3 Aclass A1 bt. ir1 na Tj re ac nt so r y 3 \ n name Time sourceSideMassFlowSource.nPorts sourceSideMassFlowSource.verifyInputs sourceSideMassFlowSource.ports[1].m_flow sourceSideMassFlowSource.ports[1].p sourceSideMassFlowSource.ports[1].h_outflow sourceSideMassFlowSource.X[1] sourceSideMassFlowSource.m_flow sourceSideMassFlowSource.T sourceSideMassFlowSource.T_in sourceSideFixedBoundary.nPorts sourceSideFixedBoundary.verifyInputs sourceSideFixedBoundary.ports[1].m_flow sourceSideFixedBoundary.ports[1].p sourceSideFixedBoundary.ports[1].h_outflow sourceSideFixedBoundary.X[1] sourceSideFixedBoundary.p sourceSideFixedBoundary.T TsuSourceRamp.height TsuSourceRamp.duration TsuSourceRamp.y TsuSourceRamp.offset TsuSourceRamp.startTime T_amb_internal.k T_amb_internal.y heatPump.allowFlowReversal1 heatPump.allowFlowReversal2 heatPump.port_a1.m_flow heatPump.port_a1.p heatPump.port_a1.h_outflow heatPump.port_b1.m_flow heatPump.port_b1.p heatPump.port_b1.h_outflow heatPump.port_a2.m_flow 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heatPump.innerCycle.switchQCon.u3 heatPump.innerCycle.switchQCon.y heatPump.innerCycle.Pel heatPump.innerCycle.switchPel.u1 heatPump.innerCycle.switchPel.u2 heatPump.innerCycle.switchPel.u3 heatPump.innerCycle.switchPel.y heatPump.innerCycle.PerformanceDataHPHeating.Pel heatPump.innerCycle.PerformanceDataHPHeating.QCon heatPump.innerCycle.PerformanceDataHPHeating.sigBus.nSet heatPump.innerCycle.PerformanceDataHPHeating.sigBus.modeSet heatPump.innerCycle.PerformanceDataHPHeating.sigBus.onOffMea heatPump.innerCycle.PerformanceDataHPHeating.sigBus.TEvaInMea heatPump.innerCycle.PerformanceDataHPHeating.sigBus.TConInMea heatPump.innerCycle.PerformanceDataHPHeating.sigBus.TEvaOutMea heatPump.innerCycle.PerformanceDataHPHeating.sigBus.TConOutMea heatPump.innerCycle.PerformanceDataHPHeating.sigBus.PelMea heatPump.innerCycle.PerformanceDataHPHeating.sigBus.m_flowEvaMea heatPump.innerCycle.PerformanceDataHPHeating.sigBus.m_flowConMea heatPump.innerCycle.PerformanceDataHPHeating.sigBus.iceFacMea heatPump.innerCycle.PerformanceDataHPHeating.QEva heatPump.innerCycle.PerformanceDataHPHeating.calcRedQCon.u1 heatPump.innerCycle.PerformanceDataHPHeating.calcRedQCon.u2 heatPump.innerCycle.PerformanceDataHPHeating.calcRedQCon.y heatPump.innerCycle.PerformanceDataHPHeating.calcRedQCon.k1 heatPump.innerCycle.PerformanceDataHPHeating.calcRedQCon.k2 heatPump.innerCycle.PerformanceDataHPHeating.proRedQEva.u1 heatPump.innerCycle.PerformanceDataHPHeating.proRedQEva.u2 heatPump.innerCycle.PerformanceDataHPHeating.proRedQEva.y heatPump.innerCycle.PerformanceDataHPHeating.QCon_flow_nominal heatPump.innerCycle.PerformanceDataHPHeating.interpMethod heatPump.innerCycle.PerformanceDataHPHeating.extrapMethod heatPump.innerCycle.PerformanceDataHPHeating.Q_flowTableNom heatPump.innerCycle.PerformanceDataHPHeating.minCOP heatPump.innerCycle.PerformanceDataHPHeating.switchPel.u1 heatPump.innerCycle.PerformanceDataHPHeating.switchPel.u2 heatPump.innerCycle.PerformanceDataHPHeating.switchPel.u3 heatPump.innerCycle.PerformanceDataHPHeating.switchPel.y heatPump.innerCycle.PerformanceDataHPHeating.switchQCon.u1 heatPump.innerCycle.PerformanceDataHPHeating.switchQCon.u2 heatPump.innerCycle.PerformanceDataHPHeating.switchQCon.u3 heatPump.innerCycle.PerformanceDataHPHeating.switchQCon.y heatPump.innerCycle.PerformanceDataHPHeating.constZero.k heatPump.innerCycle.PerformanceDataHPHeating.constZero.y heatPump.innerCycle.PerformanceDataHPHeating.QScaling.k heatPump.innerCycle.PerformanceDataHPHeating.QScaling.y heatPump.innerCycle.PerformanceDataHPHeating.product_scaling.u1 heatPump.innerCycle.PerformanceDataHPHeating.product_scaling.u2 heatPump.innerCycle.PerformanceDataHPHeating.product_scaling.y heatPump.innerCycle.PerformanceDataHPHeating.Table_QCon.nin heatPump.innerCycle.PerformanceDataHPHeating.Table_QCon.u[1] heatPump.innerCycle.PerformanceDataHPHeating.Table_QCon.u[2] heatPump.innerCycle.PerformanceDataHPHeating.Table_QCon.u[3] heatPump.innerCycle.PerformanceDataHPHeating.Table_QCon.y heatPump.innerCycle.PerformanceDataHPHeating.Table_QCon.readFromFile heatPump.innerCycle.PerformanceDataHPHeating.Table_QCon.interpMethod heatPump.innerCycle.PerformanceDataHPHeating.Table_QCon.extrapMethod heatPump.innerCycle.PerformanceDataHPHeating.Table_QCon.data[1] heatPump.innerCycle.PerformanceDataHPHeating.Table_COP.nin heatPump.innerCycle.PerformanceDataHPHeating.Table_COP.u[1] heatPump.innerCycle.PerformanceDataHPHeating.Table_COP.u[2] heatPump.innerCycle.PerformanceDataHPHeating.Table_COP.u[3] heatPump.innerCycle.PerformanceDataHPHeating.Table_COP.y heatPump.innerCycle.PerformanceDataHPHeating.Table_COP.readFromFile heatPump.innerCycle.PerformanceDataHPHeating.Table_COP.interpMethod heatPump.innerCycle.PerformanceDataHPHeating.Table_COP.extrapMethod heatPump.innerCycle.PerformanceDataHPHeating.Table_COP.data[1] heatPump.innerCycle.PerformanceDataHPHeating.multiplex3_1.n1 heatPump.innerCycle.PerformanceDataHPHeating.multiplex3_1.n2 heatPump.innerCycle.PerformanceDataHPHeating.multiplex3_1.n3 heatPump.innerCycle.PerformanceDataHPHeating.multiplex3_1.u1[1] heatPump.innerCycle.PerformanceDataHPHeating.multiplex3_1.u2[1] heatPump.innerCycle.PerformanceDataHPHeating.multiplex3_1.u3[1] heatPump.innerCycle.PerformanceDataHPHeating.multiplex3_1.y[1] heatPump.innerCycle.PerformanceDataHPHeating.multiplex3_1.y[2] heatPump.innerCycle.PerformanceDataHPHeating.multiplex3_1.y[3] heatPump.innerCycle.PerformanceDataHPHeating.divisionPel.u1 heatPump.innerCycle.PerformanceDataHPHeating.divisionPel.u2 heatPump.innerCycle.PerformanceDataHPHeating.divisionPel.y heatPump.innerCycle.PerformanceDataHPHeating.max.u1 heatPump.innerCycle.PerformanceDataHPHeating.max.u2 heatPump.innerCycle.PerformanceDataHPHeating.max.y heatPump.innerCycle.PerformanceDataHPHeating.const_minCOP.k heatPump.innerCycle.PerformanceDataHPHeating.const_minCOP.y heatPump.innerCycle.gainEva.k heatPump.innerCycle.gainEva.u heatPump.innerCycle.gainEva.y heatPump.use_rev heatPump.use_autoCalc heatPump.Q_useNominal heatPump.scalingFactor heatPump.use_refIne heatPump.refIneFre_constant heatPump.nthOrder heatPump.useBusConnectorOnly heatPump.mFlow_conNominal heatPump.VCon heatPump.dpCon_nominal heatPump.deltaM_con heatPump.use_conCap heatPump.CCon heatPump.GConOut heatPump.GConIns heatPump.mFlow_evaNominal heatPump.VEva heatPump.dpEva_nominal heatPump.deltaM_eva heatPump.use_evaCap heatPump.CEva heatPump.GEvaOut heatPump.GEvaIns heatPump.tauSenT heatPump.transferHeat heatPump.allowFlowReversalEva heatPump.allowFlowReversalCon heatPump.tauHeaTraEva heatPump.TAmbEva_nominal heatPump.tauHeaTraCon heatPump.TAmbCon_nominal heatPump.initType heatPump.pCon_start heatPump.TCon_start heatPump.TConCap_start heatPump.XCon_start[1] heatPump.pEva_start heatPump.TEva_start heatPump.TEvaCap_start heatPump.XEva_start[1] heatPump.x_start[1] heatPump.x_start[2] heatPump.x_start[3] heatPump.yRefIne_start heatPump.massDynamics heatPump.energyDynamics heatPump.machineType heatPump.show_TPort heatPump.from_dp heatPump.homotopyInitialization heatPump.linearized heatPump.con.allowFlowReversal heatPump.con.port_a.m_flow heatPump.con.port_a.p heatPump.con.port_a.h_outflow heatPump.con.port_b.m_flow heatPump.con.port_b.p heatPump.con.port_b.h_outflow heatPump.con.m_flow_nominal heatPump.con.m_flow_small heatPump.con.m_flow heatPump.con.dp heatPump.con.computeFlowResistance heatPump.con.from_dp heatPump.con.dp_nominal heatPump.con.linearizeFlowResistance heatPump.con.deltaM heatPump.con.tau heatPump.con.energyDynamics heatPump.con.massDynamics heatPump.con.p_start heatPump.con.T_start heatPump.con.X_start[1] heatPump.con.vol.energyDynamics heatPump.con.vol.massDynamics heatPump.con.vol.substanceDynamics heatPump.con.vol.traceDynamics heatPump.con.vol.p_start heatPump.con.vol.T_start heatPump.con.vol.X_start[1] heatPump.con.vol.mSenFac heatPump.con.vol.prescribedHeatFlowRate heatPump.con.vol.simplify_mWat_flow heatPump.con.vol.m_flow_nominal heatPump.con.vol.nPorts heatPump.con.vol.m_flow_small heatPump.con.vol.allowFlowReversal heatPump.con.vol.V heatPump.con.vol.ports[1].m_flow heatPump.con.vol.ports[1].p heatPump.con.vol.ports[1].h_outflow heatPump.con.vol.ports[2].m_flow heatPump.con.vol.ports[2].p heatPump.con.vol.ports[2].h_outflow heatPump.con.vol.T heatPump.con.vol.U heatPump.con.vol.p heatPump.con.vol.m heatPump.con.vol.use_C_flow heatPump.con.vol.heatPort.T heatPump.con.vol.heatPort.Q_flow heatPump.con.preDro.allowFlowReversal heatPump.con.preDro.port_a.m_flow heatPump.con.preDro.port_a.p heatPump.con.preDro.port_a.h_outflow heatPump.con.preDro.port_b.m_flow heatPump.con.preDro.port_b.p heatPump.con.preDro.port_b.h_outflow heatPump.con.preDro.m_flow_nominal heatPump.con.preDro.m_flow_small heatPump.con.preDro.m_flow heatPump.con.preDro.dp heatPump.con.preDro.from_dp heatPump.con.preDro.dp_nominal heatPump.con.preDro.linearized heatPump.con.preDro.m_flow_turbulent heatPump.con.preDro.deltaM heatPump.con.preDro.k heatPump.con.is_con heatPump.con.V heatPump.con.use_cap heatPump.con.C heatPump.con.TCap_start heatPump.con.GOut heatPump.con.GInn heatPump.con.preHea.T_ref heatPump.con.preHea.alpha heatPump.con.preHea.Q_flow heatPump.con.preHea.port.T heatPump.con.preHea.port.Q_flow heatPump.con.QFlow_in heatPump.eva.allowFlowReversal heatPump.eva.port_a.m_flow heatPump.eva.port_a.p heatPump.eva.port_a.h_outflow heatPump.eva.port_b.m_flow heatPump.eva.port_b.p heatPump.eva.port_b.h_outflow heatPump.eva.m_flow_nominal heatPump.eva.m_flow_small heatPump.eva.m_flow heatPump.eva.dp heatPump.eva.computeFlowResistance heatPump.eva.from_dp heatPump.eva.dp_nominal heatPump.eva.linearizeFlowResistance heatPump.eva.deltaM heatPump.eva.tau heatPump.eva.energyDynamics heatPump.eva.massDynamics heatPump.eva.p_start heatPump.eva.T_start heatPump.eva.X_start[1] heatPump.eva.vol.energyDynamics heatPump.eva.vol.massDynamics heatPump.eva.vol.substanceDynamics heatPump.eva.vol.traceDynamics heatPump.eva.vol.p_start heatPump.eva.vol.T_start heatPump.eva.vol.X_start[1] heatPump.eva.vol.mSenFac heatPump.eva.vol.prescribedHeatFlowRate heatPump.eva.vol.simplify_mWat_flow heatPump.eva.vol.m_flow_nominal heatPump.eva.vol.nPorts heatPump.eva.vol.m_flow_small heatPump.eva.vol.allowFlowReversal heatPump.eva.vol.V heatPump.eva.vol.ports[1].m_flow heatPump.eva.vol.ports[1].p heatPump.eva.vol.ports[1].h_outflow heatPump.eva.vol.ports[2].m_flow heatPump.eva.vol.ports[2].p heatPump.eva.vol.ports[2].h_outflow heatPump.eva.vol.T heatPump.eva.vol.U heatPump.eva.vol.p heatPump.eva.vol.m heatPump.eva.vol.use_C_flow heatPump.eva.vol.heatPort.T heatPump.eva.vol.heatPort.Q_flow heatPump.eva.preDro.allowFlowReversal heatPump.eva.preDro.port_a.m_flow heatPump.eva.preDro.port_a.p heatPump.eva.preDro.port_a.h_outflow heatPump.eva.preDro.port_b.m_flow heatPump.eva.preDro.port_b.p heatPump.eva.preDro.port_b.h_outflow heatPump.eva.preDro.m_flow_nominal heatPump.eva.preDro.m_flow_small heatPump.eva.preDro.m_flow heatPump.eva.preDro.dp heatPump.eva.preDro.from_dp heatPump.eva.preDro.dp_nominal heatPump.eva.preDro.linearized heatPump.eva.preDro.m_flow_turbulent heatPump.eva.preDro.deltaM heatPump.eva.preDro.k heatPump.eva.is_con heatPump.eva.V heatPump.eva.use_cap heatPump.eva.C heatPump.eva.TCap_start heatPump.eva.GOut heatPump.eva.GInn heatPump.eva.preHea.T_ref heatPump.eva.preHea.alpha heatPump.eva.preHea.Q_flow heatPump.eva.preHea.port.T heatPump.eva.preHea.port.Q_flow heatPump.eva.QFlow_in heatPump.realPassThroughnSetCon.u heatPump.realPassThroughnSetCon.y heatPump.realPassThroughnSetEva.u heatPump.realPassThroughnSetEva.y heatPump.sigBus.nSet heatPump.sigBus.modeSet heatPump.sigBus.onOffMea heatPump.sigBus.TEvaInMea heatPump.sigBus.TConInMea heatPump.sigBus.TEvaOutMea heatPump.sigBus.TConOutMea heatPump.sigBus.PelMea heatPump.sigBus.m_flowEvaMea heatPump.sigBus.m_flowConMea heatPump.sigBus.iceFacMea heatPump.senT_a2.allowFlowReversal heatPump.senT_a2.port_a.m_flow heatPump.senT_a2.port_a.p heatPump.senT_a2.port_a.h_outflow heatPump.senT_a2.port_b.m_flow heatPump.senT_a2.port_b.p heatPump.senT_a2.port_b.h_outflow heatPump.senT_a2.m_flow_nominal heatPump.senT_a2.m_flow_small heatPump.senT_a2.tau heatPump.senT_a2.initType heatPump.senT_a2.T heatPump.senT_a2.der(T) heatPump.senT_a2.T_start heatPump.senT_a2.transferHeat heatPump.senT_a2.TAmb heatPump.senT_a2.tauHeaTra heatPump.senT_b2.allowFlowReversal heatPump.senT_b2.port_a.m_flow heatPump.senT_b2.port_a.p heatPump.senT_b2.port_a.h_outflow heatPump.senT_b2.port_b.m_flow heatPump.senT_b2.port_b.p heatPump.senT_b2.port_b.h_outflow heatPump.senT_b2.m_flow_nominal heatPump.senT_b2.m_flow_small heatPump.senT_b2.tau heatPump.senT_b2.initType heatPump.senT_b2.T heatPump.senT_b2.der(T) heatPump.senT_b2.T_start heatPump.senT_b2.transferHeat heatPump.senT_b2.TAmb heatPump.senT_b2.tauHeaTra heatPump.mFlow_eva.allowFlowReversal heatPump.mFlow_eva.port_a.m_flow heatPump.mFlow_eva.port_a.p heatPump.mFlow_eva.port_a.h_outflow heatPump.mFlow_eva.port_b.m_flow heatPump.mFlow_eva.port_b.p heatPump.mFlow_eva.port_b.h_outflow heatPump.mFlow_eva.m_flow_nominal heatPump.mFlow_eva.m_flow_small heatPump.mFlow_eva.m_flow heatPump.senT_b1.allowFlowReversal heatPump.senT_b1.port_a.m_flow heatPump.senT_b1.port_a.p heatPump.senT_b1.port_a.h_outflow heatPump.senT_b1.port_b.m_flow heatPump.senT_b1.port_b.p heatPump.senT_b1.port_b.h_outflow heatPump.senT_b1.m_flow_nominal heatPump.senT_b1.m_flow_small heatPump.senT_b1.tau heatPump.senT_b1.initType heatPump.senT_b1.T heatPump.senT_b1.der(T) heatPump.senT_b1.T_start heatPump.senT_b1.transferHeat heatPump.senT_b1.TAmb heatPump.senT_b1.tauHeaTra heatPump.senT_a1.allowFlowReversal heatPump.senT_a1.port_a.m_flow heatPump.senT_a1.port_a.p heatPump.senT_a1.port_a.h_outflow heatPump.senT_a1.port_b.m_flow heatPump.senT_a1.port_b.p 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senTAct.der(T) senTAct.T_start senTAct.transferHeat senTAct.TAmb senTAct.tauHeaTra hysHeating.uLow hysHeating.uHigh hysHeating.pre_y_start hysHeating.u hysHeating.y booleanToReal.u booleanToReal.realTrue booleanToReal.realFalse booleanToReal.y sine.amplitude sine.freqHz sine.phase sine.y sine.offset sine.startTime pumSou.energyDynamics pumSou.massDynamics pumSou.substanceDynamics pumSou.traceDynamics pumSou.p_start pumSou.T_start pumSou.X_start[1] pumSou.mSenFac pumSou.allowFlowReversal pumSou.port_a.m_flow pumSou.port_a.p pumSou.port_a.h_outflow pumSou.port_b.m_flow pumSou.port_b.p pumSou.port_b.h_outflow pumSou.m_flow_nominal pumSou.m_flow_small pumSou.m_flow pumSou.dp pumSou.per.pressure.V_flow[1] pumSou.per.pressure.V_flow[2] pumSou.per.pressure.V_flow[3] pumSou.per.pressure.V_flow[4] pumSou.per.pressure.V_flow[5] pumSou.per.pressure.V_flow[6] pumSou.per.pressure.V_flow[7] pumSou.per.pressure.V_flow[8] pumSou.per.pressure.dp[1] pumSou.per.pressure.dp[2] pumSou.per.pressure.dp[3] 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pumSou.computePowerUsingSimilarityLaws pumSou.addPowerToMedium pumSou.nominalValuesDefineDefaultPressureCurve pumSou.tau pumSou.use_inputFilter pumSou.riseTime pumSou.init pumSou.y_start pumSou.y_actual pumSou.P pumSou.heatPort.T pumSou.heatPort.Q_flow pumSou.VMachine_flow pumSou.dpMachine pumSou.eta pumSou.etaHyd pumSou.etaMot pumSou.Nrpm Room.energyDynamics Room.massDynamics Room.substanceDynamics Room.traceDynamics Room.p_start Room.T_start Room.X_start[1] Room.mSenFac Room.prescribedHeatFlowRate Room.simplify_mWat_flow Room.m_flow_nominal Room.nPorts Room.m_flow_small Room.allowFlowReversal Room.V Room.ports[1].m_flow Room.ports[1].p Room.ports[1].h_outflow Room.ports[2].m_flow Room.ports[2].p Room.ports[2].h_outflow Room.T Room.U Room.p Room.m Room.use_C_flow Room.heatPort.T Room.heatPort.Q_flow nIn.k nIn.y heatFlowRateCon.T_ref heatFlowRateCon.alpha heatFlowRateCon.Q_flow heatFlowRateCon.port.T heatFlowRateCon.port.Q_flow gain.k gain.u gain.y not2.u not2.y sinkSideFixedBoundary.nPorts sinkSideFixedBoundary.verifyInputs sinkSideFixedBoundary.ports[1].m_flow sinkSideFixedBoundary.ports[1].p sinkSideFixedBoundary.ports[1].h_outflow sinkSideFixedBoundary.X[1] sinkSideFixedBoundary.p sinkSideFixedBoundary.T iceFac.k iceFac.y logicalSwitch.u1 logicalSwitch.u2 logicalSwitch.u3 logicalSwitch.y hysCooling.uLow hysCooling.uHigh hysCooling.pre_y_start hysCooling.u hysCooling.y sigBus1.nSet sigBus1.modeSet sigBus1.onOffMea sigBus1.TEvaInMea sigBus1.TConInMea sigBus1.TEvaOutMea sigBus1.TConOutMea sigBus1.PelMea sigBus1.m_flowEvaMea sigBus1.m_flowConMea sigBus1.iceFacMea heatPump.innerCycle.PerformanceDataHPCooling.Pel heatPump.innerCycle.PerformanceDataHPCooling.QCon heatPump.innerCycle.PerformanceDataHPCooling.sigBus.nSet heatPump.innerCycle.PerformanceDataHPCooling.sigBus.modeSet heatPump.innerCycle.PerformanceDataHPCooling.sigBus.onOffMea heatPump.innerCycle.PerformanceDataHPCooling.sigBus.TEvaInMea heatPump.innerCycle.PerformanceDataHPCooling.sigBus.TConInMea heatPump.innerCycle.PerformanceDataHPCooling.sigBus.TEvaOutMea heatPump.innerCycle.PerformanceDataHPCooling.sigBus.TConOutMea heatPump.innerCycle.PerformanceDataHPCooling.sigBus.PelMea heatPump.innerCycle.PerformanceDataHPCooling.sigBus.m_flowEvaMea heatPump.innerCycle.PerformanceDataHPCooling.sigBus.m_flowConMea heatPump.innerCycle.PerformanceDataHPCooling.sigBus.iceFacMea heatPump.innerCycle.PerformanceDataHPCooling.QEva heatPump.innerCycle.PerformanceDataHPCooling.smoothness heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[1, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[1, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[1, 3] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[1, 4] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[1, 5] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[1, 6] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[2, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[2, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[2, 3] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[2, 4] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[2, 5] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[2, 6] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[3, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[3, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[3, 3] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[3, 4] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[3, 5] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_con[3, 6] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[1, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[1, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[1, 3] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[1, 4] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[1, 5] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[1, 6] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[2, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[2, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[2, 3] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[2, 4] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[2, 5] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[2, 6] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[3, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[3, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[3, 3] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[3, 4] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[3, 5] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableP_ele[3, 6] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.mFlow_conNom heatPump.innerCycle.PerformanceDataHPCooling.dataTable.mFlow_evaNom heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableUppBou[1, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableUppBou[1, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableUppBou[2, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableUppBou[2, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[1, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[1, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[1, 3] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[1, 4] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[1, 5] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[1, 6] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[2, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[2, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[2, 3] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[2, 4] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[2, 5] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[2, 6] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[3, 1] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[3, 2] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[3, 3] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[3, 4] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[3, 5] heatPump.innerCycle.PerformanceDataHPCooling.dataTable.tableQdot_eva[3, 6] heatPump.innerCycle.PerformanceDataHPCooling.extrapolation heatPump.innerCycle.PerformanceDataHPCooling.printAsserts heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.u1 heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.u2 heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.y heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.extrapolation heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.smoothness heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[1, 1] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[1, 2] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[1, 3] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[1, 4] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[1, 5] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[1, 6] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[2, 1] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[2, 2] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[2, 3] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[2, 4] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[2, 5] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[2, 6] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[3, 1] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[3, 2] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[3, 3] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[3, 4] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[3, 5] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.table[3, 6] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.u1 heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.u2 heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.y heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.tableOnFile heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[1, 1] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[1, 2] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[1, 3] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[1, 4] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[1, 5] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[1, 6] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[2, 1] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[2, 2] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[2, 3] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[2, 4] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[2, 5] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[2, 6] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[3, 1] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[3, 2] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[3, 3] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[3, 4] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[3, 5] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.table[3, 6] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.verboseRead heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.smoothness heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.extrapolation heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.verboseExtrapolationheatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.u_min[1] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.u_min[2] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.u_max[1] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.combiTable2D.u_max[2] heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.realPassThrough2.u heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.realPassThrough2.y heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.realPassThrough1.u heatPump.innerCycle.PerformanceDataHPCooling.Qdot_EvaTable.realPassThrough1.y heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.u1 heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.u2 heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.y heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.extrapolation heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.smoothness heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[1, 1] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[1, 2] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[1, 3] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[1, 4] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[1, 5] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[1, 6] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[2, 1] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[2, 2] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[2, 3] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[2, 4] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[2, 5] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[2, 6] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[3, 1] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[3, 2] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[3, 3] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[3, 4] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[3, 5] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.table[3, 6] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.u1 heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.u2 heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.y heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.tableOnFile heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[1, 1] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[1, 2] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[1, 3] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[1, 4] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[1, 5] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[1, 6] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[2, 1] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[2, 2] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[2, 3] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[2, 4] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[2, 5] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[2, 6] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[3, 1] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[3, 2] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[3, 3] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[3, 4] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[3, 5] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.table[3, 6] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.verboseRead heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.smoothness heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.extrapolation heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.verboseExtrapolation heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.u_min[1] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.u_min[2] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.u_max[1] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.combiTable2D.u_max[2] heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.realPassThrough2.u heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.realPassThrough2.y heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.realPassThrough1.u heatPump.innerCycle.PerformanceDataHPCooling.P_eleTable.realPassThrough1.y heatPump.innerCycle.PerformanceDataHPCooling.t_Co_in.u heatPump.innerCycle.PerformanceDataHPCooling.t_Co_in.y heatPump.innerCycle.PerformanceDataHPCooling.t_Ev_ou.u heatPump.innerCycle.PerformanceDataHPCooling.t_Ev_ou.y heatPump.innerCycle.PerformanceDataHPCooling.nTimesPel.u1 heatPump.innerCycle.PerformanceDataHPCooling.nTimesPel.u2 heatPump.innerCycle.PerformanceDataHPCooling.nTimesPel.y heatPump.innerCycle.PerformanceDataHPCooling.nTimesQEva.u1 heatPump.innerCycle.PerformanceDataHPCooling.nTimesQEva.u2 heatPump.innerCycle.PerformanceDataHPCooling.nTimesQEva.y heatPump.innerCycle.PerformanceDataHPCooling.proRedQEva.u1 heatPump.innerCycle.PerformanceDataHPCooling.proRedQEva.u2 heatPump.innerCycle.PerformanceDataHPCooling.proRedQEva.y heatPump.innerCycle.PerformanceDataHPCooling.calcRedQCon.u1 heatPump.innerCycle.PerformanceDataHPCooling.calcRedQCon.u2 heatPump.innerCycle.PerformanceDataHPCooling.calcRedQCon.y heatPump.innerCycle.PerformanceDataHPCooling.calcRedQCon.k1 heatPump.innerCycle.PerformanceDataHPCooling.calcRedQCon.k2 heatPump.innerCycle.PerformanceDataHPCooling.nTimesSF.u1 heatPump.innerCycle.PerformanceDataHPCooling.nTimesSF.u2 heatPump.innerCycle.PerformanceDataHPCooling.nTimesSF.y heatPump.innerCycle.gainCon.k heatPump.innerCycle.gainCon.u heatPump.innerCycle.gainCon.y 3 n description Time in [s] Number of ports [:#(type=Integer)] Set to true to stop the simulation with an error if the medium temperature is outside its allowable range [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Fixed value of composition [kg/kg] Fixed mass flow rate going out of the fluid port [kg/s] Fixed value of temperature [K|degC] Prescribed boundary temperature [K|degC] Number of ports [:#(type=Integer)] Set to true to stop the simulation with an error if the medium temperature is outside its allowable range [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Fixed value of composition [kg/kg] Fixed value of pressure [Pa|bar] Fixed value of temperature [K|degC] Height of ramps Duration of ramp (= 0.0 gives a Step) [s] Connector of Real output signal Offset of output signal y Output y = offset for time < startTime [s] Constant output value Connector of Real output signal = false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1 [:#(type=Boolean)] = false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2 [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate [kg/s] Nominal mass flow rate [kg/s] Small mass flow rate for regularization of zero flow [kg/s] Small mass flow rate for regularization of zero flow [kg/s] Mass flow rate from port_a1 to port_b1 (m1_flow > 0 is design flow direction) [kg/s] Pressure difference between port_a1 and port_b1 [Pa|Pa] Mass flow rate from port_a2 to port_b2 (m2_flow > 0 is design flow direction) [kg/s] Pressure difference between port_a2 and port_b2 [Pa|Pa] True if the vapour compression machine is reversible [:#(type=Boolean)] Scaling factor of vapour compression machine Relative rotational speed of compressor between 0 and 1 Current operation mode: true: main operation mode, false: reversible operation mode [:#(type=Boolean)] Measured value of device being on or off (relative speed greater than 0) [:#(type=Boolean)] Temperature of flow into evaporator [K;degC] Temperature of flow into condenser [K;degC] temperature of flow out of evaporator [K;degC] Temperature of flow out of condenser [K;degC] Total electrical active power [W] Mass flow rate through evaporator [kg/s] Mass flow rate through condenser [kg/s] Efficiency factor (0..1) to estimate influence of icing. 0 means no heat is transferred through heat exchanger (fully frozen). 1 means no icing/frosting. Heat Flow to condenser [W|kW] Heat flow from evaporator [W|kW] Connector of first Real input signal [W|kW] Connector of Boolean input signal [:#(type=Boolean)] Connector of second Real input signal [W|kW] Connector of Real output signal [W|kW] Connector of first Real input signal [W|kW] Connector of Boolean input signal [:#(type=Boolean)] Connector of second Real input signal [W|kW] Connector of Real output signal [W|kW] Electrical power consumed by compressor [W|kW] Connector of first Real input signal [W|kW] Connector of Boolean input signal [:#(type=Boolean)] Connector of second Real input signal [W|kW] Connector of Real output signal [W|kW] Electrical Power consumed by HP [W|kW] Heat flow rate through Condenser [W|kW] Relative rotational speed of compressor between 0 and 1 Current operation mode: true: main operation mode, false: reversible operation mode [:#(type=Boolean)] Measured value of device being on or off (relative speed greater than 0) [:#(type=Boolean)] Temperature of flow into evaporator [K;degC] Temperature of flow into condenser [K;degC] temperature of flow out of evaporator [K;degC] Temperature of flow out of condenser [K;degC] Total electrical active power [W] Mass flow rate through evaporator [kg/s] Mass flow rate through condenser [kg/s] Efficiency factor (0..1) to estimate influence of icing. 0 means no heat is transferred through heat exchanger (fully frozen). 1 means no icing/frosting. Heat flow rate through Evaporator [W|kW] Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal Gain of input signal 1 Gain of input signal 2 Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal Nominal heating power of heat pump [W] Interpolation method [:#(type=SDF.Types.InterpolationMethod)] Extrapolation method [:#(type=SDF.Types.ExtrapolationMethod)] Nominal heat flow in map. Doesn't need to be changed. [W] Minimal possible COP value. Used to avoid division by zero error. Should never occur anyways if performance map is correctly created Connector of first Real input signal Connector of Boolean input signal [:#(type=Boolean)] Connector of second Real input signal Connector of Real output signal Connector of first Real input signal Connector of Boolean input signal [:#(type=Boolean)] Connector of second Real input signal Connector of Real output signal Constant output value Connector of Real output signal Constant output value Connector of Real output signal Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal Number of inputs [:#(type=Integer)] Connector of Real input signals Connector of Real input signals Connector of Real input signals Connector of Real output signal Read data from file [:#(type=Boolean)] Interpolation method [:#(type=SDF.Types.InterpolationMethod)] Extrapolation method [:#(type=SDF.Types.ExtrapolationMethod)] Table data (as returned by readTableData()) Number of inputs [:#(type=Integer)] Connector of Real input signals Connector of Real input signals Connector of Real input signals Connector of Real output signal Read data from file [:#(type=Boolean)] Interpolation method [:#(type=SDF.Types.InterpolationMethod)] Extrapolation method [:#(type=SDF.Types.ExtrapolationMethod)] Table data (as returned by readTableData()) Dimension of input signal connector 1 [:#(type=Integer)] Dimension of input signal connector 2 [:#(type=Integer)] Dimension of input signal connector 3 [:#(type=Integer)] Connector of Real input signals 1 Connector of Real input signals 2 Connector of Real input signals 3 Connector of Real output signals Connector of Real output signals Connector of Real output signals Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal Constant output value Connector of Real output signal Gain value multiplied with input signal [1] Input signal connector Output signal connector Is the vapour compression machine reversible? [:#(type=Boolean)] Enable automatic estimation of volumes and mass flows? [:#(type=Boolean)] Nominal usable heat flow of the vapour compression machine (HP: Heating; Chiller: Cooling) [W] Scaling-factor of vapour compression machine Consider the inertia of the refrigerant cycle [:#(type=Boolean)] Cut off frequency for inertia of refrigerant cycle [Hz] Order of refrigerant cycle interia [:#(type=Integer)] Set true to use bus connector for modeSet, nSet and iceFac input [:#(type=Boolean)] Manual input of the nominal mass flow rate (if not automatically calculated) [kg/s] Manual input of the condenser volume (if not automatically calculated) [m3] Pressure drop at nominal mass flow rate [Pa|bar] Fraction of nominal mass flow rate where transition to turbulent occurs If heat losses at capacitor side are considered or not [:#(type=Boolean)] Heat capacity of Condenser (= cp*m). If you want to neglace the dry mass of the condenser, you can set this value to zero [J/K] Constant parameter for heat transfer to the ambient. Represents a sum of thermal resistances such as conductance, insulation and natural convection. If you want to simulate a condenser with additional dry mass but without external heat losses, set the value to zero [W/K] Constant parameter for heat transfer to heat exchangers capacity. Represents a sum of thermal resistances such as forced convection and conduction inside of the capacity [W/K] Manual input of the nominal mass flow rate (if not automatically calculated) [kg/s] Manual input of the evaporator volume (if not automatically calculated) [m3] Pressure drop at nominal mass flow rate [Pa|bar] Fraction of nominal mass flow rate where transition to turbulent occurs If heat losses at capacitor side are considered or not [:#(type=Boolean)] Heat capacity of Evaporator (= cp*m). If you want to neglace the dry mass of the evaporator, you can set this value to zero [J/K] Constant parameter for heat transfer to the ambient. Represents a sum of thermal resistances such as conductance, insulation and natural convection. If you want to simulate a evaporator with additional dry mass but without external heat losses, set the value to zero [W/K]Constant parameter for heat transfer to heat exchangers capacity. Represents a sum of thermal resistances such as forced convection and conduction inside of the capacity [W/K] Time constant at nominal flow rate (use tau=0 for steady-state sensor, but see user guide for potential problems) [s] If true, temperature T converges towards TAmb when no flow [:#(type=Boolean)] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Time constant for heat transfer in temperature sensors in evaporator, default 20 minutes [s] Fixed ambient temperature for heat transfer of sensors at the evaporator side [K|degC] Time constant for heat transfer in temperature sensors in condenser, default 20 minutes [s] Fixed ambient temperature for heat transfer of sensors at the condenser side [K|degC] Type of initialization (InitialState and InitialOutput are identical) [:#(type=Modelica.Blocks.Types.Init)] Start value of pressure [Pa|bar] Start value of temperature [K|degC] Initial temperature of heat capacity of condenser [K|degC] Start value of mass fractions m_i/m [kg/kg] Start value of pressure [Pa|bar] Start value of temperature [K|degC] Initial temperature of heat capacity at evaporator [K|degC] Start value of mass fractions m_i/m [kg/kg] Initial or guess values of states Initial or guess values of states Initial or guess values of states Initial or guess value of output (= state) Type of mass balance: dynamic (3 initialization options) or steady state (only affects fluid-models) [:#(type=Modelica.Fluid.Types.Dynamics)] Type of energy balance: dynamic (3 initialization options) or steady state (only affects fluid-models) [:#(type=Modelica.Fluid.Types.Dynamics)] =true if heat pump; =false if chiller [:#(type=Boolean)] = true, if actual temperature at port is computed [:#(type=Boolean)] = true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] = true, use homotopy method [:#(type=Boolean)] = true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate [kg/s] Small mass flow rate for regularization of zero flow [kg/s] Mass flow rate from port_a to port_b (m_flow > 0 is design flow direction) [kg/s] Pressure difference between port_a and port_b [Pa|Pa] =true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] = true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] Pressure difference [Pa|Pa] = true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] Fraction of nominal flow rate where flow transitions to laminar Time constant at nominal flow (if energyDynamics <> SteadyState) [s] Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Start value of pressure [Pa|bar] Start value of temperature [K|degC] Start value of mass fractions m_i/m [kg/kg] Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Start value of pressure [Pa|bar] Start value of temperature [K|degC] Start value of mass fractions m_i/m [kg/kg] Factor for scaling the sensible thermal mass of the volume Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] Nominal mass flow rate [kg/s] Number of ports [:#(type=Integer)] Small mass flow rate for regularization of zero flow [kg/s] = false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] Volume [m3] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Temperature of the fluid [K|degC] Internal energy of the component [J] Pressure of the fluid [Pa|bar] Mass of the component [kg] Set to true to enable input connector for trace substance [:#(type=Boolean)] Port temperature [K|degC] Heat flow rate (positive if flowing from outside into the component) [W] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate [kg/s] Small mass flow rate for regularization of zero flow [kg/s] Mass flow rate from port_a to port_b (m_flow > 0 is design flow direction) [kg/s] Pressure difference between port_a and port_b [Pa|Pa] = true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] Pressure drop at nominal mass flow rate [Pa|Pa] = true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] Fraction of nominal mass flow rate where transition to turbulent occurs Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2) Type of heat exchanger [:#(type=Boolean)] Volume in condenser [m3] False if capacity and heat losses are neglected [:#(type=Boolean)] Capacity of heat exchanger. If you want to neglace the dry mass of the heat exchanger, you can set this value to zero [J/K] Initial temperature of heat capacity [K|degC] Formular for calculation of heat transfer coefficient on the outside. If you want to simulate a heat exchanger with additional dry mass but without external heat losses, set the value to zero [W/K] Formular for calculation of heat transfer coefficient on the inside Reference temperature [K|degC] Temperature coefficient of heat flow rate [1/K] [W] Port temperature [K|degC] Heat flow rate (positive if flowing from outside into the component) [W] Heat flow rate to the medium = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate [kg/s] Small mass flow rate for regularization of zero flow [kg/s] Mass flow rate from port_a to port_b (m_flow > 0 is design flow direction) [kg/s] Pressure difference between port_a and port_b [Pa|Pa] =true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] = true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] Pressure difference [Pa|Pa] = true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] Fraction of nominal flow rate where flow transitions to laminar Time constant at nominal flow (if energyDynamics <> SteadyState) [s] Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Start value of pressure [Pa|bar] Start value of temperature [K|degC] Start value of mass fractions m_i/m [kg/kg] Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Start value of pressure [Pa|bar] Start value of temperature [K|degC] Start value of mass fractions m_i/m [kg/kg] Factor for scaling the sensible thermal mass of the volume Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] Nominal mass flow rate [kg/s] Number of ports [:#(type=Integer)] Small mass flow rate for regularization of zero flow [kg/s] = false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] Volume [m3] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Temperature of the fluid [K|degC] Internal energy of the component [J] Pressure of the fluid [Pa|bar] Mass of the component [kg] Set to true to enable input connector for trace substance [:#(type=Boolean)] Port temperature [K|degC] Heat flow rate (positive if flowing from outside into the component) [W] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate [kg/s] Small mass flow rate for regularization of zero flow [kg/s] Mass flow rate from port_a to port_b (m_flow > 0 is design flow direction) [kg/s] Pressure difference between port_a and port_b [Pa|Pa] = true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] Pressure drop at nominal mass flow rate [Pa|Pa] = true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] Fraction of nominal mass flow rate where transition to turbulent occurs Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2) Type of heat exchanger [:#(type=Boolean)] Volume in condenser [m3] False if capacity and heat losses are neglected [:#(type=Boolean)] Capacity of heat exchanger. If you want to neglace the dry mass of the heat exchanger, you can set this value to zero [J/K] Initial temperature of heat capacity [K|degC] Formular for calculation of heat transfer coefficient on the outside. If you want to simulate a heat exchanger with additional dry mass but without external heat losses, set the value to zero [W/K] Formular for calculation of heat transfer coefficient on the inside Reference temperature [K|degC] Temperature coefficient of heat flow rate [1/K] [W] Port temperature [K|degC] Heat flow rate (positive if flowing from outside into the component) [W] Heat flow rate to the medium Connector of Real input signal Connector of Real output signal Connector of Real input signal Connector of Real output signal Relative rotational speed of compressor between 0 and 1 Current operation mode: true: main operation mode, false: reversible operation mode [:#(type=Boolean)] Measured value of device being on or off (relative speed greater than 0) [:#(type=Boolean)] Temperature of flow into evaporator [K;degC] Temperature of flow into condenser [K;degC] temperature of flow out of evaporator [K;degC] Temperature of flow out of condenser [K;degC] Total electrical active power [W] Mass flow rate through evaporator [kg/s] Mass flow rate through condenser [kg/s] Efficiency factor (0..1) to estimate influence of icing. 0 means no heat is transferred through heat exchanger (fully frozen). 1 means no icing/frosting. = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate, used for regularization near zero flow [kg/s] For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] Time constant at nominal flow rate (use tau=0 for steady-state sensor, but see user guide for potential problems) [s] Type of initialization (InitialState and InitialOutput are identical) [:#(type=Modelica.Blocks.Types.Init)] Temperature of the passing fluid [K|degC] der(Temperature of the passing fluid) [K/s] Initial or guess value of output (= state) [K|degC] if true, temperature T converges towards TAmb when no flow [:#(type=Boolean)] Fixed ambient temperature for heat transfer [K|degC] Time constant for heat transfer, default 20 minutes [s] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate, used for regularization near zero flow [kg/s] For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] Time constant at nominal flow rate (use tau=0 for steady-state sensor, but see user guide for potential problems) [s] Type of initialization (InitialState and InitialOutput are identical) [:#(type=Modelica.Blocks.Types.Init)] Temperature of the passing fluid [K|degC] der(Temperature of the passing fluid) [K/s] Initial or guess value of output (= state) [K|degC] if true, temperature T converges towards TAmb when no flow [:#(type=Boolean)] Fixed ambient temperature for heat transfer [K|degC] Time constant for heat transfer, default 20 minutes [s] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate, used for regularization near zero flow [kg/s] For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] Mass flow rate from port_a to port_b [kg/s] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate, used for regularization near zero flow [kg/s] For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] Time constant at nominal flow rate (use tau=0 for steady-state sensor, but see user guide for potential problems) [s] Type of initialization (InitialState and InitialOutput are identical) [:#(type=Modelica.Blocks.Types.Init)] Temperature of the passing fluid [K|degC] der(Temperature of the passing fluid) [K/s] Initial or guess value of output (= state) [K|degC] if true, temperature T converges towards TAmb when no flow [:#(type=Boolean)] Fixed ambient temperature for heat transfer [K|degC] Time constant for heat transfer, default 20 minutes [s] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate, used for regularization near zero flow [kg/s] For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] Time constant at nominal flow rate (use tau=0 for steady-state sensor, but see user guide for potential problems) [s] Type of initialization (InitialState and InitialOutput are identical) [:#(type=Modelica.Blocks.Types.Init)] Temperature of the passing fluid [K|degC] der(Temperature of the passing fluid) [K/s] Initial or guess value of output (= state) [K|degC] if true, temperature T converges towards TAmb when no flow [:#(type=Boolean)] Fixed ambient temperature for heat transfer [K|degC] Time constant for heat transfer, default 20 minutes [s] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate, used for regularization near zero flow [kg/s] For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] Mass flow rate from port_a to port_b [kg/s] Comparison with respect to threshold Connector of Real input signal Connector of Boolean output signal [:#(type=Boolean)] Time instant of step start [s] Output before startTime [:#(type=Boolean)] Connector of Boolean output signal [:#(type=Boolean)] = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate, used for regularization near zero flow [kg/s] For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] Time constant at nominal flow rate (use tau=0 for steady-state sensor, but see user guide for potential problems) [s] Type of initialization (InitialState and InitialOutput are identical) [:#(type=Modelica.Blocks.Types.Init)] Temperature of the passing fluid [K|degC] der(Temperature of the passing fluid) [K/s] Initial or guess value of output (= state) [K|degC] if true, temperature T converges towards TAmb when no flow [:#(type=Boolean)] Fixed ambient temperature for heat transfer [K|degC] Time constant for heat transfer, default 20 minutes [s] if y=true and u<=uLow, switch to y=false if y=false and u>=uHigh, switch to y=true Value of pre(y) at initial time [:#(type=Boolean)] [:#(type=Boolean)] Connector of Boolean input signal [:#(type=Boolean)] Output signal for true Boolean input Output signal for false Boolean input Connector of Real output signal Amplitude of sine wave Frequency of sine wave [Hz] Phase of sine wave [rad|deg] Connector of Real output signal Offset of output signal y Output y = offset for time < startTime [s] Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Start value of pressure [Pa|bar] Start value of temperature [K|degC] Start value of mass fractions m_i/m [kg/kg] Factor for scaling the sensible thermal mass of the volume = false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Nominal mass flow rate [kg/s] Small mass flow rate for regularization of zero flow [kg/s] Mass flow rate from port_a to port_b (m_flow > 0 is design flow direction) [kg/s] Pressure difference between port_a and port_b [Pa|Pa] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Fan or pump total pressure at these flow rates [Pa|Pa] Fan or pump total pressure at these flow rates [Pa|Pa] Fan or pump total pressure at these flow rates [Pa|Pa] Fan or pump total pressure at these flow rates [Pa|Pa] Fan or pump total pressure at these flow rates [Pa|Pa] Fan or pump total pressure at these flow rates [Pa|Pa] Fan or pump total pressure at these flow rates [Pa|Pa] Fan or pump total pressure at these flow rates [Pa|Pa] Use power data instead of motor efficiency [:#(type=Boolean)] Volumetric flow rate at user-selected operating points [m3/s] Fan or pump efficiency at these flow rates [1] Volumetric flow rate at user-selected operating points [m3/s] Fan or pump efficiency at these flow rates [1] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Volume flow rate at user-selected operating points [m3/s] Fan or pump electrical power at these flow rates [W] Fan or pump electrical power at these flow rates [W] Fan or pump electrical power at these flow rates [W] Fan or pump electrical power at these flow rates [W] Fan or pump electrical power at these flow rates [W] Fan or pump electrical power at these flow rates [W] Fan or pump electrical power at these flow rates [W] Fan or pump electrical power at these flow rates [W] If true, then motor heat is added to fluid stream [:#(type=Boolean)] Nominal rotational speed for flow characteristic [1] Normalized speed set point, used if inputType = AixLib.Fluid.Types.InputType.Constant [1] Vector of normalized speed set points, used if inputType = AixLib.Fluid.Types.InputType.Stages [1] Nominal rotational speed for flow characteristic [rev/min] Speed set point, used if inputType = AixLib.Fluid.Types.InputType.Constant [rev/min] Vector of speed set points, used if inputType = AixLib.Fluid.Types.InputType.Stages [rev/min] = true, if default record values are being used [:#(type=Boolean)] Control input type [:#(type=AixLib.Fluid.Types.InputType)] Constant input set point [1] Vector of input set points corresponding to stages [1] = true, compute power exactly, using similarity laws. Otherwise approximate. [:#(type=Boolean)] Set to false to avoid any power (=heat and flow work) being added to medium (may give simpler equations) [:#(type=Boolean)] Set to true to avoid warning if m_flow_nominal and dp_nominal are used to construct the default pressure curve [:#(type=Boolean)] Time constant of fluid volume for nominal flow, used if energy or mass balance is dynamic [s] = true, if speed is filtered with a 2nd order CriticalDamping filter [:#(type=Boolean)] Rise time of the filter (time to reach 99.6 % of the speed) [s] Type of initialization (no init/steady state/initial state/initial output) [:#(type=Modelica.Blocks.Types.Init)] Initial value of speed [1] Actual normalised pump speed that is used for computations [1] Electrical power consumed [W] Port temperature [K|degC] Heat flow rate (positive if flowing from outside into the component) [W] Volume flow rate [m3/s] Pressure difference [Pa|Pa] Global efficiency [1] Hydraulic efficiency [1] Motor efficiency [1] Prescribed rotational speed [1/min] Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Start value of pressure [Pa|bar] Start value of temperature [K|degC] Start value of mass fractions m_i/m [kg/kg] Factor for scaling the sensible thermal mass of the volume Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] Nominal mass flow rate [kg/s] Number of ports [:#(type=Integer)] Small mass flow rate for regularization of zero flow [kg/s] = false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] Volume [m3] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Temperature of the fluid [K|degC] Internal energy of the component [J] Pressure of the fluid [Pa|bar] Mass of the component [kg] Set to true to enable input connector for trace substance [:#(type=Boolean)] Port temperature [K|degC] Heat flow rate (positive if flowing from outside into the component) [W] Constant output value Connector of Real output signal Reference temperature [K|degC] Temperature coefficient of heat flow rate [1/K] [W] Port temperature [K|degC] Heat flow rate (positive if flowing from outside into the component) [W] Gain value multiplied with input signal [1] Input signal connector Output signal connector Connector of Boolean input signal [:#(type=Boolean)] Connector of Boolean output signal [:#(type=Boolean)] Number of ports [:#(type=Integer)] Set to true to stop the simulation with an error if the medium temperature is outside its allowable range [:#(type=Boolean)] Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] Fixed value of composition [kg/kg] Fixed value of pressure [Pa|bar] Fixed value of temperature [K|degC] Constant output value Connector of Real output signal Connector of first Boolean input signal [:#(type=Boolean)] Connector of second Boolean input signal [:#(type=Boolean)] Connector of third Boolean input signal [:#(type=Boolean)] Connector of Boolean output signal [:#(type=Boolean)] if y=true and u<=uLow, switch to y=false if y=false and u>=uHigh, switch to y=true Value of pre(y) at initial time [:#(type=Boolean)] [:#(type=Boolean)] Relative rotational speed of compressor between 0 and 1 Current operation mode: true: main operation mode, false: reversible operation mode [:#(type=Boolean)] Measured value of device being on or off (relative speed greater than 0) [:#(type=Boolean)] Temperature of flow into evaporator [K;degC] Temperature of flow into condenser [K;degC] temperature of flow out of evaporator [K;degC] Temperature of flow out of condenser [K;degC] Total electrical active power [W] Mass flow rate through evaporator [kg/s] Mass flow rate through condenser [kg/s] Efficiency factor (0..1) to estimate influence of icing. 0 means no heat is transferred through heat exchanger (fully frozen). 1 means no icing/frosting. Electrical Power consumed by HP [W|kW] Heat flow rate through Condenser [W|kW] Relative rotational speed of compressor between 0 and 1 Current operation mode: true: main operation mode, false: reversible operation mode [:#(type=Boolean)] Measured value of device being on or off (relative speed greater than 0) [:#(type=Boolean)] Temperature of flow into evaporator [K;degC] Temperature of flow into condenser [K;degC] temperature of flow out of evaporator [K;degC] Temperature of flow out of condenser [K;degC] Total electrical active power [W] Mass flow rate through evaporator [kg/s] Mass flow rate through condenser [kg/s] Efficiency factor (0..1) to estimate influence of icing. 0 means no heat is transferred through heat exchanger (fully frozen). 1 means no icing/frosting. Heat flow rate through Evaporator [W|kW] Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Heating power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Electrical power table; T in degC; Q_flow in W Nominal mass flow rate in condenser [kg/s] Nominal mass flow rate in evaporator [kg/s] Points to define upper boundary for sink temperature Points to define upper boundary for sink temperature Points to define upper boundary for sink temperature Points to define upper boundary for sink temperature Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W Cooling power table; T in degC; Q_flow in W False to hold last value [:#(type=Boolean)] WARNING: This will lead to a lot of state-events if extrapolation occurs frequently! If extrapolation is enabled, the user will get warnings when extrapolation occurs. [:#(type=Boolean)] Connector of Real input signal 1 [degC] Connector of Real input signal 2 [degC] Connector of Real output signal [W|kW] False to hold last value [:#(type=Boolean)] Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal = true, if table is defined on file or in function usertab [:#(type=Boolean)] Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) = true, if info message that file is loading is to be printed [:#(type=Boolean)] Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] Extrapolation of data outside the definition range [:#(type=Modelica.Blocks.Types.Extrapolation)] = true, if warning messages are to be printed if table input is outside the definition range [:#(type=Boolean)] Minimum abscissa value defined in table Minimum abscissa value defined in table Maximum abscissa value defined in table Maximum abscissa value defined in table Connector of Real input signal Connector of Real output signal Connector of Real input signal Connector of Real output signal Connector of Real input signal 1 [degC] Connector of Real input signal 2 [degC] Connector of Real output signal [W|kW] False to hold last value [:#(type=Boolean)] Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1]) Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal = true, if table is defined on file or in function usertab [:#(type=Boolean)] Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0, 0; 0, 1]) = true, if info message that file is loading is to be printed [:#(type=Boolean)] Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] Extrapolation of data outside the definition range [:#(type=Modelica.Blocks.Types.Extrapolation)] = true, if warning messages are to be printed if table input is outside the definition range [:#(type=Boolean)] Minimum abscissa value defined in table Minimum abscissa value defined in table Maximum abscissa value defined in table Maximum abscissa value defined in table Connector of Real input signal Connector of Real output signal Connector of Real input signal Connector of Real output signal Connector of Real input signal to be converted [K] Connector of Real output signal containing input signal u in another unit [degC] Connector of Real input signal to be converted [K] Connector of Real output signal containing input signal u in another unit [degC] Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal Gain of input signal 1 Gain of input signal 2 Connector of Real input signal 1 Connector of Real input signal 2 Connector of Real output signal Gain value multiplied with input signal [1] Input signal connector Output signal connector n dataInfo ���� ���� ���� @ ����
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