A Similarity Solution with Two-Equation Turbulence Model for Computation of Turbulent Film Condensation on a Vertical Surface
In this paper, we presented a similarity solution for turbulent film condensation of stationary vapor on an isothermal vertical flat plate. In this method, some similarity transformations are employed and the set of governing partial differential equations (PDE) of conservation together with transpo...
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Veröffentlicht in: | Journal of Applied Fluid Mechanics 2018-05, Vol.11 (3), p.637-645 |
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description | In this paper, we presented a similarity solution for turbulent film condensation of stationary vapor on an isothermal vertical flat plate. In this method, some similarity transformations are employed and the set of governing partial differential equations (PDE) of conservation together with transport equations of turbulent kinetic energy and dissipation rate are transformed into a set of ordinary differential equations (ODE). Calculated data for the flow field, velocity profile, wall shear stress, condensate film thickness, turbulent kinetic energy, rate of dissipation, and heat transfer properties are discussed. The effect of Prandtl (Pr) number was also investigated in a wide range of variations. The obtained results showed that at high Prandtl numbers, the velocity profile becomes more uniform across the condensation film and therefore, the kinetic energy of turbulence is reduced. Furthermore, the effect of change in Pr is negligible at high Pr numbers and consequently, the flow parameters have no significant change in this range. The friction coefficient changes linearly through the condensation film and the slope of friction lines diminishes slightly by the Pr number. The rate of turbulent kinetic energy increases linearly from the wall up to about 20% of condensate film, then rises asymptotically and converges to a constant value near the liquid-vapor interface. Also, the rate of turbulent dissipation grows linearly up to 40% of condensate film thickness and then increases slightly while it oscillates. |
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In this method, some similarity transformations are employed and the set of governing partial differential equations (PDE) of conservation together with transport equations of turbulent kinetic energy and dissipation rate are transformed into a set of ordinary differential equations (ODE). Calculated data for the flow field, velocity profile, wall shear stress, condensate film thickness, turbulent kinetic energy, rate of dissipation, and heat transfer properties are discussed. The effect of Prandtl (Pr) number was also investigated in a wide range of variations. The obtained results showed that at high Prandtl numbers, the velocity profile becomes more uniform across the condensation film and therefore, the kinetic energy of turbulence is reduced. Furthermore, the effect of change in Pr is negligible at high Pr numbers and consequently, the flow parameters have no significant change in this range. The friction coefficient changes linearly through the condensation film and the slope of friction lines diminishes slightly by the Pr number. The rate of turbulent kinetic energy increases linearly from the wall up to about 20% of condensate film, then rises asymptotically and converges to a constant value near the liquid-vapor interface. Also, the rate of turbulent dissipation grows linearly up to 40% of condensate film thickness and then increases slightly while it oscillates.</description><identifier>ISSN: 1735-3572</identifier><identifier>EISSN: 1735-3645</identifier><identifier>DOI: 10.29252/jafm.11.03.28531</identifier><language>eng</language><publisher>Isfahan: Isfahan University of Technology</publisher><subject>Coefficient of friction ; Computational fluid dynamics ; Condensates ; Differential equations ; Energy ; Film condensation ; Film thickness ; Flat plates ; Friction ; Heat transfer ; Kinetic energy ; Liquid-vapor interfaces ; Ordinary differential equations ; Partial differential equations ; Shear stress ; Similarity solutions ; Transport equations ; Turbulence models ; Turbulent film condensation; Similarity solution; k- turbulence modeling; Vertical surface ; Two-equation turbulence model ; Vapors ; Velocity ; Velocity distribution ; Wall shear stresses</subject><ispartof>Journal of Applied Fluid Mechanics, 2018-05, Vol.11 (3), p.637-645</ispartof><rights>2018. This work is published under http://creativecommons.org/licenses/by-nc-nd/4.0/ (the “License”). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,864,27924,27925</link.rule.ids></links><search><creatorcontrib>Ziaei Rad, M.</creatorcontrib><creatorcontrib>Ahmadi Nadooshan, A.</creatorcontrib><creatorcontrib>Mahmoodi, S.</creatorcontrib><creatorcontrib>Department of Mechanical Engineering, Faculty of Engineering, University of Isfahan, Isfahan, Iran</creatorcontrib><creatorcontrib>Engineering Faculty, Shahrekord University, Shahrekord, Iran</creatorcontrib><creatorcontrib>Department of Mechanical Engineering, Faculty of Engineering, Shahrekord University, Shahrekord, Iran</creatorcontrib><title>A Similarity Solution with Two-Equation Turbulence Model for Computation of Turbulent Film Condensation on a Vertical Surface</title><title>Journal of Applied Fluid Mechanics</title><description>In this paper, we presented a similarity solution for turbulent film condensation of stationary vapor on an isothermal vertical flat plate. In this method, some similarity transformations are employed and the set of governing partial differential equations (PDE) of conservation together with transport equations of turbulent kinetic energy and dissipation rate are transformed into a set of ordinary differential equations (ODE). Calculated data for the flow field, velocity profile, wall shear stress, condensate film thickness, turbulent kinetic energy, rate of dissipation, and heat transfer properties are discussed. The effect of Prandtl (Pr) number was also investigated in a wide range of variations. The obtained results showed that at high Prandtl numbers, the velocity profile becomes more uniform across the condensation film and therefore, the kinetic energy of turbulence is reduced. Furthermore, the effect of change in Pr is negligible at high Pr numbers and consequently, the flow parameters have no significant change in this range. The friction coefficient changes linearly through the condensation film and the slope of friction lines diminishes slightly by the Pr number. The rate of turbulent kinetic energy increases linearly from the wall up to about 20% of condensate film, then rises asymptotically and converges to a constant value near the liquid-vapor interface. Also, the rate of turbulent dissipation grows linearly up to 40% of condensate film thickness and then increases slightly while it oscillates.</description><subject>Coefficient of friction</subject><subject>Computational fluid dynamics</subject><subject>Condensates</subject><subject>Differential equations</subject><subject>Energy</subject><subject>Film condensation</subject><subject>Film thickness</subject><subject>Flat plates</subject><subject>Friction</subject><subject>Heat transfer</subject><subject>Kinetic energy</subject><subject>Liquid-vapor interfaces</subject><subject>Ordinary differential equations</subject><subject>Partial differential equations</subject><subject>Shear stress</subject><subject>Similarity solutions</subject><subject>Transport equations</subject><subject>Turbulence models</subject><subject>Turbulent film condensation; Similarity solution; k- turbulence modeling; Vertical surface</subject><subject>Two-equation turbulence model</subject><subject>Vapors</subject><subject>Velocity</subject><subject>Velocity distribution</subject><subject>Wall shear stresses</subject><issn>1735-3572</issn><issn>1735-3645</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><sourceid>ABUWG</sourceid><sourceid>AFKRA</sourceid><sourceid>AZQEC</sourceid><sourceid>BENPR</sourceid><sourceid>CCPQU</sourceid><sourceid>DWQXO</sourceid><sourceid>DOA</sourceid><recordid>eNo9UU1r3DAUNKWFhjQ_oDdBz97qW9YxLEkbSOlht72KJ-mp1WJbG9km5ND_Hmc3zek9ZoZ585im-czohluu-NcDpGHD2IaKDe-UYO-aC2aEaoWW6v3_XRn-sbmapuyplEYKYexF8--a7PKQe6h5fiK70i9zLiN5zPNfsn8s7c3DAidkv1S_9DgGJD9KxJ6kUsm2DMdlPgtKetPM5Db3w8qOEcfplR4JkN9Y5xygJ7ulJgj4qfmQoJ_w6nVeNr9ub_bb7-39z2932-v7NnBpWWtSxA68p1SDBdmhjsKYGDsbvPEJ0UtMEajhAhloL3WnuF5_1DQmk7i4bO7OvrHAwR1rHqA-uQLZnYBS_zh4SdajC15Y5MCj9kEmESwoa7vAjeZKeWtXry9nr2MtDwtOszuUpY5rfMelMdwI3rFVxc6qUMs0VUxvVxl1p9LcS2mOMUeFO5UmngEKBYzJ</recordid><startdate>20180501</startdate><enddate>20180501</enddate><creator>Ziaei Rad, M.</creator><creator>Ahmadi Nadooshan, A.</creator><creator>Mahmoodi, S.</creator><general>Isfahan University of Technology</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7TB</scope><scope>7U5</scope><scope>7UA</scope><scope>8FD</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>C1K</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope><scope>PIMPY</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PRINS</scope><scope>DOA</scope></search><sort><creationdate>20180501</creationdate><title>A Similarity Solution with Two-Equation Turbulence Model for Computation of Turbulent Film Condensation on a Vertical Surface</title><author>Ziaei Rad, M. ; Ahmadi Nadooshan, A. ; Mahmoodi, S.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c2491-7fde8abb006a9a48e6d377dd89cb7bfeeb4efda0723e1a6b46852647460df7f23</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>Coefficient of friction</topic><topic>Computational fluid dynamics</topic><topic>Condensates</topic><topic>Differential equations</topic><topic>Energy</topic><topic>Film condensation</topic><topic>Film thickness</topic><topic>Flat plates</topic><topic>Friction</topic><topic>Heat transfer</topic><topic>Kinetic energy</topic><topic>Liquid-vapor interfaces</topic><topic>Ordinary differential equations</topic><topic>Partial differential equations</topic><topic>Shear stress</topic><topic>Similarity solutions</topic><topic>Transport equations</topic><topic>Turbulence models</topic><topic>Turbulent film condensation; Similarity solution; k- turbulence modeling; Vertical surface</topic><topic>Two-equation turbulence model</topic><topic>Vapors</topic><topic>Velocity</topic><topic>Velocity distribution</topic><topic>Wall shear stresses</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ziaei Rad, M.</creatorcontrib><creatorcontrib>Ahmadi Nadooshan, A.</creatorcontrib><creatorcontrib>Mahmoodi, S.</creatorcontrib><creatorcontrib>Department of Mechanical Engineering, Faculty of Engineering, University of Isfahan, Isfahan, Iran</creatorcontrib><creatorcontrib>Engineering Faculty, Shahrekord University, Shahrekord, Iran</creatorcontrib><creatorcontrib>Department of Mechanical Engineering, Faculty of Engineering, Shahrekord University, Shahrekord, Iran</creatorcontrib><collection>CrossRef</collection><collection>Aqualine</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Water Resources Abstracts</collection><collection>Technology Research Database</collection><collection>ProQuest Central (Alumni Edition)</collection><collection>ProQuest Central UK/Ireland</collection><collection>ProQuest Central Essentials</collection><collection>ProQuest Central</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ProQuest One Community College</collection><collection>ProQuest Central Korea</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Publicly Available Content Database</collection><collection>ProQuest One Academic Eastern Edition (DO NOT USE)</collection><collection>ProQuest One Academic</collection><collection>ProQuest One Academic UKI Edition</collection><collection>ProQuest Central China</collection><collection>DOAJ Directory of Open Access Journals</collection><jtitle>Journal of Applied Fluid Mechanics</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ziaei Rad, M.</au><au>Ahmadi Nadooshan, A.</au><au>Mahmoodi, S.</au><aucorp>Department of Mechanical Engineering, Faculty of Engineering, University of Isfahan, Isfahan, Iran</aucorp><aucorp>Engineering Faculty, Shahrekord University, Shahrekord, Iran</aucorp><aucorp>Department of Mechanical Engineering, Faculty of Engineering, Shahrekord University, Shahrekord, Iran</aucorp><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A Similarity Solution with Two-Equation Turbulence Model for Computation of Turbulent Film Condensation on a Vertical Surface</atitle><jtitle>Journal of Applied Fluid Mechanics</jtitle><date>2018-05-01</date><risdate>2018</risdate><volume>11</volume><issue>3</issue><spage>637</spage><epage>645</epage><pages>637-645</pages><issn>1735-3572</issn><eissn>1735-3645</eissn><abstract>In this paper, we presented a similarity solution for turbulent film condensation of stationary vapor on an isothermal vertical flat plate. In this method, some similarity transformations are employed and the set of governing partial differential equations (PDE) of conservation together with transport equations of turbulent kinetic energy and dissipation rate are transformed into a set of ordinary differential equations (ODE). Calculated data for the flow field, velocity profile, wall shear stress, condensate film thickness, turbulent kinetic energy, rate of dissipation, and heat transfer properties are discussed. The effect of Prandtl (Pr) number was also investigated in a wide range of variations. The obtained results showed that at high Prandtl numbers, the velocity profile becomes more uniform across the condensation film and therefore, the kinetic energy of turbulence is reduced. Furthermore, the effect of change in Pr is negligible at high Pr numbers and consequently, the flow parameters have no significant change in this range. The friction coefficient changes linearly through the condensation film and the slope of friction lines diminishes slightly by the Pr number. The rate of turbulent kinetic energy increases linearly from the wall up to about 20% of condensate film, then rises asymptotically and converges to a constant value near the liquid-vapor interface. Also, the rate of turbulent dissipation grows linearly up to 40% of condensate film thickness and then increases slightly while it oscillates.</abstract><cop>Isfahan</cop><pub>Isfahan University of Technology</pub><doi>10.29252/jafm.11.03.28531</doi><tpages>9</tpages><oa>free_for_read</oa></addata></record> |
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subjects | Coefficient of friction Computational fluid dynamics Condensates Differential equations Energy Film condensation Film thickness Flat plates Friction Heat transfer Kinetic energy Liquid-vapor interfaces Ordinary differential equations Partial differential equations Shear stress Similarity solutions Transport equations Turbulence models Turbulent film condensation Similarity solution k- turbulence modeling Vertical surface Two-equation turbulence model Vapors Velocity Velocity distribution Wall shear stresses |
title | A Similarity Solution with Two-Equation Turbulence Model for Computation of Turbulent Film Condensation on a Vertical Surface |
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