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1、Charpter2.ThepropertiesofpetroleumandproductsCONTENTnConditionalDensity,Specificgravity,nAveragemolecularweight,characteristicfactor(k)nViscositynCriticalpropertiesnThermalpropertiesnOthersSignificance•Thecriterionsofoilqualityevaluation;•Thecontrollingparametersofprocessing;•Thebasisofeng
2、ineeringtechnicaldesign.Characteristics:•Thecomprehensiveperformancesofthevariouscompoundsintheconstituents,andarerelatedcloselytotheirchemicalconstituents;•ThepropertiesaretestedbyConditionalexperiments;•Tousewidelyoftheexperiencechartsandcorrelationformula.1.Volatility1.1Vaporpressure:nI
3、stheforceexertedonthewallsofaclosedcontainerbythevaporizedportionofaliquid.Topreventitfromfurthervaporizing.nIncreaseswithtemperatureforanygivenproduct1.1.1VPofpurehydrocarbons•Dependingonthenaturesofhydrocarbons,inthesamilartemperature,thehigherMWmoleculeshavelowerVPinthesamegroupofhydroc
4、arbons.•Tospecialpuremolecules,VPIncreaseswithtemperature.DHV-lnp=-+CRTBlnp=A-T+C1.1.2VPofmixedhydrocarbonsanddistillates•Asthetotalpressureofsystemisnotveryhigh,forthemixedhydrocarbonswithsimpleconstituents:np=åpxiii=1•Forthemixedhydrocarbons,atthedefinitetemp.,onlytheconstituentsofgas,li
5、quidphasesortotalsystemaredefinite,theVPisconstantvalue.•Fordistillates,duetotheconstituentsaredifficulttodefine,theaboveequationisnotsuitable.Forthenarrowcutdistillates,VPcouldbeobtainedbyKandaverageBP.1.2BPrangeBoilingpoint:vtemperature,at1atmvHomologousseries:BPincreasewithmolecularweig
6、ht;branchedparaffinisomershavelowerBPthanthecorrespondingnormalalkane.vThereisanincreaseinBPwithanincreaseincarbonnumber.1.2BPrange1.2.1BPofpurehydrocarbonForliquidhydrocarbons,theirBParethetempera-tureastheirVPequaltoambientpressure(AP),i.e.,BPatAP.1.2.2BPofmixedhydrocarbonsForliquidmixtu
7、re,theBPatAPisnotconstant,theheaviercompositionsareconcentratedinliquidphaseduringthegasificationprocess,andtheBPincreasecontinuously;forthesecomplicatedmixtureofdistill-ates,theBPrangeisusuallyexpresseditsvaporationandgasificationproperties,i.e.,Boilingrange.