中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
Concentration fluctuation caused by reaction-diffusion coupling near catalytic active sites

文献类型:期刊论文

作者Zhang, Haolei1,2; Zhao, Mingcan1; Li, Yanping1; Li, Chengxiang1,3; Ge, Wei1,2,4
刊名CHINESE JOURNAL OF CHEMICAL ENGINEERING
出版日期2022-10-01
卷号50页码:254-263
ISSN号1004-9541
关键词Molecular dynamics simulation Concentration fluctuation Reaction-diffusion coupling Catalyst
DOI10.1016/j.cjche.2022.06.023
英文摘要The coupling of reaction and diffusion between neighboring active sites in the catalyst pore leads to the spatiotemporal fluctuation in component concentration, which is very important to catalyst performance and hence its optimal design. Molecular dynamics simulation with hard-sphere and pseudo-particle modeling has previously revealed the non-stochastic concentration fluctuation of the reactant/product near isolated active site due to such coupling, using a simple model reaction of A -> B in 2D pores. The topic is further developed in this work by studying the concentration fluctuation due to such coupling between neighboring active sites in 3D pores. Two 3D pore models containing an isolated active site and two adjacent active sites were constructed, respectively. For the isolated site, the concentration fluctuation intensifies for larger pores, but the product yield decreases, and for a given pore size, the product yield reaches a peak at a certain reactant concentration. For two neighboring sites, their distance (d) is found to have little effect on the reaction, but significant to the diffusion. For the same reaction competing at both sites, larger d leads to more efficient diffusion and better overall performance. However, for sequential reactions at the two sites, higher overall performance presents at a smaller d. The results should be helpful to the catalyst design and reaction control in the relevant processes. (C) 2022 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.
WOS关键词SKELETAL ISOMERIZATION ; SIMULATION ; CONVERSION ; PORE ; 1-BUTENE ; 2-BUTENE ; H-ZSM-5 ; BIOMASS ; OLEFINS
资助项目National Natural Science Foundation of China[92034302] ; National Natural Science Foundation of China[22178347] ; Dalian National Laboratory for Clean Energy (DNL) Cooperation Fund, the Chinese Academy of Sciences[DNL201905] ; "Transformational Technologies for Clean Energy and Demonstration", Strategic Priority Research Program of the Chinese Academy of Sciences[XDA21030700] ; National Science and Technology Major Project[2017-I-0004-0005]
WOS研究方向Engineering
语种英语
出版者CHEMICAL INDUSTRY PRESS CO LTD
WOS记录号WOS:000907280600002
资助机构National Natural Science Foundation of China ; Dalian National Laboratory for Clean Energy (DNL) Cooperation Fund, the Chinese Academy of Sciences ; "Transformational Technologies for Clean Energy and Demonstration", Strategic Priority Research Program of the Chinese Academy of Sciences ; National Science and Technology Major Project
源URL[http://ir.ipe.ac.cn/handle/122111/56452]  
专题中国科学院过程工程研究所
通讯作者Li, Chengxiang; Ge, Wei
作者单位1.Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
2.Univ Chinese Acad Sci, Sch Chem Engn, Beijing 100049, Peoples R China
3.Chinese Acad Sci, Dalian Natl Lab Clean Energy, Dalian 116023, Liaoning, Peoples R China
4.Chinese Acad Sci, Innovat Acad Green Mfg, Beijing 100049, Peoples R China
推荐引用方式
GB/T 7714
Zhang, Haolei,Zhao, Mingcan,Li, Yanping,et al. Concentration fluctuation caused by reaction-diffusion coupling near catalytic active sites[J]. CHINESE JOURNAL OF CHEMICAL ENGINEERING,2022,50:254-263.
APA Zhang, Haolei,Zhao, Mingcan,Li, Yanping,Li, Chengxiang,&Ge, Wei.(2022).Concentration fluctuation caused by reaction-diffusion coupling near catalytic active sites.CHINESE JOURNAL OF CHEMICAL ENGINEERING,50,254-263.
MLA Zhang, Haolei,et al."Concentration fluctuation caused by reaction-diffusion coupling near catalytic active sites".CHINESE JOURNAL OF CHEMICAL ENGINEERING 50(2022):254-263.

入库方式: OAI收割

来源:过程工程研究所

浏览0
下载0
收藏0
其他版本

除非特别说明,本系统中所有内容都受版权保护,并保留所有权利。