{"title":"计算催化的重大挑战","authors":"F. Studt","doi":"10.3389/fctls.2021.658965","DOIUrl":null,"url":null,"abstract":"Catalysis is a cornerstone of modern societies as over 90% of processes in the chemical industry are facilitated by catalysts, with the majority requiring a homogeneous or heterogeneous catalyst (Hagen, 2015). Future renewable energy scenarios also rely heavily on the utilization of electro-catalysts, e.g., for the production of clean hydrogen. This shift towards new feedstocks and benign processes entails the development of new generations of catalysts. While the discovery of catalysts has often relied on trial and error in the first half of the last century, the establishment of (design) rules has significantly improved the speed with which new catalysts are being discovered. To this end, the knowledge-based improvement and design of new catalysts is increasingly supported by quantum chemical calculations of reaction mechanisms and kinetic modeling of corresponding reaction rates. In fact, first examples of catalyst design by means of computational screening have already emerged (Nørskov et al., 2009; Medford et al., 2015; Zhao et al., 2019). The extent to which computational modeling becomes a dominant factor in the catalysis community in the 21st century depends crucially on the accuracy with which predictions can be made, but also on the development of a reductionist approach, where the main contributing factors to the performance of a given class of catalysts are reduced to a few selected key parameters that can be used efficiently for computational screening. Perhaps the most challenging issue in computational catalysis is the fact that the rate constant of a reaction step changes drastically with minor changes of the reaction barrier (e.g., for a reaction occurring at 500 K by a factor of about 120 for typical errors of ±20 kJ/mol, or a factor of approximately 3 for an error ±5 kJ/mol, that is commonly referred to as chemical accuracy) and that only approximate methods are computationally feasible for the calculation of enthalpy and entropy contributions of a transition states free energy as the catalytic systems are often large and complex. In all fields discussed here (homogeneous, heterogeneous and electro-catalysis) density functional theory (DFT) has become the workhorse of computational studies as it exhibits the best compromise between accuracy and computational cost. In homogeneous catalysis for example, the enthalpy related to the active site of a transition-metal complex can be determined quite accurately with advanced hybrid functionals (Jiang et al., 2012). However, homogeneous catalysts often exhibit large ligands raising the issue of conformational complexity that is difficult to model. This is often getting even more problematic with solvation and leads to difficulties in determining the active conformational space and corresponding enthalpy and particularly entropy contributions to the free energy (Harvey et al., 2019). A balanced description of interand intramolecular interactions during solvation is similarly challenging (Schmidt et al., 2013). In large parts of heterogeneous catalysis (e.g., supported transition metals) one needs to approximate the active site with a simple extended periodic surface model, that usually omits the effect of particle size and shape as well as particle-support interactions. 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The extent to which computational modeling becomes a dominant factor in the catalysis community in the 21st century depends crucially on the accuracy with which predictions can be made, but also on the development of a reductionist approach, where the main contributing factors to the performance of a given class of catalysts are reduced to a few selected key parameters that can be used efficiently for computational screening. 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引用次数: 16
摘要
催化是现代社会的基石,因为化学工业中超过90%的过程都是由催化剂促进的,其中大多数需要均相或非均相催化剂(Hagen, 2015)。未来的可再生能源方案也严重依赖于电催化剂的利用,例如用于生产清洁氢。这种向新原料和良性工艺的转变需要开发新一代催化剂。虽然在上个世纪上半叶,催化剂的发现往往依赖于试验和错误,但(设计)规则的建立大大提高了发现新催化剂的速度。为此,基于知识的新型催化剂的改进和设计越来越多地得到反应机理的量子化学计算和相应反应速率的动力学建模的支持。事实上,通过计算筛选来设计催化剂的第一个例子已经出现(Nørskov et al., 2009;Medford et al., 2015;Zhao et al., 2019)。计算建模在21世纪成为催化界的主导因素的程度主要取决于预测的准确性,但也取决于还原论方法的发展,在这种方法中,对特定类型催化剂性能的主要影响因素被简化为几个选定的关键参数,这些参数可以有效地用于计算筛选。也许计算催化中最具挑战性的问题是,反应阶跃的速率常数随着反应势垒的微小变化而急剧变化(例如,对于发生在500 K下的反应,典型误差为±20 kJ/mol时,速率常数约为120倍,误差为±5 kJ/mol时,速率常数约为3倍)。这通常被称为化学精度),并且只有近似的方法在计算过渡态自由能的焓和熵贡献时是可行的,因为催化系统通常是大而复杂的。在这里讨论的所有领域(均相、多相和电催化)中,密度泛函理论(DFT)已经成为计算研究的主要方法,因为它展示了精度和计算成本之间的最佳折衷。例如,在均相催化中,使用先进的杂化官能团可以相当准确地确定与过渡金属配合物活性位点相关的焓(Jiang etal ., 2012)。然而,均相催化剂通常表现出大配体,引起难以建模的构象复杂性问题。这在溶剂化过程中往往会变得更加成问题,并导致难以确定活性构象空间和相应的焓,特别是熵对自由能的贡献(Harvey et al., 2019)。在溶剂化过程中平衡描述分子间和分子内相互作用同样具有挑战性(Schmidt et al., 2013)。在大部分非均相催化(例如,负载过渡金属)中,需要用简单的扩展周期表面模型来近似活性位点,该模型通常忽略了颗粒大小和形状以及颗粒-支撑相互作用的影响。此外,使用广义梯度近似(GGA)的泛函通常是唯一适用的选择,最佳泛函的吸附能误差为±20 kJ/mol (Wellendorff等人,2015)。编辑和审查:Frank Hollmann,代尔夫特理工大学,荷兰
Catalysis is a cornerstone of modern societies as over 90% of processes in the chemical industry are facilitated by catalysts, with the majority requiring a homogeneous or heterogeneous catalyst (Hagen, 2015). Future renewable energy scenarios also rely heavily on the utilization of electro-catalysts, e.g., for the production of clean hydrogen. This shift towards new feedstocks and benign processes entails the development of new generations of catalysts. While the discovery of catalysts has often relied on trial and error in the first half of the last century, the establishment of (design) rules has significantly improved the speed with which new catalysts are being discovered. To this end, the knowledge-based improvement and design of new catalysts is increasingly supported by quantum chemical calculations of reaction mechanisms and kinetic modeling of corresponding reaction rates. In fact, first examples of catalyst design by means of computational screening have already emerged (Nørskov et al., 2009; Medford et al., 2015; Zhao et al., 2019). The extent to which computational modeling becomes a dominant factor in the catalysis community in the 21st century depends crucially on the accuracy with which predictions can be made, but also on the development of a reductionist approach, where the main contributing factors to the performance of a given class of catalysts are reduced to a few selected key parameters that can be used efficiently for computational screening. Perhaps the most challenging issue in computational catalysis is the fact that the rate constant of a reaction step changes drastically with minor changes of the reaction barrier (e.g., for a reaction occurring at 500 K by a factor of about 120 for typical errors of ±20 kJ/mol, or a factor of approximately 3 for an error ±5 kJ/mol, that is commonly referred to as chemical accuracy) and that only approximate methods are computationally feasible for the calculation of enthalpy and entropy contributions of a transition states free energy as the catalytic systems are often large and complex. In all fields discussed here (homogeneous, heterogeneous and electro-catalysis) density functional theory (DFT) has become the workhorse of computational studies as it exhibits the best compromise between accuracy and computational cost. In homogeneous catalysis for example, the enthalpy related to the active site of a transition-metal complex can be determined quite accurately with advanced hybrid functionals (Jiang et al., 2012). However, homogeneous catalysts often exhibit large ligands raising the issue of conformational complexity that is difficult to model. This is often getting even more problematic with solvation and leads to difficulties in determining the active conformational space and corresponding enthalpy and particularly entropy contributions to the free energy (Harvey et al., 2019). A balanced description of interand intramolecular interactions during solvation is similarly challenging (Schmidt et al., 2013). In large parts of heterogeneous catalysis (e.g., supported transition metals) one needs to approximate the active site with a simple extended periodic surface model, that usually omits the effect of particle size and shape as well as particle-support interactions. Moreover, functionals using the generalized gradient approximation (GGA) are typically the only applicable choice, with the best functionals having errors of ±20 kJ/mol for adsorption energies (Wellendorff et al., 2015) Edited and reviewed by: Frank Hollmann, Delft University of Technology, Netherlands