Marsden Grant, Kostetskyy Pavlo, Sekiya Ryoh-Suke, Hoffman Alexander, Lee Songhyun, Gounder Rajamani, Hibbitts David, Broadbelt Linda J
Department of Chemical and Biological Engineering, Northwestern University, 2145 Sheridan Road, Evanston, Illinois 60208, United States.
Department of Chemical Engineering, University of Florida, 1030 Center, Drive P.O. Box 116005, Gainesville, Florida 32611, United States.
ACS Mater Au. 2021 Dec 13;2(2):163-175. doi: 10.1021/acsmaterialsau.1c00057. eCollection 2022 Mar 9.
Control of the spatial proximity of Brønsted acid sites within the zeolite framework can result in materials with properties that are distinct from materials synthesized through conventional crystallization methods or available from commercial sources. Recent experimental evidence has shown that turnover rates of different acid-catalyzed reactions increase with the fraction of proximal sites in chabazite (CHA) zeolites. The catalytic conversion of oxygenates is an important research area, and the dehydration of methanol to dimethyl ether (DME) is a well-studied reaction as part of methanol-to-olefin chemistry catalyzed by solid acids. Published experimental data have shown that DME formation rates (per acid site) increase systematically with the fraction of proximal acid sites in the six-membered ring of CHA. Here, we probe the effect of acid site proximity in CHA on methanol dehydration rates using electronic structure calculations and microkinetic modeling to identify the primary causes of this chemistry and their relationship to the local structure of the catalyst at the nanoscale. We report a density functional theory-parametrized microkinetic model of methanol dehydration to DME, catalyzed by acidic CHA zeolite with direct comparison to experimental data. Effects of proximal acid sites on reaction rates were captured quantitatively for a range of operating conditions and catalyst compositions, with a focus on total paired acid site concentration and reactant clustering to form higher nuclearity complexes. Next-nearest neighbor paired acid sites were identified as promoting the formation of methanol trimer clusters rather than the inhibiting tetramer or pentamer clusters, resulting in large increases in the rate for DME production due to the lower energy barriers present in the concerted methanol trimer reaction pathway. The model framework developed in this study can be extended to other zeolite materials and reaction chemistries toward the goal of rational design and development of next-generation catalytic materials and chemical processes.
控制沸石骨架内布朗斯台德酸位点的空间接近度可得到具有与通过传统结晶方法合成的材料或市售材料不同性质的材料。最近的实验证据表明,不同酸催化反应的转化率随菱沸石(CHA)沸石中近端位点的比例增加而提高。含氧化合物的催化转化是一个重要的研究领域,甲醇脱水制二甲醚(DME)作为固体酸催化的甲醇制烯烃化学的一部分,是一个经过充分研究的反应。已发表的实验数据表明,CHA六元环中DME的生成速率(每酸位点)随近端酸位点的比例而系统增加。在这里,我们使用电子结构计算和微观动力学模型来探究CHA中酸位点接近度对甲醇脱水速率的影响,以确定这种化学过程的主要原因及其与纳米级催化剂局部结构的关系。我们报告了由酸性CHA沸石催化甲醇脱水制DME的密度泛函理论参数化微观动力学模型,并与实验数据进行了直接比较。在一系列操作条件和催化剂组成下,定量地捕捉了近端酸位点对反应速率的影响,重点关注总配对酸位点浓度和反应物聚集形成更高核数的络合物。次近邻配对酸位点被确定为促进甲醇三聚体簇的形成,而不是抑制四聚体或五聚体簇,由于协同甲醇三聚体反应途径中存在较低的能垒,导致DME生成速率大幅增加。本研究中开发的模型框架可扩展到其他沸石材料和反应化学,以实现下一代催化材料和化学过程的合理设计与开发。