Systematic mesh development for 3D CFD simulation of fixed beds: Single sphere study
To develop and validate meshes for computational fluid dynamics (CFD) simulations of transport in fixed beds, a single particle is often used as a test case. We present results for drag coefficient ( C D) and heat transfer Nusselt number ( Nu) for flow past a sphere, focusing on high flow rates typi...
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Veröffentlicht in: | Computers & chemical engineering 2011-07, Vol.35 (7), p.1171-1185 |
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creator | Dixon, Anthony G. Ertan Taskin, M. Nijemeisland, Michiel Stitt, E. Hugh |
description | To develop and validate meshes for computational fluid dynamics (CFD) simulations of transport in fixed beds, a single particle is often used as a test case. We present results for drag coefficient (
C
D) and heat transfer Nusselt number (
Nu) for flow past a sphere, focusing on high flow rates typical of industrial steam reformers (400
<
Re
<
20,000). Over this range, good predictions of
C
D were obtained using large eddy simulation (LES) to capture vortex shedding and wake dynamics, with a mesh refined downstream from the sphere. The small time-steps and high cell count required make this too expensive for fixed beds.
Nu can be accurately calculated using a Reynolds-averaged Navier–Stokes (RANS) method with shear-stress transport (SST)
k–
ω closure provided the mesh at the particle surface is fine enough and covers most of the boundary layer. Single sphere simulations of heat transfer are more useful for fixed bed mesh development than drag coefficient calculations. |
doi_str_mv | 10.1016/j.compchemeng.2010.12.006 |
format | Article |
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C
D) and heat transfer Nusselt number (
Nu) for flow past a sphere, focusing on high flow rates typical of industrial steam reformers (400
<
Re
<
20,000). Over this range, good predictions of
C
D were obtained using large eddy simulation (LES) to capture vortex shedding and wake dynamics, with a mesh refined downstream from the sphere. The small time-steps and high cell count required make this too expensive for fixed beds.
Nu can be accurately calculated using a Reynolds-averaged Navier–Stokes (RANS) method with shear-stress transport (SST)
k–
ω closure provided the mesh at the particle surface is fine enough and covers most of the boundary layer. Single sphere simulations of heat transfer are more useful for fixed bed mesh development than drag coefficient calculations.</description><identifier>ISSN: 0098-1354</identifier><identifier>EISSN: 1873-4375</identifier><identifier>DOI: 10.1016/j.compchemeng.2010.12.006</identifier><identifier>CODEN: CCENDW</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Analytical and numerical techniques ; Computational fluid dynamics ; Computational methods in fluid dynamics ; Computer simulation ; Drag coefficient ; Drag coefficients ; Exact sciences and technology ; Finite element method ; Fixed beds ; Fluid dynamics ; Fundamental areas of phenomenology (including applications) ; Heat transfer ; Mathematical analysis ; Mathematical models ; Navier-Stokes equations ; Packed bed ; Physics ; Sphere ; Turbulence simulation and modeling ; Turbulent flow ; Turbulent flows, convection, and heat transfer ; Wakes</subject><ispartof>Computers & chemical engineering, 2011-07, Vol.35 (7), p.1171-1185</ispartof><rights>2010 Elsevier Ltd</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c420t-5c7ffb68553e158b2caa61fb609609b6ced547cb28e1cf8d7898946c6ae9e4593</citedby><cites>FETCH-LOGICAL-c420t-5c7ffb68553e158b2caa61fb609609b6ced547cb28e1cf8d7898946c6ae9e4593</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.compchemeng.2010.12.006$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=24284375$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Dixon, Anthony G.</creatorcontrib><creatorcontrib>Ertan Taskin, M.</creatorcontrib><creatorcontrib>Nijemeisland, Michiel</creatorcontrib><creatorcontrib>Stitt, E. Hugh</creatorcontrib><title>Systematic mesh development for 3D CFD simulation of fixed beds: Single sphere study</title><title>Computers & chemical engineering</title><description>To develop and validate meshes for computational fluid dynamics (CFD) simulations of transport in fixed beds, a single particle is often used as a test case. We present results for drag coefficient (
C
D) and heat transfer Nusselt number (
Nu) for flow past a sphere, focusing on high flow rates typical of industrial steam reformers (400
<
Re
<
20,000). Over this range, good predictions of
C
D were obtained using large eddy simulation (LES) to capture vortex shedding and wake dynamics, with a mesh refined downstream from the sphere. The small time-steps and high cell count required make this too expensive for fixed beds.
Nu can be accurately calculated using a Reynolds-averaged Navier–Stokes (RANS) method with shear-stress transport (SST)
k–
ω closure provided the mesh at the particle surface is fine enough and covers most of the boundary layer. Single sphere simulations of heat transfer are more useful for fixed bed mesh development than drag coefficient calculations.</description><subject>Analytical and numerical techniques</subject><subject>Computational fluid dynamics</subject><subject>Computational methods in fluid dynamics</subject><subject>Computer simulation</subject><subject>Drag coefficient</subject><subject>Drag coefficients</subject><subject>Exact sciences and technology</subject><subject>Finite element method</subject><subject>Fixed beds</subject><subject>Fluid dynamics</subject><subject>Fundamental areas of phenomenology (including applications)</subject><subject>Heat transfer</subject><subject>Mathematical analysis</subject><subject>Mathematical models</subject><subject>Navier-Stokes equations</subject><subject>Packed bed</subject><subject>Physics</subject><subject>Sphere</subject><subject>Turbulence simulation and modeling</subject><subject>Turbulent flow</subject><subject>Turbulent flows, convection, and heat transfer</subject><subject>Wakes</subject><issn>0098-1354</issn><issn>1873-4375</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2011</creationdate><recordtype>article</recordtype><recordid>eNqNkN9LwzAQx4MoOH_8D_FBfOpM0rRNfZPNqTDwYfM5pOlly2ibmnTD_fdmbIiPwsHB8bnvcR-E7igZU0Lzx81Yu7bXa2ihW40ZOczZmJD8DI2oKNKEp0V2jkaElCKhacYv0VUIG0II40KM0HKxDwO0arAatxDWuIYdNK6PcQM2zuN0iiezKQ623TaRch12Bhv7DTWuoA5PeGG7VQM49GvwsQ3ben-DLoxqAtye-jX6nL0sJ2_J_OP1ffI8TzRnZEgyXRhT5SLLUqCZqJhWKqdxQspYVa6hznihKyaAaiPqQpSi5LnOFZTAszK9Rg_H3N67ry2EQbY2aGga1YHbBinKnArOmYhkeSS1dyF4MLL3tlV-LymRB5FyI_-IlAeRkjIZRcbd-9MVFbRqjFedtuE3gMX8g-TITY4cxJd3FrwM2kIXv7Ae9CBrZ_9x7Qe5_49Y</recordid><startdate>20110711</startdate><enddate>20110711</enddate><creator>Dixon, Anthony G.</creator><creator>Ertan Taskin, M.</creator><creator>Nijemeisland, Michiel</creator><creator>Stitt, E. Hugh</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SC</scope><scope>7U5</scope><scope>8FD</scope><scope>JQ2</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope></search><sort><creationdate>20110711</creationdate><title>Systematic mesh development for 3D CFD simulation of fixed beds: Single sphere study</title><author>Dixon, Anthony G. ; Ertan Taskin, M. ; Nijemeisland, Michiel ; Stitt, E. Hugh</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c420t-5c7ffb68553e158b2caa61fb609609b6ced547cb28e1cf8d7898946c6ae9e4593</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2011</creationdate><topic>Analytical and numerical techniques</topic><topic>Computational fluid dynamics</topic><topic>Computational methods in fluid dynamics</topic><topic>Computer simulation</topic><topic>Drag coefficient</topic><topic>Drag coefficients</topic><topic>Exact sciences and technology</topic><topic>Finite element method</topic><topic>Fixed beds</topic><topic>Fluid dynamics</topic><topic>Fundamental areas of phenomenology (including applications)</topic><topic>Heat transfer</topic><topic>Mathematical analysis</topic><topic>Mathematical models</topic><topic>Navier-Stokes equations</topic><topic>Packed bed</topic><topic>Physics</topic><topic>Sphere</topic><topic>Turbulence simulation and modeling</topic><topic>Turbulent flow</topic><topic>Turbulent flows, convection, and heat transfer</topic><topic>Wakes</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Dixon, Anthony G.</creatorcontrib><creatorcontrib>Ertan Taskin, M.</creatorcontrib><creatorcontrib>Nijemeisland, Michiel</creatorcontrib><creatorcontrib>Stitt, E. Hugh</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Computer and Information Systems Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>ProQuest Computer Science Collection</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Computer and Information Systems Abstracts Academic</collection><collection>Computer and Information Systems Abstracts Professional</collection><jtitle>Computers & chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Dixon, Anthony G.</au><au>Ertan Taskin, M.</au><au>Nijemeisland, Michiel</au><au>Stitt, E. Hugh</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Systematic mesh development for 3D CFD simulation of fixed beds: Single sphere study</atitle><jtitle>Computers & chemical engineering</jtitle><date>2011-07-11</date><risdate>2011</risdate><volume>35</volume><issue>7</issue><spage>1171</spage><epage>1185</epage><pages>1171-1185</pages><issn>0098-1354</issn><eissn>1873-4375</eissn><coden>CCENDW</coden><abstract>To develop and validate meshes for computational fluid dynamics (CFD) simulations of transport in fixed beds, a single particle is often used as a test case. We present results for drag coefficient (
C
D) and heat transfer Nusselt number (
Nu) for flow past a sphere, focusing on high flow rates typical of industrial steam reformers (400
<
Re
<
20,000). Over this range, good predictions of
C
D were obtained using large eddy simulation (LES) to capture vortex shedding and wake dynamics, with a mesh refined downstream from the sphere. The small time-steps and high cell count required make this too expensive for fixed beds.
Nu can be accurately calculated using a Reynolds-averaged Navier–Stokes (RANS) method with shear-stress transport (SST)
k–
ω closure provided the mesh at the particle surface is fine enough and covers most of the boundary layer. Single sphere simulations of heat transfer are more useful for fixed bed mesh development than drag coefficient calculations.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.compchemeng.2010.12.006</doi><tpages>15</tpages></addata></record> |
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subjects | Analytical and numerical techniques Computational fluid dynamics Computational methods in fluid dynamics Computer simulation Drag coefficient Drag coefficients Exact sciences and technology Finite element method Fixed beds Fluid dynamics Fundamental areas of phenomenology (including applications) Heat transfer Mathematical analysis Mathematical models Navier-Stokes equations Packed bed Physics Sphere Turbulence simulation and modeling Turbulent flow Turbulent flows, convection, and heat transfer Wakes |
title | Systematic mesh development for 3D CFD simulation of fixed beds: Single sphere study |
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