fluent-换热器的相变模拟计算

fluent-换热器的相变模拟计算

ID:26635389

大小:1.65 MB

页数:28页

时间:2018-11-27

fluent-换热器的相变模拟计算_第1页
fluent-换热器的相变模拟计算_第2页
fluent-换热器的相变模拟计算_第3页
fluent-换热器的相变模拟计算_第4页
fluent-换热器的相变模拟计算_第5页
资源描述:

《fluent-换热器的相变模拟计算》由会员上传分享,免费在线阅读,更多相关内容在教育资源-天天文库

1、NewInitiativesatFluentInc.PhaseChangeinHeatExchangersBrianBell,FluentInc.UGM20011CompanyConfidentialCopyright2001FluentInc.Allrightsreserved.MotivationDemonstratetheuseofFluenttomodelphasechangeinheatexchangersProcessesofinterestCondensationEvaporationBoilingIllustratehowtomodelon

2、esuchprocessthroughuseofadetailedexampleShell-and-tubecondenserProvidemotivationforuserstobegindevelopingmodelsoftheirowndevices2CompanyConfidentialCopyright2001FluentInc.Allrightsreserved.OutlineProblemDescriptionShell-and-tubecondenserPurevaporcondensationNon-condensablegasesMod

3、elingApproachPorousmediumHeatandmasstransfermodelingModelImplementationUser-DefinedFunctionsandUser-DefinedMemoryResultsSteamcondenserwithnon-condensablegasesCommercialchillercondenser3CompanyConfidentialCopyright2001FluentInc.Allrightsreserved.DescriptionofProblemShell-and-tubeco

4、ndenser4CompanyConfidentialCopyright2001FluentInc.Allrightsreserved.GoalsofCFDModelingCondenserperformancecharacterizedbyheatandmasstransferrateCFDallowsevaluationoffactorsaffectingheatandmasstransferincondenserTubebundleconfigurationTubearrangementNumberofpassesLocationofinletpor

5、tsBafflesPressuredropVelocityfieldNon-condensablesLocationandconfigurationofpurgesystemResultsallowidentificationofpotentialdesignimprovements5CompanyConfidentialCopyright2001FluentInc.Allrightsreserved.FilmCondensationProcessDrivingpotentialforcondensationisthetemperaturedifferen

6、cebetweenvaporandcoolingwaterDrivingpotentialvariationcausedbyPressuredropRiseofcoolingwatertemperatureNon-condensablesTPH2OPairCondensatelayerTubewallCoolingwater6CompanyConfidentialCopyright2001FluentInc.Allrightsreserved.CFDModelingTheoryPorousmediumapproachTubebundletreatedasp

7、orousmediumEnablescomputationallyefficientmodelingofentirecondenserComparisonwithdetailedmodelingapproachIn2-D,O(100)-O(1000)controlvolumespertubeversusmorethanonetubepercontrolvolumeHeatandmasstransfermodelsCondensationratecalculationCondensationratedeterminedfromlocalflowfieldan

8、dcoolingwatertemperatureLiquidfil

当前文档最多预览五页,下载文档查看全文

此文档下载收益归作者所有

当前文档最多预览五页,下载文档查看全文
温馨提示:
1. 部分包含数学公式或PPT动画的文件,查看预览时可能会显示错乱或异常,文件下载后无此问题,请放心下载。
2. 本文档由用户上传,版权归属用户,天天文库负责整理代发布。如果您对本文档版权有争议请及时联系客服。
3. 下载前请仔细阅读文档内容,确认文档内容符合您的需求后进行下载,若出现内容与标题不符可向本站投诉处理。
4. 下载文档时可能由于网络波动等原因无法下载或下载错误,付费完成后未能成功下载的用户请联系客服处理。