| Boolean | fixLiquidLevel (from VesselLevel) | true | if true, liquid height will be fixed to liquidL |
| SI.Height | liquidL (from VesselLevel) | 0 | fixed liquid level over lowest vessel point |
| Boolean | fixLiquidVolume (from VesselLevel) | false | if true, liquid volume will be fixed to liquidV. Do not fix height and volume simultaneously |
| SI.Volume | liquidV (from VesselLevel) | 0 | fixed liquid volume |
| Nozzles config |
| Modelica.Units.SI.Height | inletL (from VesselFlow) | 0 | inlet height over lowest internal point of the vessel |
| Modelica.Units.SI.Height | outletL (from VesselFlow) | 0 | outlet height over lowest internal point of the vessel |
| Modelica.Units.SI.Height | overflowL (from VesselFlow) | 0 | overflow height over lowest internal point of the vessel |
| Modelica.Units.SI.Height | ventOutL (from VesselFlow) | 0 | overflow height over lowest internal point of the vessel |
| Boolean | useVentIn (from VesselFlow) | false | |
| Operations |
| Modelica.Units.SI.ThermalConductance | lgConductance (from VesselFlow) | 0 | thermal conductange at the liquid-gas interface |
| Initialization |
| SI.Volume | vesselVolume (from VesselFlow) | 1.0 | total volume of the vessel |
| SI.Volume | initialLiquidVolume (from VesselFlow) | 1.0 | initial volume of liquid in the vessel |
| SI.Mass | initialLiquidMass (from VesselFlow) | initialLiquidVolume*MediumL.density(MediumL.setState_pTX(initialP, initialT)) | initial vessel liquid mass |
| SI.Mass | initialGasMass (from VesselFlow) | (vesselVolume - initialLiquidVolume)*MediumG.density(MediumG.setState_pTX(initialP, initialT)) | initial vessel gas mass |
| SI.Temperature | initialT (from VesselFlow) | 298 | initial temperature of the vessel liquid |
| SI.AbsolutePressure | initialP (from VesselFlow) | 101325 | initial vessel pressure in the gas phase |
| Modelica.Units.SI.Energy | initialLiquidEnthalpy (from VesselFlow) | initialLiquidMass*MediumL.specificEnthalpy(MediumL.setState_pTX(initialP, initialT)) | |
| Modelica.Units.SI.Energy | initialGasEnthalpy (from VesselFlow) | initialGasMass*MediumG.specificEnthalpy(MediumG.setState_pTX(initialP, initialT)) | |
| Shell data |
| Boolean | isVertical (from VesselPhysical) | true | if true, the shell is considered vertical, otherwise horizontal |
| Types.VesselForm | vesselForm (from VesselPhysical) | Types.VesselForm.cylinder | |
| Modelica.Units.SI.Diameter | di (from VesselPhysical) | 0 | internal diameter, if cylinder or sphere |
| Modelica.Units.SI.Area | section (from VesselPhysical) | 0 | if prism |
| Modelica.Units.SI.Length | perimeter (from VesselPhysical) | 0 | if prism |
| Modelica.Units.SI.Length | shellLength (from VesselPhysical) | 0 | shell length |
| SI.Distance | shellThickness (from VesselPhysical) | 0 | shell wall thickness |
| SI.Density | shellRho (from VesselPhysical) | 8000 | typical for SS: 8000 kgr/m3, HDPE: 960 |
| SI.HeatCapacity | shellCp (from VesselPhysical) | 500 | typical for SS: 500 J/(kgr·K), HDPE: 2260 |
| SI.ThermalConductivity | shellK (from VesselPhysical) | 15 | shell wall thermal conductivity. typical value for SS=16.7, HDPE:0.33 |
| Bottom data |
| Types.HeadShape | vesselBottom (from VesselPhysical) | Types.HeadShape.flat | |
| Fraction | bFd (from VesselPhysical) | if vesselBottom == Types.HeadShape.Klopper then 1.0 elseif vesselBottom == Types.HeadShape.Korbbogen then 0.8 else 0 | ratio of bottom dish radius to tank diameter for torispheral head |
| Fraction | bFk (from VesselPhysical) | if vesselBottom == Types.HeadShape.Klopper then 0.1 elseif vesselBottom == Types.HeadShape.Korbbogen then 0.154 else 0 | ratio of bottom knuckle radius to tank diameter for torispheral head |
| SI.Distance | bottomHeight (from VesselPhysical) | 0 | bottom height if ellipsoidal/conical/piramid |
| SI.Distance | bottomThickness (from VesselPhysical) | shellThickness | bottom wall thickness |
| SI.Density | bottomRho (from VesselPhysical) | shellRho | typical for SS: 8000 kgr/m3, HDPE: 960 |
| SI.HeatCapacity | bottomCp (from VesselPhysical) | shellCp | typical for SS: 500 J/(kgr·K), HDPE: 2260 |
| SI.ThermalConductivity | bottompK (from VesselPhysical) | shellK | bottom wall thermal conductivity. typical value for SS=16.7, HDPE:0.33 |
| Top data |
| Types.HeadShape | vesselTop (from VesselPhysical) | Types.HeadShape.flat | |
| Fraction | tFd (from VesselPhysical) | if vesselTop == Types.HeadShape.Klopper then 1.0 elseif vesselTop == Types.HeadShape.Korbbogen then 0.8 else 0 | ratio of bottom dish radius to tank diameter for torispheral head |
| Fraction | tFk (from VesselPhysical) | if vesselTop == Types.HeadShape.Klopper then 0.1 elseif vesselTop == Types.HeadShape.Korbbogen then 0.154 else 0 | ratio of bottom knuckle radius to tank diameter for torispheral head |
| SI.Distance | topHeight (from VesselPhysical) | 0 | top height if ellipsoidal/conical/piramid. Measured inside |
| SI.Distance | topThickness (from VesselPhysical) | shellThickness | top wall thickness |
| SI.Density | topRho (from VesselPhysical) | shellRho | typical for SS: 8000 kgr/m3, HDPE: 960 |
| SI.HeatCapacity | topCp (from VesselPhysical) | shellCp | typical for SS: 500 J/(kgr·K), HDPE: 2260 |
| SI.ThermalConductivity | topK (from VesselPhysical) | shellK | top wall thermal conductivity. typical value for SS=16.7, HDPE:0.33 |
| Insulation |
| SI.Distance | insulationThickness (from VesselPhysical) | 0 | |
| SI.ThermalConductivity | insulationK (from VesselPhysical) | 0.04 | Insulation thermal conductivity. Typical value for glass fiber=0.04 W/(K·m) |
