Juncheng Hao, Shaofu Du, Yuchao Niu, Shaoqin Yin, Xuehua Ruan, Xiaoming Yan, Xiangcun Li, Gaohong He and Xiaobin Jiang*,
{"title":"Simulation-Based Hollow Fiber Membrane Module Design for Membrane-Assisted Antisolvent Crystallization","authors":"Juncheng Hao, Shaofu Du, Yuchao Niu, Shaoqin Yin, Xuehua Ruan, Xiaoming Yan, Xiangcun Li, Gaohong He and Xiaobin Jiang*, ","doi":"10.1021/acs.iecr.5c00690","DOIUrl":null,"url":null,"abstract":"<p >Membrane-assisted antisolvent crystallization (MAAC) is an innovative separation process that enables precise control of crystal morphology. The membrane packing density of the membrane module directly affects the crystallization solution mixing behavior and influences crystal morphology. Herein, through an integrated approach combining Computational Fluid Dynamics (CFD) simulations and MAAC experimental validation, this study systematically analyzes the fluid mixing behavior within membrane modules and the resulting crystal products under varying membrane packing densities. The experimental results demonstrate that, compared to the other two membrane modules with packing densities of 42.60 and 383.40 m<sup>2</sup>/m<sup>3</sup>, the optimally packed module (170.42 m<sup>2</sup>/m<sup>3</sup>) produces crystals with both larger particle sizes (>75 μm) and narrower size distribution (C.V. < 40%) across a broader range of shell side flow rates (36–60 mL/min). This study provides a potential tool to guide the design and optimization of membrane modules for the MAAC process.</p>","PeriodicalId":39,"journal":{"name":"Industrial & Engineering Chemistry Research","volume":"64 26","pages":"13397–13409"},"PeriodicalIF":3.9000,"publicationDate":"2025-06-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Industrial & Engineering Chemistry Research","FirstCategoryId":"5","ListUrlMain":"https://pubs.acs.org/doi/10.1021/acs.iecr.5c00690","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
Abstract
Membrane-assisted antisolvent crystallization (MAAC) is an innovative separation process that enables precise control of crystal morphology. The membrane packing density of the membrane module directly affects the crystallization solution mixing behavior and influences crystal morphology. Herein, through an integrated approach combining Computational Fluid Dynamics (CFD) simulations and MAAC experimental validation, this study systematically analyzes the fluid mixing behavior within membrane modules and the resulting crystal products under varying membrane packing densities. The experimental results demonstrate that, compared to the other two membrane modules with packing densities of 42.60 and 383.40 m2/m3, the optimally packed module (170.42 m2/m3) produces crystals with both larger particle sizes (>75 μm) and narrower size distribution (C.V. < 40%) across a broader range of shell side flow rates (36–60 mL/min). This study provides a potential tool to guide the design and optimization of membrane modules for the MAAC process.
期刊介绍:
ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.