w3heattransferthermalstresskwWord格式.docx
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∙Understandtheinputandoutputforasteady-stateandatransientheattransferanalysis.
∙Useanamplitudespecificationforloading.
∙Understandtheprocedureforwritingtemperaturestotheresults(.fil)fileandreadingthosetemperaturesintoastressanalysis.
∙Understandhowusersubroutinesareused(optional).
Problemdescription
Thephysicalproblemisasquaretubewithacircularhole.Thetubeissurroundedbyafluid,andtheholeisfilledwithanotherfluid.Thetwo-dimensionalfiniteelementmodelwillcontainonlyaone-eighthsectorofthetube,asshowninFigureW3–1.Thethermalpropertiesofthetubearegivenbelow:
∙Thermalpropertiesofthetube:
Specificheat=485.7N·
m/kg·
°
C
Density=7833.0kg/m3
Conductivity=11.19W/m·
FigureW3–1Squaretubewithcircularhole.
Steady-stateheattransferanalysis
AppliedTemperatures
Wewillstartwithananalysisinwhichthefluidtemperaturesareapplieddirectlytothenodesoftheinnerandouterwallsofthetube.Thisapproachimpliesthatthefluidstouchingthewallsareinfiniteheatsinks.
1.Entertheworkingdirectoryforthisworkshop:
../heat_transfer/keywords/workshop3
andviewthecontentsoffilet-sstemp.inpinatexteditor.
2.Submittheinputfilet-sstemp.inp.
3.Afterthejobcompletes,startanABAQUS/Viewersessionandopen
t-sstemp.odb.Theundeformedmodelshapeisplottedbydefault.
4.UsetheResultsTreetodeterminethelocationsofthedifferentnodeandelementsets.
a.IntheResultsTree,expandtheElementSetsandNodeSetscontainersunderneaththeoutputdatabasenamedt-sstemp.odb.
b.Selectdifferentsets;
thecorrespondingsetswillbehighlightedintheviewport.
c.Onceyouarefamiliarwiththelocationsofthedifferentsets,collapsethecontainers.
Onlyone-eighthofthecross-sectionneedstobemodeledbecauseofsymmetry.
QuestionW3–1:
Whatshouldtheboundaryconditionsbeatthosesymmetrylines?
Whataretheappliedboundaryconditionsinthemodel?
Thinkaboutthedifferencebetweenenforcingsymmetryforathermalboundaryascomparedtothatforadisplacementboundary.
5.Createacontourplotofthetemperature(variableNT11).Theprocedureisprovidedbelow.Checkthecontourlinesatthesymmetrylines.Thecontourlinesshouldbenormaltotheedgeifthesymmetryconditionsarecorrectlyenforced.
d.Fromthemainmenubar,selectResultFieldOutput.
e.IntheFieldOutputdialogbox,selectNT11(nodaltemperature)astheprimaryvariable.ClickOK.
f.IntheSelectPlotStatedialogbox,chooseContourandclickOK.
Filmcoefficients(forsurfaceconvection)
Theinterfacebetweenthetubeandthefluidscanbemodeledmorerealisticallybydefiningfilmcoefficientsandsinktemperatures.
6.Copyt-sstemp.inptoafilecalledt-ssfilm.inp.
7.Modifyt-ssfilm.inpbygivingthestepanewtitleandremovingtheoptionthatappliestemperaturestotheinnerandouterwalls.
8.Adda*FILMoptiontothehistorysectionwiththefollowingtwolines:
*FILM
INWL,F4,400.,1500.
Thisfilmdefinitionspecifiesasinktemperatureof400°
Candafilmcoefficientof1500
W/m2·
C,appliedtotheelementssurroundingtheroundhole(set=INWL).ThefilmtypeF4appliesthefilmtoelementface4.ThefacenumberisbasedontheelementconnectivityandisdocumentedintheelementlibrarysectionoftheUser’sManual.Forplanarquadsthefacesarenumberedasshownatright:
Allelement-baseddistributedloadsareappliedtoelementfacesinasimilarmanner.Alternatively,surface-baseddistributedloadsmaybeusedtoapplydistributedloadstopredefinedsurfaces(e.g.,*SFILM).
9.Youalsoneedtoapplyafilmdefinitiontotherightedgeofthemodel.TheelementsetOUTWLalreadygroupstheelementsalongtheedge.Tofindtheelementface,runadatacheckanalysisoft-sstemp.inpandeitherlookfortheelementconnectivityint-sstemp.dat(lookforthestring“ELEM”)ordothefollowinginABAQUS/Viewer(recommended):
g.Opent-sstemp.odbinABAQUS/Viewer.Theundeformedmodelshapeisplottedbydefault.
h.UsetheResultsTreetolimitthedisplaytoelementsetPART-1-1.OUTWL.
i.Inthetoolbox,clicktheCommonOptionstool
.
j.IntheCommonPlotOptionsdialogbox,clicktheLabelstabandtoggleonShowelementlabelsandShowfacelabels.
k.ClickOK.
10.Withtheinformationobtainedinthepreviousstep,addanadditionaldatalinetothe*FILMoptiondefinedabovethatspecifiesafilmdefinitionfortherightedge.Giveasin