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Thermodynamics---Chapter2
TheFirstLawofThermodynamics---Chapter2
TheFirstLaw
ofThermodynamicsContentsTheinternalenergy,thetotalenergyThefirstlawofthermodynamicsFirstlawofthermodynamicsforaclosedsystem,andanopensystemMovingboundarywork,
FlowworkEnthalpy2-1TheTotalEnergyofaSystem
Thetotalenergyofasystem(系统的总能/储存能)(1)Microscopicforms—internalenergy
(2)macroscopicforms—KE,PE1.InternalEnergy(热力学能)
isdefinedasthesumofallthemicroscopicformsofenergyofasystem.Itisrelatedtothemolecularstructureandthedegreeofmolecularactivity.
2-1-2InternalEnergy(热力学能)(3)Chemicalenergy(化学能)
Nuclearenergy(核能)
Magneticenergy(磁能)Including:(1)Molecular
kineticenergy(分子动能/内动能)
Translationalenergy,rotationalkineticenergy,vibrationalkineticenergyIncreasesasthetemperatureofthesubstanceincreases(2)Molecularpotentialenergy(分子势能/内势能)
AssociatedwiththeattractiveforcesbetweenmoleculesIncreasesasthedistancebetweenmoleculesincreasesItishigherforgases,andlowerforsolidsinternalenergyMolecular
kineticenergyMolecularPotentialenergyChemicalenergyNuclearenergymagneticenergy++++Molecular
kineticenergyMolecularPotentialenergy+negligibleUnit:J,denotedbyU.Specificinternalenergy(比热力学能)
Theinternalenergyonamassbasis.u,J/kg.2.Internalenergyisaproperty,itisafunctionoftemperatureandspecificvolumeofthesubstance.3.Thermodynamicsprovidesnoinformationastoabsolutevaluesofinternalenergy.
Itisonlythechangeininternalenergy,However,whichisimportantinengineeringproblem.AvalueofU=0canbeassignedtoanyparticularstateofasystem.itisusualtochoosetheoriginas0ºC,atwhichtemperaturetheinternalenergyissuggestedasbeingzero.
2-1-2KineticEnergyandPotentialEnergyKineticEnergy(宏观动能)
Theenergythatasystempossessesasaresultofitsmotionrelativetosomereferenceframe.EK2.PotentialEnergy(宏观位能)
Theenergythatasystempossessesasaresultofitselevationinagravitationalfield.EP
Expressedas:
2-1-3TheTotalEnergy(总储存能)
Thetotalenergy:E=U+EK+EPJ,KJ
Onpermassbasis:e=u+ek+epJ/kg,KJ/kg
等量空气从相同的初态出发,分别经过可逆绝热过程A和不可逆绝热过程B到达相同的终态,分析空气的热力学能变化:ΔUA,ΔUB关系。解:ΔUA=ΔUB(热力学能是状态参数,热力学能的变化只与初终状态有关)。2-2TheFirstLawofThermodynamics
2-2-1SomeStatementsStatement2(陈述2)
Theperpetualmotionmachineofthefirstkind
(第一类永动机)canneverbemanufactured.Statement1(陈述1)
Energycanbeneithercreatednordestroyed.itcanonlychangeforms.TheFirstLawofThermodynamics,knownastheconservationofenergyprinciple,providesasoundbasisforstudyingtherelationshipsamongthevariousformsofenergyandenergyinteractions.
2-2-2EnergyBalance(方程表达式)
ForanykindofsystemundergoinganykindofprocessTheenergywhichleavethesystemThechangeinthetotalenergyofthesystem-Theenergywhichenterthesystem=
Thefirstlawofthermodynamicsisafar-reachingprincipleofnaturewhichisinducedfromtheresultsofmanyexperiments.Itcannotbededucedorprovedfromanyotherprincipleofnature,Itisentirelyempirical.Energytransferbyheat,work,andmassChangeininternal,kinetic,potential.etc.energies
自然界中发生的一切过程都必须遵守能量守恒定律,反之,遵守能量守恒与转换定律的一切过程都可以自发进行。(x)2-3EnergyBalanceforClosedSystem(闭口系统的热力学第一定律表达式)
2-3-1EnergyBalanceforClosedSystemSystem:gasclosedinapiston-cylinderAssumptions:
Process:fromequilibriumstate1tostate2Heatinput:Qworkoutput:WNeglect:ΔEK,ΔEP21QWTheenergywhichleavethesystemThechangeinthetotalenergyofthesystem-Theenergywhichenterthesystem=Energybalance:——Energyequationforclosedsystem
Q–W=UQ=W+U=W+U2-U1
2-3-2Notes(说明)
Signification(意义):
Theheatabsorbedbyasystem:
Onaunitmassbasis:q=w+u
Applicationconditions(适用条件):a:Reversibleprocess,non-reversibleprocessb:Idealgas,actualgasc:Theendstatesisinequilibriumstate.QWu2-3-3VariousFormsoftheFirstLawRelationforClosedSystem(不同形式)GeneralQ=U+W
(一般形式)q=
u+wDifferentialform
Q=dU+
W
(微分形式)
q=du+
wReversibleprocessQ=U+12pdV
(可逆过程)q=u+12pdvDifferentialreversible
Q=dU+pdV
(可逆微元过程)
q=du+pdv
Cycle
(循环)
Qnet=wnet
q:微元热量
w:微元功量du:热力学能的微元变化量1.系统中工质经历一个可逆定温过程,由于没有温度变化,故该系统中工质不能与外界交换热量。2.封闭热力系内发生可逆定容过程时,系统一定不对外作容积变化功。3.封闭热力系中,不作膨胀功的过程一定是定容过程。4.气体膨胀时一定对外作功。5.工质吸热后一定会膨胀。
q=w+u(x)(x)(x)()(x)例题例1:一个装有2kg工质的闭口系统经历了如下过程:过程中系统散热25kJ,外界对系统作功100kJ,比热力学能减少15kJ/kg,而且整个系统被举高1000m。试确定过程中系统动能的变化。简单求解过程:系统为闭口系统,并考虑闭口系动能,位能的变化。应用热力学第一定律:说明:系统动能增加,增加了85.4kJ
。注意:注意求解过程中热量,功的正负。例2:一活塞汽缸中的气体经历了两个过程,从状态1到状态2,气体吸热500kJ,活塞对外做功800kJ。从状态2到状态3是一个定压的压缩过程,压力为400kPa,气体向外散热450kJ。并且已知U1=2000kJ,U3=3500kJ,试计算2-3过程中气体体积的变化。简单求解过程:系统为闭口系统,考虑气体经历两个过程:过程1-2和过程2-3。对过程1-2:Q12=W12+U2-U1(1)对过程2-3:Q23=W23+U3-U2(2)过程2-3为可逆定压过程,根据可逆过程体积变化功的计算公式:将(1)+(2)得:
Q12+Q23=W12+W23+U3-U1代入数据:
500+(-450)=800+400(V3-V2)+(3500-2000)解得:V3-V2=-5.625m3说明:压缩过程中,体积减小。
2-4EnergyBalanceforSteady-FlowSystems(开口系统稳定流动的能量方程式)(1)Thefluidpropertiesatdifferentpositionisdifferent(2)Energycanbetransferredtoorfromasysteminthreeforms:heat,work,massflow(3)Consideringbothenergybalanceandmass
balance(4)Work:Movingboundarywork,flowwork.etc.notes
2-4-1SteadyFlow(稳定流动)1.SteadyFlow(稳定流动)
Aprocessduringwhichafluidflowsthroughacontrolvolumesteadily.thatis,thefluidpropertiescanchangefrompointtopointwithinthecontrolvolume,butatanypoint,theyremainconstantduringtheentireprocess.
2.CharacteristicsofSteady-FlowProcess(特性)(2)Energybalance(perunittime):
Ein=Eout,Ecv=constant(3)Nopropertieswithinthecontrolvolumechangewithtime(1)Massbalance(perunittime):
min=mout,
mcv=constant
2-4-2FlowWork(流动功)
1.FlowWork
Requiredtopushthemassintooroutofthecontrolvolume
2.FlowWorkRelation(关系式)
2112Perunitmass:Theproductpvrepresentsenergyforflowingfluidsonlyanddoesnotrepresentanyformofenergyfornon-flow(closed)system.notes
2-4-3Enthalpy(焓)Definition(定义):H=U+pVJkJperunitmass:h=u+pvJ/kgkJ/kg(1)Enthalpyisaproperty.(2)Wecannotobtainabsolutevaluesofenthalpy.Internalenergyandflowworkusuallytransferredatthesametimeinflowingfluid.notes
2-4-4EnergyBalanceforSteady-FlowSystems
(开口系统稳定流动能量方程式)
System:Considerasteady-flowsystemasshown.thesystemhasasingleinletandasingleoutlet2112WsQ1.EnergyBalanceforSteady-Flow
Systems
Assumption:forperunittimein:m1,cf1out:m2,cf2
energy:input:Q,
output:WS(shaftwork)
totalenergychangeECV
TheenergywhichenterthesystemTheenergywhichleavethesystemTheenergywhichleavethesystemThechangeinthetotalenergyofthesystem-Theenergywhichenterthesystem=Energybalance:ThechangeinthetotalenergyofthesystemForsteadyflowΔECV=0So:——EnergyBalanceforSteady-FlowSystems
Applicationconditions(适用条件):
(1)Steadyflow
(2)Reversibleprocess,non-reversibleprocess
2.Analysis(分析)HeattransferChangeofinternalenergyChangeofmechanic-alenergyFlowworkShaftwork
EnergyBalanceforClosedSystem:
EnergyBalanceforSteady-FlowSystems:notesSameprinciple:expansion----workoutputDifferentforms:
2-4-5TechnicalWork(技术功)
1.Definition
Inthermodynamics,thesummationofenergywhichincreasesinkineticenergy,potentialenergyandworkofshaftiscalledtechnicalwork.
2.TherelationshipofW,WS,Wt,
(pv)
3.TechnicalWorkinReversibleProcess
(可逆过程中技术功表示)pv120vdpIfdp<0,wt>0,workdonebythesystemIfdp>0,wt<0,workdoneonthesystemIfdp=0,wt=0Notes
2-4-6VariousFormsoftheFirstLawRelationforSteady-FlowSystem(不同形式)Differentialform
Q=dH+Wt
(微分形式)
q=dh+wtReversibleprocessQ=H-12Vdp
(可逆过程)
q=h-12vdp
DifferentialreversibleprocessQ=dH-Vdp
(可逆微元过程)
q=dh-vdpGeneralQ=H+Wt
(一般形式)q=h+wt根据热力学第一定律,任何循环的净热量等于该循环的净功量。热力过程中,工质向外界放热,其温度必然降低。工质从同一初态出发,分别经历可逆过程和不可逆过程达到相同的终态,则两过程中工质与外界交换的热量相同。工质所作的膨胀功与技术功,在某种条件下,两者的数值会相等。Q=H+Wt,q=h+wt
()()(x)(x)功不是状态参数,热力学能与推动功之和也不是状态参数。流动功的改变量仅取决于系统进出口状态,而与工质经历的过程无关。(x)()2-5SomeSteady-flowEngineeringDevices(稳定流动能量方程式的应用)
Energybalanceforsteady-flowsystems
Somecommonsteady-flowdevicesTurbinesandcompressors(pump,fan)(汽轮机和压缩机)
Heatexchanges(热交换器)
Nozzlesanddiffusers(喷嘴和扩压器)
Throttlingvalues(节流阀)
2-5-1HeatExchanges(热交换器)EnergyBalanceNotes:Theheattransferassociatedwithaheatexchangemaybezeroornonzerodependingonhowthesystemisselected.Heatexchangesaredeviceswheretwomovingfluidstreamsexchangeheatwithoutmixing.
Characteristics
Noworkinteractions,ws=0Negligiblekineticandpotentialenergychanges,cf2=0,z=0h2h1
2-5-2Turbines(涡轮,汽轮机)Characteristics
Wellinsulated,Negligible,q=0Negligiblekineticandpotentialenergychanges,cf2=0,z=0EnergyBalanceNotes:Ws=Wt.Thedevicethatdrivestheelectricgeneratorinsteam,gas,orhydroelectricplants.
2-5-3Compressors(压缩机)
Compressors,aswellaspumpsandfans,aredevicesusedtoincreasethepressureofafluid.Charac
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