催化作用
煅烧
化学
反应速率
多相催化
化学反应工程
化学反应
反应速率常数
反应机理
表面反应
化学动力学
化学工程
物理化学
动力学
有机化学
物理
量子力学
工程类
作者
Paweł Bernard,Paweł Stelmachowski,P. Broś,Wacław Makowski,Andrzej Kotarba
标识
DOI:10.1021/acs.jchemed.0c01101
摘要
Heterogeneous catalysis plays an important role in many chemical reactions, especially those applied in industrial processes, and therefore, its theoretical foundations are introduced not only to students majoring in chemical engineering or catalysis but also as part of general chemistry courses. The consideration of catalytic activity of various solids and mechanisms of catalytic reactions requires the introduction of the concept of an active site, which together with the catalyst specific surface area are discussed as key parameters controlling the reaction rate. There are many known demonstrations of heterogeneous catalysis phenomena that can be performed live in a lecture hall, but all of them focus only on the general idea of catalytic processes and are not suitable for quantitative analysis. Therefore, herein we present a simple demonstration of the influence of the specific surface area of a catalyst on the rate of a catalytic reaction. This demonstration is based on a model reaction of hydrogen peroxide decomposition catalyzed by cobalt spinel (Co3O4) calcined at various temperatures. The differences in reaction rates can be monitored visually, and the obtained data can be used directly for a simple kinetic analysis, including comparison of numerical values of the reaction rate constants.
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