy in finding the best‐fit expression was compared. The MATLAB built‐in function fminsearch was employed to perform the regression of the data. The Graaf model in its parent form, but with the new optimized values of the parameters, was found to be the best‐fit rate model. The Graaf kinetics, with re‐estimated parameters, could be helpful in designing and simulating a methanol synthesis reactor operating on CO 2 and H 2 feed and utilizing a CuO/ZnO/ZrO 2 catalyst.
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