Loading…

CFD modeling of bubble columns flows: implementation of population balance

The Bubble Population Balance Equation is implemented both in the two-fluid model and in the Algebraic Slip Mixture Model. Two and three-dimensional numerical simulations of two-phase (air–water) and pseudo-two-phase (air–Therminol-Glass beads) transient flows are performed for laboratory scale bubb...

Full description

Saved in:
Bibliographic Details
Published in:Chemical engineering science 2004-11, Vol.59 (22), p.5201-5207
Main Authors: Chen, P., Sanyal, J., Dudukovic, M.P.
Format: Article
Language:English
Subjects:
Citations: Items that this one cites
Items that cite this one
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by cdi_FETCH-LOGICAL-c424t-b367e83431af575ebe4ce0f8679e63bfabe06dc340ad6dce5da6f0abb62730843
cites cdi_FETCH-LOGICAL-c424t-b367e83431af575ebe4ce0f8679e63bfabe06dc340ad6dce5da6f0abb62730843
container_end_page 5207
container_issue 22
container_start_page 5201
container_title Chemical engineering science
container_volume 59
creator Chen, P.
Sanyal, J.
Dudukovic, M.P.
description The Bubble Population Balance Equation is implemented both in the two-fluid model and in the Algebraic Slip Mixture Model. Two and three-dimensional numerical simulations of two-phase (air–water) and pseudo-two-phase (air–Therminol-Glass beads) transient flows are performed for laboratory scale bubble columns of two different diameters operated over a range of superficial gas velocities (8 to 20 cm/s) in the churn turbulent regime. The ability of the simulations to predict liquid recirculation and gas radial holdup profile, which drives the recirculation, is illustrated. The simulations also capture the effects of increased superficial gas velocity and of surface tension on bubble size distribution in agreement with observations. At all conditions a uni-modal bubble size distribution is predicted.
doi_str_mv 10.1016/j.ces.2004.07.037
format article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_28105045</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0009250904004737</els_id><sourcerecordid>28105045</sourcerecordid><originalsourceid>FETCH-LOGICAL-c424t-b367e83431af575ebe4ce0f8679e63bfabe06dc340ad6dce5da6f0abb62730843</originalsourceid><addsrcrecordid>eNp9kMtO5DAQRS00SDSPD2CXzcwuoRw7dnpYjZq3kNjA2rKdMnLLiUOcgPh73GokdrMqlXRuPQ4h5xQqClRcbCuLqaoBeAWyAiYPyIq2kpWcQ_OLrABgXdYNrI_IcUrb3EpJYUUeNjdXRR87DH54LaIrzGJMwMLGsPRDKlyIH-lv4fsxYI_DrGcfhx03xnEJ-87ooAeLp-TQ6ZDw7LuekJeb6-fNXfn4dHu_-fdYWl7zuTRMSGwZZ1S7RjZokFsE1wq5RsGM0wZBdJZx0F2u2HRaONDGiFoyaDk7IX_2c8cpvi2YZtX7ZDHkIzAuSdUthQZ4k0G6B-0UU5rQqXHyvZ4-FQW1s6a2KltTO2sKpMrWcub393CdrA5uyp_59BMULGuTInOXew7zp-8eJ5Wsx2yh8xPaWXXR_2fLF3U4grM</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>28105045</pqid></control><display><type>article</type><title>CFD modeling of bubble columns flows: implementation of population balance</title><source>ScienceDirect Freedom Collection</source><creator>Chen, P. ; Sanyal, J. ; Dudukovic, M.P.</creator><creatorcontrib>Chen, P. ; Sanyal, J. ; Dudukovic, M.P.</creatorcontrib><description>The Bubble Population Balance Equation is implemented both in the two-fluid model and in the Algebraic Slip Mixture Model. Two and three-dimensional numerical simulations of two-phase (air–water) and pseudo-two-phase (air–Therminol-Glass beads) transient flows are performed for laboratory scale bubble columns of two different diameters operated over a range of superficial gas velocities (8 to 20 cm/s) in the churn turbulent regime. The ability of the simulations to predict liquid recirculation and gas radial holdup profile, which drives the recirculation, is illustrated. The simulations also capture the effects of increased superficial gas velocity and of surface tension on bubble size distribution in agreement with observations. At all conditions a uni-modal bubble size distribution is predicted.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/j.ces.2004.07.037</identifier><identifier>CODEN: CESCAC</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Applied sciences ; Bubble columns ; Chemical engineering ; Computational fluid dynamics ; Dynamic simulation ; Exact sciences and technology ; Modeling ; Multiphase flow ; Population balance</subject><ispartof>Chemical engineering science, 2004-11, Vol.59 (22), p.5201-5207</ispartof><rights>2004 Elsevier Ltd</rights><rights>2005 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c424t-b367e83431af575ebe4ce0f8679e63bfabe06dc340ad6dce5da6f0abb62730843</citedby><cites>FETCH-LOGICAL-c424t-b367e83431af575ebe4ce0f8679e63bfabe06dc340ad6dce5da6f0abb62730843</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>309,310,314,776,780,785,786,23910,23911,25119,27903,27904</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=16371076$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Chen, P.</creatorcontrib><creatorcontrib>Sanyal, J.</creatorcontrib><creatorcontrib>Dudukovic, M.P.</creatorcontrib><title>CFD modeling of bubble columns flows: implementation of population balance</title><title>Chemical engineering science</title><description>The Bubble Population Balance Equation is implemented both in the two-fluid model and in the Algebraic Slip Mixture Model. Two and three-dimensional numerical simulations of two-phase (air–water) and pseudo-two-phase (air–Therminol-Glass beads) transient flows are performed for laboratory scale bubble columns of two different diameters operated over a range of superficial gas velocities (8 to 20 cm/s) in the churn turbulent regime. The ability of the simulations to predict liquid recirculation and gas radial holdup profile, which drives the recirculation, is illustrated. The simulations also capture the effects of increased superficial gas velocity and of surface tension on bubble size distribution in agreement with observations. At all conditions a uni-modal bubble size distribution is predicted.</description><subject>Applied sciences</subject><subject>Bubble columns</subject><subject>Chemical engineering</subject><subject>Computational fluid dynamics</subject><subject>Dynamic simulation</subject><subject>Exact sciences and technology</subject><subject>Modeling</subject><subject>Multiphase flow</subject><subject>Population balance</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2004</creationdate><recordtype>article</recordtype><recordid>eNp9kMtO5DAQRS00SDSPD2CXzcwuoRw7dnpYjZq3kNjA2rKdMnLLiUOcgPh73GokdrMqlXRuPQ4h5xQqClRcbCuLqaoBeAWyAiYPyIq2kpWcQ_OLrABgXdYNrI_IcUrb3EpJYUUeNjdXRR87DH54LaIrzGJMwMLGsPRDKlyIH-lv4fsxYI_DrGcfhx03xnEJ-87ooAeLp-TQ6ZDw7LuekJeb6-fNXfn4dHu_-fdYWl7zuTRMSGwZZ1S7RjZokFsE1wq5RsGM0wZBdJZx0F2u2HRaONDGiFoyaDk7IX_2c8cpvi2YZtX7ZDHkIzAuSdUthQZ4k0G6B-0UU5rQqXHyvZ4-FQW1s6a2KltTO2sKpMrWcub393CdrA5uyp_59BMULGuTInOXew7zp-8eJ5Wsx2yh8xPaWXXR_2fLF3U4grM</recordid><startdate>20041101</startdate><enddate>20041101</enddate><creator>Chen, P.</creator><creator>Sanyal, J.</creator><creator>Dudukovic, M.P.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope></search><sort><creationdate>20041101</creationdate><title>CFD modeling of bubble columns flows: implementation of population balance</title><author>Chen, P. ; Sanyal, J. ; Dudukovic, M.P.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c424t-b367e83431af575ebe4ce0f8679e63bfabe06dc340ad6dce5da6f0abb62730843</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2004</creationdate><topic>Applied sciences</topic><topic>Bubble columns</topic><topic>Chemical engineering</topic><topic>Computational fluid dynamics</topic><topic>Dynamic simulation</topic><topic>Exact sciences and technology</topic><topic>Modeling</topic><topic>Multiphase flow</topic><topic>Population balance</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Chen, P.</creatorcontrib><creatorcontrib>Sanyal, J.</creatorcontrib><creatorcontrib>Dudukovic, M.P.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology &amp; Engineering</collection><collection>Engineering Research Database</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Chen, P.</au><au>Sanyal, J.</au><au>Dudukovic, M.P.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>CFD modeling of bubble columns flows: implementation of population balance</atitle><jtitle>Chemical engineering science</jtitle><date>2004-11-01</date><risdate>2004</risdate><volume>59</volume><issue>22</issue><spage>5201</spage><epage>5207</epage><pages>5201-5207</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>The Bubble Population Balance Equation is implemented both in the two-fluid model and in the Algebraic Slip Mixture Model. Two and three-dimensional numerical simulations of two-phase (air–water) and pseudo-two-phase (air–Therminol-Glass beads) transient flows are performed for laboratory scale bubble columns of two different diameters operated over a range of superficial gas velocities (8 to 20 cm/s) in the churn turbulent regime. The ability of the simulations to predict liquid recirculation and gas radial holdup profile, which drives the recirculation, is illustrated. The simulations also capture the effects of increased superficial gas velocity and of surface tension on bubble size distribution in agreement with observations. At all conditions a uni-modal bubble size distribution is predicted.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ces.2004.07.037</doi><tpages>7</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0009-2509
ispartof Chemical engineering science, 2004-11, Vol.59 (22), p.5201-5207
issn 0009-2509
1873-4405
language eng
recordid cdi_proquest_miscellaneous_28105045
source ScienceDirect Freedom Collection
subjects Applied sciences
Bubble columns
Chemical engineering
Computational fluid dynamics
Dynamic simulation
Exact sciences and technology
Modeling
Multiphase flow
Population balance
title CFD modeling of bubble columns flows: implementation of population balance
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-25T22%3A06%3A31IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=CFD%20modeling%20of%20bubble%20columns%20flows:%20implementation%20of%20population%20balance&rft.jtitle=Chemical%20engineering%20science&rft.au=Chen,%20P.&rft.date=2004-11-01&rft.volume=59&rft.issue=22&rft.spage=5201&rft.epage=5207&rft.pages=5201-5207&rft.issn=0009-2509&rft.eissn=1873-4405&rft.coden=CESCAC&rft_id=info:doi/10.1016/j.ces.2004.07.037&rft_dat=%3Cproquest_cross%3E28105045%3C/proquest_cross%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c424t-b367e83431af575ebe4ce0f8679e63bfabe06dc340ad6dce5da6f0abb62730843%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_pqid=28105045&rft_id=info:pmid/&rfr_iscdi=true