{"title":"An experimental study of pressure drop characteristics under single-phase flow through packed bed microreactors","authors":"Lu Zhang, Arne Hommes, Remon Schuring, Jun Yue","doi":"10.1002/aic.18640","DOIUrl":null,"url":null,"abstract":"Packed bed microreactors offer a promising platform for intensifying heterogeneously catalyzed reactions. To understand hydrodynamics therein, N<sub>2</sub> or water flow was investigated experimentally through microreactors packed with glass beads in this work, corresponding to a microreactor to particle diameter ratio (<i>D</i>/<i>d</i>) of 1.29–25.12. The porosity of a single pellet string microreactor (<i>D</i>/<i>d</i> < 1.866) agrees with the literature's theoretical equation. For microreactors with larger <i>D</i>/<i>d</i> ratios, an empirical porosity correlation is proposed to address the dense packing nature of the bed. The existing correlations are inadequate to describe the pressure drop data in microreactors within the entire <i>D</i>/<i>d</i> ratios and modified Reynolds numbers (<i>Re</i><sub><i>m</i></sub> < 291). At <i>D</i>/<i>d</i> ≥ 3, the measured pressure drop is described by the modified Ergun equation using properties of the bulk bed zone to exclude the wall effect. At <i>D</i>/<i>d</i> < 3, it can be predicted by introducing a correction term for the wall effect into the Ergun equation.","PeriodicalId":120,"journal":{"name":"AIChE Journal","volume":"237 1","pages":""},"PeriodicalIF":3.5000,"publicationDate":"2024-11-20","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"AIChE Journal","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1002/aic.18640","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
Packed bed microreactors offer a promising platform for intensifying heterogeneously catalyzed reactions. To understand hydrodynamics therein, N2 or water flow was investigated experimentally through microreactors packed with glass beads in this work, corresponding to a microreactor to particle diameter ratio (D/d) of 1.29–25.12. The porosity of a single pellet string microreactor (D/d < 1.866) agrees with the literature's theoretical equation. For microreactors with larger D/d ratios, an empirical porosity correlation is proposed to address the dense packing nature of the bed. The existing correlations are inadequate to describe the pressure drop data in microreactors within the entire D/d ratios and modified Reynolds numbers (Rem < 291). At D/d ≥ 3, the measured pressure drop is described by the modified Ergun equation using properties of the bulk bed zone to exclude the wall effect. At D/d < 3, it can be predicted by introducing a correction term for the wall effect into the Ergun equation.
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