modelHEXgeneric2Ph
Exchanger model without heat transfer coefficient calculation, for two phases flow in tubes
Extends from FreeFluids.Pipes.PipeFlow2Ph (Single pipe(not double) for two phases flow. With no detailed heat transfer model. Muller-Steinhagen and Heck method).
Information
The model is for a tube heat exchanger, that can have several passes and extended surface, in an undefined external flowing media. We need to specify the global U, as it is impossible its calculation. We define also the inner media, and the external media Cp, inlet temperature, and outlet temperature or mass flow rate.As an alternative it is also possible to use a fixed exchanged power, or a fixed temperature for the tubes external surface.
As two phases are coexisting along the exchanger a straight LMTD method is used.
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| Physical data | |||
| Boolean | useTubeLength (from PipePhysical) | true | use the supplied length |
| Modelica.Units.SI.Distance | lTube (from PipePhysical) | 0 | supplied individual tube length |
| Boolean | fixNumTubes (from PipePhysical) | true | if true fixes the number of tubes to numTubes |
| Integer | numTubes (from PipePhysical) | 1 | number of parallel identical paths |
| Boolean | isCircular (from PipePhysical) | true | the pipe is circular in shape |
| Boolean | useDiameter (from PipePhysical) | true | the supplied diameter will be used for calculation of section and perimeter |
| Modelica.Units.SI.Distance | di (from PipePhysical) | 0.0 | supplied internal diameter if path is circular |
| Boolean | useSectionAndPerimeter (from PipePhysical) | false | the supplied section and perimeter will be used |
| Modelica.Units.SI.Area | section (from PipePhysical) | 0 | supplied pipe section if not circular |
| Modelica.Units.SI.Distance | perimeter (from PipePhysical) | 0 | supplied perimeter if not circular |
| Modelica.Units.SI.Distance | thickness (from PipePhysical) | 1e-3 | pipe thickness. Vessel wall thickness for halfcoils |
| Modelica.Units.SI.Distance | roughness (from PipePhysical) | 1.5e-005 | pipe roughness. SS:1.5e-5, Steel new:4.6e-5, Steel old:2.0e-4, Concrete:1.5e-3 |
| Modelica.Units.SI.Distance | thicknessInsul (from PipePhysical) | 0 | insulation thickness |
| Modelica.Units.SI.Density | rhoWall (from PipePhysical) | 8000 | |
| Modelica.Units.SI.Length | tubeLength | ||
| Integer | numTubesTotal | ||
| Integer | numPasses | 1 | |
| Ports links | |||
| Boolean | useElevDifference (from TwoFluidPorts) | true | introduces, or not, an equation for the ports elevation. Use only in one connector |
| FreeFluids.Types.ElevationOption | elevCalcMethod (from TwoFluidPorts) | FreeFluids.Types.ElevationOption.differential | if useElevDifference==true, selects the equation to use: differential, or absolute for PortB |
| Modelica.Units.SI.Length | elevDifference (from TwoFluidPorts) | 0.0 | used only if previously selected. Positive if PortB higher than PortA |
| Modelica.Units.SI.Length | portBelevation (from TwoFluidPorts) | 0.0 | used only if previously selected. |
| Boolean | calcEnthalpyDifference (from TwoFluidPorts) | true | if true, will calculate the enthalpy difference between ports. Use only in one connector |
| Boolean | passComposition (from TwoFluidPorts) | true | if true, the equation PortA.X=PortB.X will be activated |
| Flow | |||
| Integer | numActiveTubes (from Pipe) | numTubes | number of parallel identical paths used with flow. Default=numTubes |
| Real | pipeComplexity (from Pipe) | 0 | Approx. estimation of equivalent length,0=not used,0.25=supply lines,0.5=long runs, 1=normal,2=valves,4=complex valves |
| Real | equivL_Di (from Pipe) | 0 | Equivalent length of accesories as multiples of Di |
| Real | numVelocityHeads (from Pipe) | 0 | number of velocity heads for pressure loss |
| Modelica.Units.SI.Area | kv (from Pipe) | 0 | This allows for special head loses to be incorporated inside the pipe calculation via Kv |
| Fraction | aperture (from Pipe) | 1 | Fraction of Kv used |
| Boolean | fullBore (from Pipe) | true | true if the full pipe section is used for flow |
| Boolean | isCompressibleFlow (from Pipe) | false | indicates if kinetic energy and momentum are taken into account or not |
| Boolean | twoPhaseFlow (from PipeFlowBase) | false | indicates if there is a two phase flow |
| Heat transfer | |||
| FreeFluids.Types.ThermalType | thermalType (from PipeFlowBase) | FreeFluids.Types.ThermalType.detailed | Alternatives: detailed, isenthalpic, adiabatic, isothermal, fixed W, fixed deltaT. If detailed, W calculation must be supplied |
| Modelica.Units.SI.HeatFlowRate | fixedW (from PipeFlowBase) | 0 | Heat exchange if thermaltype = fixedPower. Positive if heat enters the tube |
| Modelica.Units.SI.TemperatureDifference | fixedDeltaT (from PipeFlowBase) | 0 | fixed T diff. between ports if thermalType = fixedDeltaT. Positive if Tb > Ta |
| Integer | numRows | 1 | necessary only for crossflow |
| Modelica.Units.SI.SpecificHeatCapacity | extCp | 1003 | fixed specific heat capacity of external media. Air=1003. Water=4194 |
| Modelica.Units.SI.Temperature | extTin | 298.15 | fixed external media inlet temperature |
| Boolean | fixExternalFlow | true | if false the external media outlet temp. will be fixed |
| Modelica.Units.SI.MassFlowRate | extG | fixed external media massic flow | |
| Modelica.Units.SI.Temperature | extTout | 318.15 | fixed external media outlet temperature |
| Modelica.Units.SI.CoefficientOfHeatTransfer | u | fixed overall heat transfer coefficient referenced to external surface | |
| Real | extSratio | (di + 2*thickness)/di | ratio of external surface to internal bare tube surface |
| Optional user phys. prop. | |||
| Modelica.Units.SI.Density | rhoL (from PipeFlow2Ph) | 0 | fixed liquid density to use in calculations. If 0, will be calculated from the medium |
| Modelica.Units.SI.DynamicViscosity | muL (from PipeFlow2Ph) | 0 | fixed liquid dynamic viscosity to use in calculations |
| Modelica.Units.SI.Density | rhoG (from PipeFlow2Ph) | 0 | fixed gas density to use in calculations |
| Modelica.Units.SI.DynamicViscosity | muG (from PipeFlow2Ph) | 0 | fixed gas dynamic viscosity to use in calculations |
| Real | x (from PipeFlow2Ph) | 0 | fixed mass gas fraction at average conditions |
Connectors
| Type | Name | Default | Description |
|---|---|---|---|
| FreeFluids.Interfaces.FluidPortA | PortA (from TwoFluidPorts) | ||
| FreeFluids.Interfaces.FluidPortB | PortB (from TwoFluidPorts) |
Components
| Type | Name | Default | Description |
|---|---|---|---|
| Modelica.Units.SI.Diameter | Di (from PipePhysical) | pipe internal diameter only if circular, otherwise four times Section/Perimeter | |
| Modelica.Units.SI.Area | PathSection (from PipePhysical) | Internal section of the tube. But not the flow section if double pipe | |
| Modelica.Units.SI.Distance | PathPerimeter (from PipePhysical) | Internal perimeter of the tube. But not the flow perimeter if double pipe | |
| Modelica.Units.SI.Distance | Ltotal (from PipePhysical) | total pipe length, as necessary for obtainning its total weight | |
| Modelica.Units.SI.Distance | Ltube (from PipePhysical) | pipe path length, as necessary for obtainning friction loss | |
| Integer | NumTubes (from PipePhysical) | number of parallel identical paths | |
| Modelica.Units.SI.Area | SiTube (from PipePhysical) | each tube internal surface | |
| Modelica.Units.SI.Area | SiTotal (from PipePhysical) | total pipe internal surface | |
| Modelica.Units.SI.Volume | ViTube (from PipePhysical) | each tube internal volume | |
| Modelica.Units.SI.Volume | ViTotal (from PipePhysical) | total pipe internal volume | |
| Modelica.Units.SI.Diameter | Do (from PipePhysical) | pipe external diameter | |
| Modelica.Units.SI.Diameter | Dinsul (from PipePhysical) | pipe diameter with insulation | |
| Modelica.Units.SI.Area | SoTube (from PipePhysical) | each tube external surface | |
| Modelica.Units.SI.Area | SoTotal (from PipePhysical) | total pipe external surface | |
| Modelica.Units.SI.Volume | VoTube (from PipePhysical) | each tube external volume | |
| Modelica.Units.SI.Volume | VoTotal (from PipePhysical) | total pipe external volume | |
| Modelica.Units.SI.Area | SinsulTube (from PipePhysical) | each tube insulation surface | |
| Modelica.Units.SI.Area | SinsulTotal (from PipePhysical) | total pipe insulation surface | |
| Modelica.Units.SI.Mass | MassPipeTotal (from PipePhysical) | total mass of the pipe | |
| Modelica.Units.SI.SpecificEnthalpy | Hdiff (from TwoFluidPorts) | specific enthalpy difference: Port B - Port A | |
| Modelica.Units.SI.PressureDifference | Pdiff (from TwoFluidPorts) | pressure difference: Port B - Port A | |
| Integer | NumActiveTubes (from Pipe) | number of parallel identical paths used with flow. | |
| Real | Slope (from Pipe) | pipe slope as (PortB.Elevation-PortA.Elevation)/Ltube | |
| Modelica.Units.SI.Area | SiActive (from Pipe) | active pipe internal surface | |
| Modelica.Units.SI.Volume | ViActive (from Pipe) | active pipe internal volume | |
| Modelica.Units.SI.Area | SoActive (from Pipe) | active pipe external surface | |
| Modelica.Units.SI.Volume | VoActive (from Pipe) | active pipe external volume | |
| Modelica.Units.SI.Area | SinsulActive (from Pipe) | active pipe external surface | |
| Modelica.Units.SI.Distance | LeTube (from Pipe) | equivalent length of the pipe for pressure loss | |
| Modelica.Units.SI.Area | PathSectionActive (from Pipe) | section of each tube used for flow calculation | |
| Modelica.Units.SI.Distance | PathPerimeterActive (from Pipe) | perimeter of each tube used for flow calculation | |
| Modelica.Units.SI.Diameter | Dh (from Pipe) | four time the hydraulic radius | |
| Modelica.Units.SI.Mass | MassProductTotal (from Pipe) | Mass of product inside all the tubes | |
| Modelica.Units.SI.Pressure | PLossFriction (from Pipe) | friction head loss | |
| Modelica.Units.SI.Velocity | Va (from PipeFlowBase) | ||
| Modelica.Units.SI.Velocity | Vb (from PipeFlowBase) | ||
| Medium.Density | RhoA (from PipeFlowBase) | density at Port A | |
| Medium.Density | RhoB (from PipeFlowBase) | density at PortB | |
| Medium.ThermodynamicState | StateA (from PipeFlowBase) | state at PortA | |
| Medium.ThermodynamicState | StateB (from PipeFlowBase) | state at PortB | |
| Modelica.Units.SI.VolumeFlowRate | Qa (from PipeFlowBase) | volume flow rate at PortA | |
| Modelica.Units.SI.VolumeFlowRate | Qb (from PipeFlowBase) | volume flow rate at PortB | |
| Medium.Temperature | Ta (from PipeFlowBase) | ||
| Medium.Temperature | Tb (from PipeFlowBase) | ||
| Modelica.Units.SI.Power | W (from PipeFlowBase) | heat transfer between fluid and wall. Positive if fluid inputs heat | |
| Medium.Density | RhoL (from PipeFlow2Ph) | density of liquid phase | |
| Medium.DynamicViscosity | MuL (from PipeFlow2Ph) | dynamic viscosity of liquid phase | |
| Modelica.Units.SI.Velocity | Vl (from PipeFlow2Ph) | velocity in each active tube if all was liquid | |
| Modelica.Units.SI.ReynoldsNumber | ReL (from PipeFlow2Ph) | Reynolds number if all was liquid | |
| Real | Fl (from PipeFlow2Ph) | Darcy's friction factor if all liquid | |
| Medium.AbsolutePressure | PLossFrictionL (from PipeFlow2Ph) | friction head loss if all was liquid | |
| Medium.Density | RhoG (from PipeFlow2Ph) | density of gas phase | |
| Medium.DynamicViscosity | MuG (from PipeFlow2Ph) | dynamic viscosity of gas phase | |
| Modelica.Units.SI.Velocity | Vg (from PipeFlow2Ph) | velocity in each active tube if all was gas | |
| Modelica.Units.SI.ReynoldsNumber | ReG (from PipeFlow2Ph) | Reynolds number if all was gas | |
| Real | Fg (from PipeFlow2Ph) | Darcy's friction factor if all gas | |
| Medium.AbsolutePressure | PLossFrictionG (from PipeFlow2Ph) | friction head loss if all was gas | |
| Fraction | X (from PipeFlow2Ph) | average gas fraction | |
| Medium.ThermodynamicState | StateL (from PipeFlow2Ph) | ||
| Medium.ThermodynamicState | StateG (from PipeFlow2Ph) | ||
| Modelica.Units.SI.Area | Sext | ||
| Modelica.Units.SI.MassFlowRate | Gext | external media mass flow rate | |
| Modelica.Units.SI.Temperature | TextOut | ||
| Modelica.Units.SI.ThermalConductance | ThConductance | ||
| Modelica.Units.SI.TemperatureDifference | LMTD |