| Boolean | alpha_input | false | |
| Integer | nShot | 2 | number of species which are equal in vapour and liquid phase |
| Integer | nScold | 2 | number of species which are equal in vapour and liquid phase |
| Integer | nLhot | nSLhot - nShot | number of additional substances which are only in liquid phase |
| Integer | nLcold | nSLcold - nScold | number of additional substances which are only in liquid phase |
| Integer | nSLhot | MediumLiquidHot.nSubstance | |
| Integer | nSLcold | MediumLiquidCold.nSubstance | |
| SI.Density | rhoHotLiquid_nom | MediumLiquidHot.DensityWater(p = pLiquid_nom, T = ThotLiquidOut_nom) | |
| SI.Density | rhoColdLiquid_nom | MediumLiquidCold.DensityWater(p = pLiquid_nom, T = TcoldLiquidOut_nom) | |
| SI.Length | dummyDiameter | 0.0254 | diameter is abitrary |
| SI.Length | hotLiquidTubeLength | volumeHotLiquid/(0.25*Modelica.Constants.pi*dummyDiameter^2) | |
| SI.Length | coldLiquidTubeLength | volumeColdLiquid/(0.25*Modelica.Constants.pi*dummyDiameter^2) | |
| SI.Area | CrossSectionArea | Modelica.Constants.pi*dummyDiameter^2/4 | |
| Real | zetaHotLiquid | (dpHotLiquid*CrossSectionArea^2*2*dummyDiameter)/((mFlowHotLiquid_nom/rhoHotLiquid_nom)^2*hotLiquidTubeLength*rhoHotLiquid_nom) | |
| Real | zetaHotLiquid_haiko | Modelica.Constants.pi^2*dummyDiameter^5/(8*hotLiquidTubeLength)*(dpHotLiquid*rhoHotLiquid_nom/mFlowHotLiquid_nom^2) | |
| Real | zetaColdLiquid | Modelica.Constants.pi^2*dummyDiameter^5/(8*coldLiquidTubeLength)*(dpColdLiquid*rhoColdLiquid_nom/mFlowColdLiquid_nom^2) | |
| Boolean | ss_hot_c2 | true | true if c_l[2] of the hot liquid is to be a state |
| Boolean | ss_cold_c2 | true | true if c_l[2] of the cold liquid is to be a state |
| Geometry |
| SI.Mass | plateMetalMass | 310 | |
| SI.SpecificHeatCapacity | cpMetal | 500 | |
| SI.Volume | volumeHotLiquid | 11e-3 | |
| SI.Volume | volumeColdLiquid | 11e-3 | |
| SI.Area | surfaceArea | 10.4 | |
| nominal operating point |
| SI.Pressure | dpHotLiquid | 2e5 | |
| SI.Pressure | dpColdLiquid | 2e5 | |
| SI.MassFlowRate | mFlowHotLiquid_nom | 0.3 | |
| SI.MassFlowRate | mFlowColdLiquid_nom | 0.3 | |
| SI.Temperature | ThotLiquidOut_nom | ThotLiquid_start | |
| SI.Temperature | TcoldLiquidOut_nom | TcoldLiquid_start | |
| SI.AbsolutePressure | pLiquid_nom | 4e5 | |
| Initialization |
| SI.Temperature | ThotLiquidIn_start | 104 + 273.15 | |
| SI.Temperature | TcoldLiquidIn_start | 51 + 273.15 | |
| SI.Temperature | ThotLiquid_start | 56 + 273.15 | |
| SI.Temperature | TcoldLiquid_start | 98 + 273.15 | |
| SI.Concentration[nSLhot] | c_l_start_hot | {5, 40000} | initial value for concentration of hot liquid |
| SI.Concentration[nSLcold] | c_l_start_cold | {5, 40000} | initial value for concentration of cold liquid |
MediumLiquidCold