高速泵结构比较文章图.docx
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高速泵结构比较文章图.docx
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高速泵结构比较文章图
ProceedingsofASME20103rdJointUS-EuropeanFluidsEngineeringSummerMeetingand8thInternationalConferenceonNanochannels,Microchannels,andMinichannels
FEDSM2010-ICNMM2010
August1-5,2010,Montreal,Canada
FEDSM-ICNMM2010-30405
NUMERICANALYSISONINTERNALFLOWOFHIGH-SPEEDPUMPOFDIFFERENTSTRUCTURALSTYLE
ShiHai-xia
ChemicalMachineryResearchInstitute,HefeiUniversityofTechnology,Hefei,China,23009
-0551-*******
jdshx@
WuJian-bo
ChemicalMachineryResearchInstitute,HefeiUniversityofTechnology,Hefei,China,23009
-0551-*******
gmriwjb2000@
HeYu-jie
ChemicalMachineryResearchInstitute,HefeiUniversityofTechnology,Hefei,China,23009
-0551-*******
Heyujie301@
LiQiang
ChemicalMachineryResearchInstitute,HefeiUniversityofTechnology,Hefei,China,23009
-0551-*******
hfliqiang@
ABSTRACT
Inordertostudytheeffectofthestructuralstyleofhigh-speedpumponinternalflow,4typeshigh-speedpumpofdifferentstructuralstyleareselectedforcomprehensiveanalysis,S-AturbulencemodelandSIMPLIECalgorithmareadoptedfornumericalsimulationofinternalflow.Bycomprehensivelycomparingthestaticpressure,totalpressure,sectionalvelocityvectorandflowpathline,twotypesofhigh-speedpumpswithcylindrical-bladeimpellermatchingnozzletypepumpcasinghaverelativelyidealpressurefieldandflowcondition,canreducehydraulicloss.Thecomprehensiveperformanceof4typesofhigh-speedpumpispredictedthroughcomputationalsimulation,thehigh-speedpumpwithopencylindrical-bladeimpellermatchingnozzletypepumpcasinghasmostexcellentperformance,indicatingthestructuralstyleofhigh-speedpumphaseffectonitsinternalflowandperformance.
Keywords:
high-speedpump,structuralstyle,numericalsimulation,flowanalysis,performance.
NOMENCLATURE
Impellerdiameter,m
Impellerwidthatoutlet,m
Numberoflong/shortblades
Basiccircleofvolutecasing,m
Throatdiameterofdiffuser,m
Lengthofdiffusionsectionofdiffuser,m
Diffusionangle,0C;
Totalpressure
Staticpressure
Absolutespeed
Totalpressureatimpellerinlet
Totalpressureatoutletofpumpcasing
SumofmomentsaboutZ-axis
INTRODUCTION
High-speedpartialemissionpumpistheonewithspecialconstructionandloworultra-lowspecificspeed(<50[1]),ithasthefeaturesofsmallflow,highhead,highspeed,simpleconstruction,highreliability,convenientmanufactureandrepair,etc.[2],itiswidelyappliedinthefieldofaviation,sprayirrigation,firefighting,petrochemicalengineeringetc.Themediumentersthesuctionchamberofthepumpandisdischargedafterpassingthroughopenimpeller,annularvolutecasingandnozzletypediffuser,theinternalflowofthepumpisverycomplexandbelongstounsteadyflow[3].Internalflowdiffersfordifferentstructuralstyleofhigh-speedpumpandthehydraulicperformancedifferssomewhat;inliterature[4~6]onlysingle-itemnumericalsimulationiscarriedoutonimpeller,internalflowpassageandvolute,thuscannottrulyreflectstheoverallflowconditionofhigh-speedpump,whereasliterature[7]conductedfully3Dunsteadycomputationalsimulationontheentireconstant-speedcentrifugalpump,inthispaperfocusisplacedonanalysisandcomparisonofinternalflowcharacteristicsof4differentstructuresofhigh-speedpump,andinternalflowanalysisandnumericsimulationstudyarecarriedoutondifferentstructuresofhigh-speedpumpforthecommon4combinationsofimpellerandnozzlestylecasingwiththeturbulencemodelsofNavier-StokesandRealizableequationsfor3DturbulentflowusingFluentsoftware,wall-functionmethodandmeshtechniqueforslidingbetweenimpellerandpumpcasingandS-AturbulencemodelandimplicitcorrectionSIMPLIECalgorithmofsecond-ordercentraldifferencescheme.
STRUCTURALSTYLEOFIMPELLERANDNOZZLESTYLEPUMPCASING
4differentstructuralstylesareformedbymatching4typesofimpellerwithnozzlestylepumpcasing,amongthemtheassemblyofstraight-bladeimpellerandnozzlestylepumpcasinghasmoreapplicationinpractice.
Structuralstyleofimpeller
Thecommonstructuralstylesofimpeller[8-9]athomeandabroadareshownasinFig.1,thesefourtypesofimpellerhavethesamegeometricdimensions,seeTable1and2.
Table1:
Performanceparametersofhigh-speedpump
DescriptionValue
Flow(m3/h)15
Head(m)400
NPSH(m)3.5
Speed(r/min)8500
Power(kW)75
Table2:
hydraulicdimensionsofhigh-speedpump
DescriptionValue
Impellerdiameter(m)0.17
Impellerwidthatoutlet(m)0.012
Numberoflong/shortblades8/8
Basiccircleofvolutecasing(m)0.186
Throatdiameterofdiffuser(m)0.0095
Lengthofdiffusionsectionofdiffuser(m)0.067
Diffusionangle(0C)8
(a)Semi-openstraight-bladecompositeimpeller
(b)Openstraight-bladeimpeller
(c)Opencylindrical-bladeimpeller
(d)Semi-opencylindrical-bladecompositeimpeller
Figure1.Structuraldiagramofimpeller
Structuralstyleofpumpcasing
Thepumpcasingiscomposedofannularvoluteandnozzlestylediffuser,asshowninFig.2.
Figure2.Structuraldiagramofpumpcasing
NUMERICCOMPUTATION
Griddivision
Pro/Eisappliedtobuild3Dhydraulicmodeldiagramofpump,andinordertoobtainbettercomputationalresults,alengthofleadingpipewhoselengthis3timesofpipediameterisaddedatimpellerinletandoutletofvolutecasing.Thehydraulicdimensionsofhigh-speedpumparegenerallyrelativelysmall,andthegapbetweenimpellerandpumpchamberisverysmall,inordertoobtainbettercomputationalresults,thelocationsofsmalldimensionsarelocallyencryptedingriddivision,thesizeofgriddivisionshouldnotbetoobig.ANSYS-Fluentpre-processingsoftwareGambitisusedforgriddivision,andnon-structuredhybridgridTGirdisadoptedtodividetheentiremodel,thisgridismainlycomposedoftetrahedrons,andhexahedrons,conesandwedgesatlocallocations,itcanwellprocessgriddivisionofcomplexmodel;themax.divisionsizeofimpellerandannularvoluteis1,thenumberofdivisionelementsofimpelleris1307994andthatofannularvoluteis380929.
Selectionofturbulencemodel
Dr.Basquepointedoutthattheflowpatternvariessignificantlyonthewallareaofhigh-speedpartialemissionpump,theflowintheflowpassageofimpellercanalmostbedeemedtobeastateofrigidmotionwithimpeller,therotatingflowinannularvolutealsodoesnothavemotionrelativetoimpeller,therefore,thestressofturbulentflowactshardly;modeloflowReynoldsnumberisselectedintheanalysisofhigh-speedpump.
InANSYS-Fluent,theSpalart-AllmarasmodelisproventobeveryeffectiveforbuildinglowRe-numbermodel,especiallyithasshownveryeffectforwallrestrainingflow,andhasmoreextensiveapplicationinrotarymachinery;byreferencetoselectionofturbulencemodelfornumericanalysisofpartialemissionpumpwithspecificspeedintherangeof50~130,thismodelisselectedastheturbulencemodelfornumericsimulationofhigh-speedpumpwithlowspecificspeed.
Settingofboundaryconditions
Theinletboundaryconditionissettobeaninletofuniformandcontinuousvelocitywithoutrotation,andtheoutletissettobetheoneoffreeoutflow;thefrontandrearcover,wallofannularvolute,wallofwaterpilotingsectionatinletandoutletandwaterbodyaresettobestationary;theimpellerwallandwaterbodyofimpelleraresettoberotarywiththerotaryspeedof8500rpm,MRFmodelisselectedandimpellerwall,frontandrearshroudandwallofvolutehousingareallsettobesliplessadiabaticwall[6].
ANALYSISOFSIMULATIONRESULTS
Analysisofpressurefield
TaketheaxialmiddlesectionofannularvolutetocalculatethestaticpressureinsidetheannularvoluteandimpelleranduseANSYS-CFD-Postprogramtoanalyzethecomputationalresults.
Nomenclature
Typeahigh-speedpumpofcombinedconstructionofsemi-openstraight-bladecompositeimpellerandnozzlestylepumpcasing.
Typebhigh-speedpumpofcombinedconstructionofopenstraight-bladecompositeimpellerandnozzlestylepumpcasing.
Typechigh-speedpumpofcombinedconstructionofopencylindrical-bladecompositeimpellerandnozzlestylepumpcasing.
Typedhigh-speedpumpofcombinedconstructionofsemi-opencylindrical-bladecompositeimpellerandnozzlestylepumpcasing.
(a)High-speedpumpoftypea
(b)High-speedpumpoftypeb
(c)High-speedpumpoftypec
(d)High-speedpumpoftyped
Figure3.Staticpressurediagramsofthefourtypesofhigh-speedpump
Cavitationtendstotakeplaceattheinletsofthefourtypesofhigh-speedpump,thepressurepresentsatendencyofannularoutwardincrement,yetthepressuregraduallyincreasesfrominlettooutletandfromhubtorim,indicatingtheworkdonebybladeprofileincreasesradially.Takethetangentialpositionofnozzletoexcircleofannularvoluteas0°position,intheareawhichissweptacrossthenozzletovoluteshroudbytheimpellerfrom0°positioninthedirectionofimpellerrotation,thepressureinimpellerandannularflowpassagehassomewhatdropcomparedtootherareasandthepressuregradientincreasesslowly;intheareafrom0°to90°,largernegativepressureareaappearsatimpellerinletandbladeinlet,whichextremelytendstocausecavitation.
Intheannularflowpassageofannularvolute,thestaticpressuredistributionisratheruniformintherangefrom90°to360°intherotationaldirectionofimpeller;intheareafrom0°to90°,especiallyinfrontofinletofstraightpipesection,thestaticpressuredropssignificantly;intheareafromstraightpipesectiontodif
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