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Comparative analysis on gas–solid drag models in MFIX-DEM simulations of bubbling fluidized bed
[Display omitted] In this study, the open-source software MFIX-DEM simulations of a bubbling fluidized bed (BFB) are applied to assess nine drag models according to experimental and direct numerical simulation (DNS) results. The influence of superficial gas velocity on gas–solid flow is also examine...
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Published in: | Chinese journal of chemical engineering 2023-12, Vol.64 (12), p.64-75 |
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cites | cdi_FETCH-LOGICAL-c333t-ae157541963795b0c1eb2a97351716e773a224c8e22adcdfe93d1cf784cb84f43 |
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container_title | Chinese journal of chemical engineering |
container_volume | 64 |
creator | Li, Ruiyu Huang, Xiaole Wu, Yuhao Dong, Lingxiao Belošević, Srdjan Milićević, Aleksandar Tomanović, Ivan Deng, Lei Che, Defu |
description | [Display omitted]
In this study, the open-source software MFIX-DEM simulations of a bubbling fluidized bed (BFB) are applied to assess nine drag models according to experimental and direct numerical simulation (DNS) results. The influence of superficial gas velocity on gas–solid flow is also examined. The results show that according to the distribution of time-averaged particle axial velocity in y direction, except for Wen–Yu and Tenneti–Garg–Subramaniam (TGS), other drag models are consistent with the experimental and DNS results. For the TGS drag model, the layer-by-layer movement of particles is observed, which indicates the particle velocity is not correctly predicted. The time domain and frequency domain analysis results of pressure drop of each drag model are similar. It is recommended to use the drag model derived from DNS or fine grid computational fluid dynamics–discrete element method (CFD-DEM) data first for CFD-DEM simulations. For the investigated BFB, the superficial gas velocity less than 0.9 m·s−1 should be adopted to obtain normal hydrodynamics. |
doi_str_mv | 10.1016/j.cjche.2023.06.002 |
format | article |
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In this study, the open-source software MFIX-DEM simulations of a bubbling fluidized bed (BFB) are applied to assess nine drag models according to experimental and direct numerical simulation (DNS) results. The influence of superficial gas velocity on gas–solid flow is also examined. The results show that according to the distribution of time-averaged particle axial velocity in y direction, except for Wen–Yu and Tenneti–Garg–Subramaniam (TGS), other drag models are consistent with the experimental and DNS results. For the TGS drag model, the layer-by-layer movement of particles is observed, which indicates the particle velocity is not correctly predicted. The time domain and frequency domain analysis results of pressure drop of each drag model are similar. It is recommended to use the drag model derived from DNS or fine grid computational fluid dynamics–discrete element method (CFD-DEM) data first for CFD-DEM simulations. For the investigated BFB, the superficial gas velocity less than 0.9 m·s−1 should be adopted to obtain normal hydrodynamics.</description><identifier>ISSN: 1004-9541</identifier><identifier>EISSN: 2210-321X</identifier><identifier>DOI: 10.1016/j.cjche.2023.06.002</identifier><language>eng</language><publisher>Elsevier B.V</publisher><subject>Bubbling fluidized bed ; Dense flow ; Drag model ; Gas–solid ; MFIX-DEM ; Simulation</subject><ispartof>Chinese journal of chemical engineering, 2023-12, Vol.64 (12), p.64-75</ispartof><rights>2023 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd</rights><rights>Copyright © Wanfang Data Co. Ltd. All Rights Reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c333t-ae157541963795b0c1eb2a97351716e773a224c8e22adcdfe93d1cf784cb84f43</citedby><cites>FETCH-LOGICAL-c333t-ae157541963795b0c1eb2a97351716e773a224c8e22adcdfe93d1cf784cb84f43</cites><orcidid>0000-0001-7573-7224 ; 0000-0003-4615-8789</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Uhttp://www.wanfangdata.com.cn/images/PeriodicalImages/cjce/cjce.jpg</thumbnail><link.rule.ids>314,776,780,27903,27904</link.rule.ids></links><search><creatorcontrib>Li, Ruiyu</creatorcontrib><creatorcontrib>Huang, Xiaole</creatorcontrib><creatorcontrib>Wu, Yuhao</creatorcontrib><creatorcontrib>Dong, Lingxiao</creatorcontrib><creatorcontrib>Belošević, Srdjan</creatorcontrib><creatorcontrib>Milićević, Aleksandar</creatorcontrib><creatorcontrib>Tomanović, Ivan</creatorcontrib><creatorcontrib>Deng, Lei</creatorcontrib><creatorcontrib>Che, Defu</creatorcontrib><title>Comparative analysis on gas–solid drag models in MFIX-DEM simulations of bubbling fluidized bed</title><title>Chinese journal of chemical engineering</title><description>[Display omitted]
In this study, the open-source software MFIX-DEM simulations of a bubbling fluidized bed (BFB) are applied to assess nine drag models according to experimental and direct numerical simulation (DNS) results. The influence of superficial gas velocity on gas–solid flow is also examined. The results show that according to the distribution of time-averaged particle axial velocity in y direction, except for Wen–Yu and Tenneti–Garg–Subramaniam (TGS), other drag models are consistent with the experimental and DNS results. For the TGS drag model, the layer-by-layer movement of particles is observed, which indicates the particle velocity is not correctly predicted. The time domain and frequency domain analysis results of pressure drop of each drag model are similar. It is recommended to use the drag model derived from DNS or fine grid computational fluid dynamics–discrete element method (CFD-DEM) data first for CFD-DEM simulations. For the investigated BFB, the superficial gas velocity less than 0.9 m·s−1 should be adopted to obtain normal hydrodynamics.</description><subject>Bubbling fluidized bed</subject><subject>Dense flow</subject><subject>Drag model</subject><subject>Gas–solid</subject><subject>MFIX-DEM</subject><subject>Simulation</subject><issn>1004-9541</issn><issn>2210-321X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2023</creationdate><recordtype>article</recordtype><recordid>eNp9kLtOwzAUQC0EEqXwBSxeGBP8yHNgQKWFSq1YQOpmOfZNcJTEld0WlYl_4A_5ElzKzHSXc67uPQhdUxJTQrPbNlateoOYEcZjksWEsBM0YoySiDO6OkUjSkgSlWlCz9GF920ASEGLEZIT26-lkxuzAywH2e298dgOuJH--_PL285orJ1scG81dB6bAS9n81X0MF1ib_ptF1Q7BKXG1baqOjM0uO62RpsP0LgCfYnOatl5uPqbY_Q6m75MnqLF8-N8cr-IFOd8E0mgaR7uKzOel2lFFIWKyTLnKc1pBnnOJWOJKoAxqZWuoeSaqjovElUVSZ3wMbo57n2XQy2HRrR268JDXoQ2cChDGSFF4PiRU85676AWa2d66faCEnGoKVrxW1McHEEyEWIF6-5ohQawM-CEVwYGBdo4UBuhrfnX_wEBo38m</recordid><startdate>20231201</startdate><enddate>20231201</enddate><creator>Li, Ruiyu</creator><creator>Huang, Xiaole</creator><creator>Wu, Yuhao</creator><creator>Dong, Lingxiao</creator><creator>Belošević, Srdjan</creator><creator>Milićević, Aleksandar</creator><creator>Tomanović, Ivan</creator><creator>Deng, Lei</creator><creator>Che, Defu</creator><general>Elsevier B.V</general><general>Shunde Institute of Inspection,Guangdong Institute of Special Equipment Inspection and Research,Foshan 528300,China%State Key Laboratory of Multiphase Flow in Power Engineering,School of Energy and Power Engineering,Xi'an Jiaotong University,Xi'an 710049,China%Department of Thermal Engineering and Energy,"VIN?A"Institute of Nuclear Sciences-National Institute of the Republic of Serbia,University of Belgrade,Mike Petrovi?a Alasa 12-14,11351 Vin?a,PO Box 522,11001 Belgrade,Serbia</general><general>State Key Laboratory of Multiphase Flow in Power Engineering,School of Energy and Power Engineering,Xi'an Jiaotong University,Xi'an 710049,China</general><scope>AAYXX</scope><scope>CITATION</scope><scope>2B.</scope><scope>4A8</scope><scope>92I</scope><scope>93N</scope><scope>PSX</scope><scope>TCJ</scope><orcidid>https://orcid.org/0000-0001-7573-7224</orcidid><orcidid>https://orcid.org/0000-0003-4615-8789</orcidid></search><sort><creationdate>20231201</creationdate><title>Comparative analysis on gas–solid drag models in MFIX-DEM simulations of bubbling fluidized bed</title><author>Li, Ruiyu ; Huang, Xiaole ; Wu, Yuhao ; Dong, Lingxiao ; Belošević, Srdjan ; Milićević, Aleksandar ; Tomanović, Ivan ; Deng, Lei ; Che, Defu</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c333t-ae157541963795b0c1eb2a97351716e773a224c8e22adcdfe93d1cf784cb84f43</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2023</creationdate><topic>Bubbling fluidized bed</topic><topic>Dense flow</topic><topic>Drag model</topic><topic>Gas–solid</topic><topic>MFIX-DEM</topic><topic>Simulation</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Li, Ruiyu</creatorcontrib><creatorcontrib>Huang, Xiaole</creatorcontrib><creatorcontrib>Wu, Yuhao</creatorcontrib><creatorcontrib>Dong, Lingxiao</creatorcontrib><creatorcontrib>Belošević, Srdjan</creatorcontrib><creatorcontrib>Milićević, Aleksandar</creatorcontrib><creatorcontrib>Tomanović, Ivan</creatorcontrib><creatorcontrib>Deng, Lei</creatorcontrib><creatorcontrib>Che, Defu</creatorcontrib><collection>CrossRef</collection><collection>Wanfang Data Journals - Hong Kong</collection><collection>WANFANG Data Centre</collection><collection>Wanfang Data Journals</collection><collection>万方数据期刊 - 香港版</collection><collection>China Online Journals (COJ)</collection><collection>China Online Journals (COJ)</collection><jtitle>Chinese journal of chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Li, Ruiyu</au><au>Huang, Xiaole</au><au>Wu, Yuhao</au><au>Dong, Lingxiao</au><au>Belošević, Srdjan</au><au>Milićević, Aleksandar</au><au>Tomanović, Ivan</au><au>Deng, Lei</au><au>Che, Defu</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Comparative analysis on gas–solid drag models in MFIX-DEM simulations of bubbling fluidized bed</atitle><jtitle>Chinese journal of chemical engineering</jtitle><date>2023-12-01</date><risdate>2023</risdate><volume>64</volume><issue>12</issue><spage>64</spage><epage>75</epage><pages>64-75</pages><issn>1004-9541</issn><eissn>2210-321X</eissn><abstract>[Display omitted]
In this study, the open-source software MFIX-DEM simulations of a bubbling fluidized bed (BFB) are applied to assess nine drag models according to experimental and direct numerical simulation (DNS) results. The influence of superficial gas velocity on gas–solid flow is also examined. The results show that according to the distribution of time-averaged particle axial velocity in y direction, except for Wen–Yu and Tenneti–Garg–Subramaniam (TGS), other drag models are consistent with the experimental and DNS results. For the TGS drag model, the layer-by-layer movement of particles is observed, which indicates the particle velocity is not correctly predicted. The time domain and frequency domain analysis results of pressure drop of each drag model are similar. It is recommended to use the drag model derived from DNS or fine grid computational fluid dynamics–discrete element method (CFD-DEM) data first for CFD-DEM simulations. For the investigated BFB, the superficial gas velocity less than 0.9 m·s−1 should be adopted to obtain normal hydrodynamics.</abstract><pub>Elsevier B.V</pub><doi>10.1016/j.cjche.2023.06.002</doi><tpages>12</tpages><orcidid>https://orcid.org/0000-0001-7573-7224</orcidid><orcidid>https://orcid.org/0000-0003-4615-8789</orcidid></addata></record> |
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subjects | Bubbling fluidized bed Dense flow Drag model Gas–solid MFIX-DEM Simulation |
title | Comparative analysis on gas–solid drag models in MFIX-DEM simulations of bubbling fluidized bed |
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