形状阻力公式大全形阻公式Word文档下载推荐.docx
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whereis:
hL-headloss;
v-velocity;
gn-accelerationofgravity;
Thenumberofvelocityheadslostduetoresistanceofvalvesandfittingsis:
K-resistancecoefficient;
Theheadlossduetoresistanceinvalvesandfittingsarealwaysassociatedwiththediameteronwhichvelocityoccurs.
TheresistancecoefficientKisconsideredtobeconstantforanydefinedvalvesorfittingsinallflowconditions,astheheadlossduetofrictionisminorcomparedtotheheadlossduetochangeindirectionofflow,obstructionsandsuddenorgradualchangesincrosssectionandshapeofflow.
HeadlossduetofrictioninstraightpipeisexpressedbytheDarcyequation:
f-frictionfactor;
L-length;
D-internaldiameter;
Itfollowsthat:
L-lengt;
TheratioL/Disequivalentlengthinpipediametersofstraightpipethatwillcausethesamepressuredroporheadlossasthevalvesorfittingsunderthesameflowconditions.AstheresistancecoefficientisKisconstanttheequivalentlengthL/Dwillvaryinverselywiththechangeinfrictionfactorfordifferentflowconditions.
Forgeometricallysimilarvalvesandfittings,theresistancecoefficientwouldbeconstant.Actuallytherearealwayssmallerorbiggergeometricalnonsimilarityinvalvesandfittingsofdifferentnominalsize,sotheresistancecoefficientisnotconstant.TheresistancecoefficientKforagiventypeofvalvesorfittings,tendstovarywithsizeasdoesfrictionfactorforstraightcleancommercialsteelpipeatthesameflowconditions.
Someresistancesinpipinglikesuddenorgradualcontractionsandenlargements,aswellaspipeentrancesorexistsaregeometricallysimilar.ThereforetheresistancecoefficientorequivalentlengthL/Disfortheseitemsindependentofsize.
ThevaluesforresistancecoefficientorequivalentlengthL/Darealwaysassociatedwithinternalpipediameterwheretheresistanceisoccurring.
IftheresistancecoefficientorequivalentlengthL/Dshouldbeusedfordifferentinternalpipediameterthanthediameterforwhichexistingvaluescanbefoundfollowingrelationshipcanbeused:
wheresubscript"
a"
definesKanddwiththereferencetointernalpipediameter,andsubscript"
b"
definesKanddwiththereferencetotheinternaldiameterforwhichvaluesofKcanbefoundintablesordiagrams.
ThisequationcanalsobeusedifthepipingsystemhasmorethanonesizeofvalvesandfittingstoexpresstheresistancecoefficientorequivalentlengthL/Dintermsofonesize.
ResistancecoefficientKcalculatorforvalvesandfittingscanbeused.
ResistancecoefficientKforinternaldiametersuddenandgradualcontractionandenlargement
Usingmomentum,continuityandBernoulliequationtheresistanceduetosuddenenlargementsmaybeexpressedas:
andtheresistancefactorduetosuddencontractionas:
K1-resistancecoefficient;
d1-internaldiameter(smaller);
d2-internaldiameter(larger);
Usingβasdiameterratio,bothequationcanbeexpressedas:
β-diameterratiod1/d2;
Inordertoexpresstheresistancecoefficientintermsoflargerpipediameter,followingrelationshouldbeused:
K1-resistancecoefficientbasedonsmallerinternaldiameter;
K2-resistancecoefficientbasedonlargerinternaldiameter;
Iftheenlargementisnotsuddenbutgradual,orifangleofgradualenlargementisdifferentfromO,GibsoncoefficientCecanbeusedfordifferentangleofdivergenceasfollows:
Inotherwords,ifangleofdivergenceisbiggerthan45O,theresistancecoefficientisequaltooneforsuddenenlargement.
ForgradualcontractiontheresistancecoefficientonthesamebasisbasedonCranetestdata,contractioncoefficientCccanbeusedfordifferentanglesofconvergence,asfollows:
Usingaboveexpressionsforenlargementandcontractioncoefficient,resistancecoefficientcanbecalculatedas:
Forgradualenlargement:
Ce-coefficientofenlargement;
θ-enlargementangle;
Forgradualcontraction:
Cc-coefficientofcontraction;
Forresistancecoefficientbasedonthelargepipediameterexpression:
shouldbeused,withaboveequations.
Equationsforgradualenlargementandcontractioncanbeusedforresistancecoefficientcalculationforreducedborestraight-throughvalveslikeballvalvesandgatevalves.Thetotalresistancecoefficientforthistypeofballandgatevalvesisthesummationofresistancecoefficientforgradualcontractionandgradualenlargement.
YoucancalculateresistancecoefficientusingresistancecoefficientKandequivalentlengthl/dcalculator.
FlowcoefficientCv,pressuredrop,controlvalveflowrate
Selectingthecorrectvalvesizeforagivenapplicationrequiresknowledgeofprocessconditionsthatthevalvewillactuallyseein.Intheindustryofcontrolvalvesitispracticetouseflowcoefficientandflowcharacteristics.
IntheUKandintheUSAcoefficientCvisusedanditisdefinedasflowrateofwateringpmat60OFthatcreatespressuredropof1psiacrossthevalve.Basicequationforvalvesizingforliquidis:
Cv-flowcoefficient[gpm];
q-flowrate[gpm];
Δp-pressuredrop[bar];
S-specificgravity(relativedensity)[-];
ToaidinestablishinguniformmeasurementofliquidflowcoefficientsCv,standardizedtestingfacilitybyFluidControlInstitute(FCI)areusedbymanufacturers.Theeffectofviscosityoffluidsotherthanwatershouldbeconsideredwhenselectingthevalve,asincreasedviscosityoffluidisreducingthevalvecapacity.
AnothercoefficientKvisusedinsomecountries,particularlyinEuropeandisdefinedasflowrateofwaterinm3/hthatcreatespressuredropof1kg/cm2acrossthevalve(1kg/cm2isequalto0.980665bar).
Controlvalvesizingisbasedonthecalculationofflowcoefficientforgivenpressuredropandflowrate.LiquidflowcapacityofavalveinmetricunitscanbeconvertedtoCvas:
qm-flowrate[l/m];
ρ-density[kg/m3];
Also,liquidflowcapacityofavalvecanbeconvertedtoKvas:
Kv-flowcharacteristic[m3/h];
qh-flowrate[m3/h];
AboveequationsareusedinflowcoefficientCv,pressuredropandcontrolvalveflowratecalculator.
Flashingandcavitation,vaporpressureatvalvevenacontracta
Flashingorcavitationinsideavalvecanhaveasignificantinfluenceonvalvecapacity.Flashingandcavitationcanreducetheflowthroughvalveinmanyliquids.Also,damagecanbemadetothevalveaswellastothepipingsystem.Theeffectisrepresentedbythechangefromliquidtovaporstateoffluid,resultinginthevelocityincreasedownstreamfromthevalve.
Asliquidpassesthroughtherestrictionareainsidethevalveflowstreamiscontracted.Thesmallestcrosssectionareaofstreamisjustdownstreamoftheactualphysicalrestrictionatapointcalledvenacontracta.Atthatpointthevelocityisatitsmaximumandpressureattheminimum.
Asthefluidexitsthevalve,awayfromvenacontracta,velocitydecreaseandpressureincrease,sothecriticalpointforflashingandcavitationisatthepointwherethepressureissmallestwhichisinvenacontracta.Ifpressureatvenacontractadropsbellowsthevaporpressureofthefluid,duetoincreasedvelocityatthispoint,bubbleswillformintheflowstream.
Ifpressuredownstreamofthevenacontractaincreaseabovethevaporpressure,bubbleswillcollapseorimplodeproducingcavitation.Cavitationreleasesenergyandproducesanoise.Ifcavitationoccursclosetosolidsurfaces,theenergyreleasedgraduallywearsthematerialleavingtheroughsurface.Cavitationcanalsodamagethedownstreampipeline,ifatthatplacethepressurerisesabovethevaporpressureandbubblescollapse.
Chockedflowvalvepressuredropandcavitationinhighpressurerecoveryvalve
Formationofbubblesinthevalveresultingofflashingandcavitationeffectreduc