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Methanol Formation in the Water Gas Shift Reactionover Copper-Containing Catalysts

机译:含铜催化剂在水煤气变换反应中甲醇的生成

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摘要

In ammonia and hydrogen production, methanol formation takes place mainly at the low-tem - perature (second) WGS stage, where the gas composition, catalysts, and operating conditions are similar to those in methanol synthesis. The methanol formation reaction consumes hydrogen, an expensive gas, and causes a number of technological and environmental problems. This raises the problem of reducing the meth-anol formation rate. To do this, it is necessary to analyze the kinetics, thermodynamics, and technological features of methanol formation at the low-temperature shift stage. Here, we report the equilibrium methanol concentrations calculated for CO conversion under near-industrial conditions. Systematizing the relevant experimental data available from the literature, we demonstrate how methanol formation depends on WGS conditions. The methanol formation rate can be reduced by lowering the CO concentration in the feed gas and employing low-methanol catalysts. Another favorable factor for methanol reduction is the aging of the catalyst during its operation.
机译:在氨气和氢气生产中,甲醇的形成主要发生在低温(第二)WGS阶段,该阶段的气体组成,催化剂和操作条件与甲醇合成中的相似。甲醇形成反应消耗氢,昂贵的气体,并引起许多技术和环境问题。这就产生了降低甲醇生成速率的问题。为此,有必要分析低温转化阶段甲醇形成的动力学,热力学和技术特征。在这里,我们报告了在接近工业条件下计算出的用于CO转化的平衡甲醇浓度。系统化从文献中获得的相关实验数据,我们证明了甲醇的形成如何取决于WGS条件。可以通过降低进料气中的CO浓度并使用低甲醇催化剂来降低甲醇形成速率。甲醇还原的另一个有利因素是催化剂在其操作过程中的老化。

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