{"title":"CFD modeling of gas–solid flow in a two-stage jetting fluidized bed with an overflow standpipe","authors":"Zhengyu Wang, Teng Wang, Meiyu Zhou, Luhaibo Zhao","doi":"10.1002/apj.3163","DOIUrl":null,"url":null,"abstract":"<p>The two-fluid model–kinetic theory of granular flow (TFM–KTGF) model and the sub-grid-scale (SGS) model are used to conduct a three-dimensional numerical simulation study on the hydrodynamic characteristics of a two-stage fluidized bed with an integrated overflow pipe. Using various drag models, the gas–solid flows, bed expansions, pressure drop distributions, and equilibrium conditions in the two-stage bed are compared, and the conditions for the formation of a stable overflow in the two-stage bed are thoroughly investigated. In addition, during the simulation of the secondary distribution in the bed, the porous media model simulates the momentum loss caused by the redistribution plate to avoid the direct simulation of the redistribution plate, which requires extensive grid division work and calculation costs. This work can provide technical direction for the industrialization of one-step coal to multistage fluidized bed natural gas technology.</p>","PeriodicalId":49237,"journal":{"name":"Asia-Pacific Journal of Chemical Engineering","volume":"20 1","pages":""},"PeriodicalIF":1.4000,"publicationDate":"2024-09-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Asia-Pacific Journal of Chemical Engineering","FirstCategoryId":"5","ListUrlMain":"https://onlinelibrary.wiley.com/doi/10.1002/apj.3163","RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
CFD modeling of gas–solid flow in a two-stage jetting fluidized bed with an overflow standpipe
The two-fluid model–kinetic theory of granular flow (TFM–KTGF) model and the sub-grid-scale (SGS) model are used to conduct a three-dimensional numerical simulation study on the hydrodynamic characteristics of a two-stage fluidized bed with an integrated overflow pipe. Using various drag models, the gas–solid flows, bed expansions, pressure drop distributions, and equilibrium conditions in the two-stage bed are compared, and the conditions for the formation of a stable overflow in the two-stage bed are thoroughly investigated. In addition, during the simulation of the secondary distribution in the bed, the porous media model simulates the momentum loss caused by the redistribution plate to avoid the direct simulation of the redistribution plate, which requires extensive grid division work and calculation costs. This work can provide technical direction for the industrialization of one-step coal to multistage fluidized bed natural gas technology.
期刊介绍:
Asia-Pacific Journal of Chemical Engineering is aimed at capturing current developments and initiatives in chemical engineering related and specialised areas. Publishing six issues each year, the journal showcases innovative technological developments, providing an opportunity for technology transfer and collaboration.
Asia-Pacific Journal of Chemical Engineering will focus particular attention on the key areas of: Process Application (separation, polymer, catalysis, nanotechnology, electrochemistry, nuclear technology); Energy and Environmental Technology (materials for energy storage and conversion, coal gasification, gas liquefaction, air pollution control, water treatment, waste utilization and management, nuclear waste remediation); and Biochemical Engineering (including targeted drug delivery applications).