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Flow Characterization in Triply-Periodic-Minimal-Surface (TPMS)-Based Porous Geometries: Part 2—Heat Transfer
Complex physical phenomena take place while dealing with the convective heat transfer in porous medium. Due to involved complexities, most of the earlier numerical studies are performed using various porous models compromising the detailed phenomena. Therefore, a pore-scale simulation has been perfo...
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Published in: | Transport in porous media 2024, Vol.151 (1), p.141-169 |
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description | Complex physical phenomena take place while dealing with the convective heat transfer in porous medium. Due to involved complexities, most of the earlier numerical studies are performed using various porous models compromising the detailed phenomena. Therefore, a pore-scale simulation has been performed for convective heat transfer in triply-periodic-minimal-surface lattices, with identical void fraction and unit-cell size, but different geometrical shapes (tortuosity), namely Diamond, Inverted Weaire–Phelan, Primitive, and Gyroid. Further, each lattice derived into three different types of porous structures by designing second subdomain as solid (in Type 1), fluid (in Type 2), and microporous zones (in Type 3). The convective heat transfer in a square mini-channel filled with the porous structures is investigated for the range of flow Reynolds number
0.01
<
Re
<
100
and
Pr
=
7
. The temperature distributions, solid and fluid Nusselt numbers on the external walls and on the internal walls, and quantitative departure from local thermal equilibrium (LTE) assumption are calculated for different porous media. The effect of porous morphology/tortuosity and effective porosity on the heat transfer is examined. The results revealed that the maximum temperature within the domain is found in Type 2 treatment, leading to inferior heat transfer performance compared to Type 1 and Type 3. Among all the lattices, the Diamond lattice provides more uniform temperature distribution over the external walls and within the volume including solid and fluid. The effective and the internal Nusselt numbers increase drastically for Re > 10. For the range of Re considered here, the Primitive lattice shows the maximum deviation from LTE assumption. |
doi_str_mv | 10.1007/s11242-023-02036-x |
format | article |
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0.01
<
Re
<
100
and
Pr
=
7
. The temperature distributions, solid and fluid Nusselt numbers on the external walls and on the internal walls, and quantitative departure from local thermal equilibrium (LTE) assumption are calculated for different porous media. The effect of porous morphology/tortuosity and effective porosity on the heat transfer is examined. The results revealed that the maximum temperature within the domain is found in Type 2 treatment, leading to inferior heat transfer performance compared to Type 1 and Type 3. Among all the lattices, the Diamond lattice provides more uniform temperature distribution over the external walls and within the volume including solid and fluid. The effective and the internal Nusselt numbers increase drastically for Re > 10. For the range of Re considered here, the Primitive lattice shows the maximum deviation from LTE assumption.</description><identifier>ISSN: 0169-3913</identifier><identifier>EISSN: 1573-1634</identifier><identifier>DOI: 10.1007/s11242-023-02036-x</identifier><language>eng</language><publisher>Dordrecht: Springer Netherlands</publisher><subject>Civil Engineering ; Classical and Continuum Physics ; Convective heat transfer ; Diamonds ; Earth and Environmental Science ; Earth Sciences ; External walls ; Fluid dynamics ; Fluid flow ; Geotechnical Engineering & Applied Earth Sciences ; Heat transfer ; Hydrogeology ; Hydrology/Water Resources ; Industrial Chemistry/Chemical Engineering ; Porous media ; Reynolds number ; Temperature distribution ; Tortuosity ; Unit cell ; Void fraction</subject><ispartof>Transport in porous media, 2024, Vol.151 (1), p.141-169</ispartof><rights>The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c319t-e7fceedba1fe2932356df3bcf37455f4d285927ea5e3cb112f0da562737de1e23</citedby><cites>FETCH-LOGICAL-c319t-e7fceedba1fe2932356df3bcf37455f4d285927ea5e3cb112f0da562737de1e23</cites><orcidid>0000-0002-3755-6374</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Rathore, Surendra Singh</creatorcontrib><creatorcontrib>Mehta, Balkrishna</creatorcontrib><creatorcontrib>Kumar, Pradeep</creatorcontrib><creatorcontrib>Asfer, Mohammad</creatorcontrib><title>Flow Characterization in Triply-Periodic-Minimal-Surface (TPMS)-Based Porous Geometries: Part 2—Heat Transfer</title><title>Transport in porous media</title><addtitle>Transp Porous Med</addtitle><description>Complex physical phenomena take place while dealing with the convective heat transfer in porous medium. Due to involved complexities, most of the earlier numerical studies are performed using various porous models compromising the detailed phenomena. Therefore, a pore-scale simulation has been performed for convective heat transfer in triply-periodic-minimal-surface lattices, with identical void fraction and unit-cell size, but different geometrical shapes (tortuosity), namely Diamond, Inverted Weaire–Phelan, Primitive, and Gyroid. Further, each lattice derived into three different types of porous structures by designing second subdomain as solid (in Type 1), fluid (in Type 2), and microporous zones (in Type 3). The convective heat transfer in a square mini-channel filled with the porous structures is investigated for the range of flow Reynolds number
0.01
<
Re
<
100
and
Pr
=
7
. The temperature distributions, solid and fluid Nusselt numbers on the external walls and on the internal walls, and quantitative departure from local thermal equilibrium (LTE) assumption are calculated for different porous media. The effect of porous morphology/tortuosity and effective porosity on the heat transfer is examined. The results revealed that the maximum temperature within the domain is found in Type 2 treatment, leading to inferior heat transfer performance compared to Type 1 and Type 3. Among all the lattices, the Diamond lattice provides more uniform temperature distribution over the external walls and within the volume including solid and fluid. The effective and the internal Nusselt numbers increase drastically for Re > 10. For the range of Re considered here, the Primitive lattice shows the maximum deviation from LTE assumption.</description><subject>Civil Engineering</subject><subject>Classical and Continuum Physics</subject><subject>Convective heat transfer</subject><subject>Diamonds</subject><subject>Earth and Environmental Science</subject><subject>Earth Sciences</subject><subject>External walls</subject><subject>Fluid dynamics</subject><subject>Fluid flow</subject><subject>Geotechnical Engineering & Applied Earth Sciences</subject><subject>Heat transfer</subject><subject>Hydrogeology</subject><subject>Hydrology/Water Resources</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Porous media</subject><subject>Reynolds number</subject><subject>Temperature distribution</subject><subject>Tortuosity</subject><subject>Unit cell</subject><subject>Void fraction</subject><issn>0169-3913</issn><issn>1573-1634</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2024</creationdate><recordtype>article</recordtype><recordid>eNp9kM1Kw0AUhQdRsFZfwFXAjS5G5yfJJO602FZoMdC6HqaTO5rSZupMgq0rH8In9EkcjeDOxeXC5Xzncg5Cp5RcUkLElaeUxQwTxsMQnuLtHurRRHBMUx7vox6haY55TvkhOvJ-SUjAsriH7HBlX6PBs3JKN-CqN9VUto6qOpq7arPa4SIcbVlpPK3qaq1WeNY6ozRE5_NiOrvAt8pDGRXW2dZHI7BraFwF_joqlGsi9vn-MQbVBDdVewPuGB0YtfJw8rv76HF4Nx-M8eRhdD-4mWDNad5gEEYDlAtFDbCcM56kpeELbbiIk8TEJcuSnAlQCXC9COENKVWSMsFFCRQY76Ozznfj7EsLvpFL27o6vJQsZzRjLBNxULFOpZ313oGRGxdCup2kRH4XK7tiZShW_hQrtwHiHeSDuH4C92f9D_UFazl9Sg</recordid><startdate>2024</startdate><enddate>2024</enddate><creator>Rathore, Surendra Singh</creator><creator>Mehta, Balkrishna</creator><creator>Kumar, Pradeep</creator><creator>Asfer, Mohammad</creator><general>Springer Netherlands</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0002-3755-6374</orcidid></search><sort><creationdate>2024</creationdate><title>Flow Characterization in Triply-Periodic-Minimal-Surface (TPMS)-Based Porous Geometries: Part 2—Heat Transfer</title><author>Rathore, Surendra Singh ; Mehta, Balkrishna ; Kumar, Pradeep ; Asfer, Mohammad</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c319t-e7fceedba1fe2932356df3bcf37455f4d285927ea5e3cb112f0da562737de1e23</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2024</creationdate><topic>Civil Engineering</topic><topic>Classical and Continuum Physics</topic><topic>Convective heat transfer</topic><topic>Diamonds</topic><topic>Earth and Environmental Science</topic><topic>Earth Sciences</topic><topic>External walls</topic><topic>Fluid dynamics</topic><topic>Fluid flow</topic><topic>Geotechnical Engineering & Applied Earth Sciences</topic><topic>Heat transfer</topic><topic>Hydrogeology</topic><topic>Hydrology/Water Resources</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Porous media</topic><topic>Reynolds number</topic><topic>Temperature distribution</topic><topic>Tortuosity</topic><topic>Unit cell</topic><topic>Void fraction</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Rathore, Surendra Singh</creatorcontrib><creatorcontrib>Mehta, Balkrishna</creatorcontrib><creatorcontrib>Kumar, Pradeep</creatorcontrib><creatorcontrib>Asfer, Mohammad</creatorcontrib><collection>CrossRef</collection><jtitle>Transport in porous media</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Rathore, Surendra Singh</au><au>Mehta, Balkrishna</au><au>Kumar, Pradeep</au><au>Asfer, Mohammad</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Flow Characterization in Triply-Periodic-Minimal-Surface (TPMS)-Based Porous Geometries: Part 2—Heat Transfer</atitle><jtitle>Transport in porous media</jtitle><stitle>Transp Porous Med</stitle><date>2024</date><risdate>2024</risdate><volume>151</volume><issue>1</issue><spage>141</spage><epage>169</epage><pages>141-169</pages><issn>0169-3913</issn><eissn>1573-1634</eissn><abstract>Complex physical phenomena take place while dealing with the convective heat transfer in porous medium. Due to involved complexities, most of the earlier numerical studies are performed using various porous models compromising the detailed phenomena. Therefore, a pore-scale simulation has been performed for convective heat transfer in triply-periodic-minimal-surface lattices, with identical void fraction and unit-cell size, but different geometrical shapes (tortuosity), namely Diamond, Inverted Weaire–Phelan, Primitive, and Gyroid. Further, each lattice derived into three different types of porous structures by designing second subdomain as solid (in Type 1), fluid (in Type 2), and microporous zones (in Type 3). The convective heat transfer in a square mini-channel filled with the porous structures is investigated for the range of flow Reynolds number
0.01
<
Re
<
100
and
Pr
=
7
. The temperature distributions, solid and fluid Nusselt numbers on the external walls and on the internal walls, and quantitative departure from local thermal equilibrium (LTE) assumption are calculated for different porous media. The effect of porous morphology/tortuosity and effective porosity on the heat transfer is examined. The results revealed that the maximum temperature within the domain is found in Type 2 treatment, leading to inferior heat transfer performance compared to Type 1 and Type 3. Among all the lattices, the Diamond lattice provides more uniform temperature distribution over the external walls and within the volume including solid and fluid. The effective and the internal Nusselt numbers increase drastically for Re > 10. For the range of Re considered here, the Primitive lattice shows the maximum deviation from LTE assumption.</abstract><cop>Dordrecht</cop><pub>Springer Netherlands</pub><doi>10.1007/s11242-023-02036-x</doi><tpages>29</tpages><orcidid>https://orcid.org/0000-0002-3755-6374</orcidid></addata></record> |
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subjects | Civil Engineering Classical and Continuum Physics Convective heat transfer Diamonds Earth and Environmental Science Earth Sciences External walls Fluid dynamics Fluid flow Geotechnical Engineering & Applied Earth Sciences Heat transfer Hydrogeology Hydrology/Water Resources Industrial Chemistry/Chemical Engineering Porous media Reynolds number Temperature distribution Tortuosity Unit cell Void fraction |
title | Flow Characterization in Triply-Periodic-Minimal-Surface (TPMS)-Based Porous Geometries: Part 2—Heat Transfer |
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