modelCoilForcedConvection

Power exchanged between a flowing fluid and the internal wall. Needs an external heat flow model. It uses all the active coil surface

Extends from CoilPhysical (Gives pipes additional information regarding the coil shape), PipeForcedConvection (Model for pipes with thermal,single phase, flow).

Parameters

TypeNameDefaultDescription
Physical data
Modelica.Units.SI.DiametercoilDiam (from CoilPhysical)1.5Coil diameter
Realnum (from CoilPhysical)10total number of spires
Modelica.Units.SI.Distancepath (from CoilPhysical)0.15distance between centers of coil spires in meters(pitch)
Modelica.Units.SI.LengthheightInit (from CoilPhysical)0initial heigh of coil over reference (normally tangent) line
BooleanuseTubeLength (from PipePhysical)trueuse the supplied length
Modelica.Units.SI.DistancelTube (from PipePhysical)0supplied individual tube length
BooleanfixNumTubes (from PipePhysical)trueif true fixes the number of tubes to numTubes
IntegernumTubes (from PipePhysical)1number of parallel identical paths
BooleanisCircular (from PipePhysical)truethe pipe is circular in shape
BooleanuseDiameter (from PipePhysical)truethe supplied diameter will be used for calculation of section and perimeter
Modelica.Units.SI.Distancedi (from PipePhysical)0.0supplied internal diameter if path is circular
BooleanuseSectionAndPerimeter (from PipePhysical)falsethe supplied section and perimeter will be used
Modelica.Units.SI.Areasection (from PipePhysical)0supplied pipe section if not circular
Modelica.Units.SI.Distanceperimeter (from PipePhysical)0supplied perimeter if not circular
Modelica.Units.SI.Distancethickness (from PipePhysical)1e-3pipe thickness. Vessel wall thickness for halfcoils
Modelica.Units.SI.Distanceroughness (from PipePhysical)1.5e-005pipe roughness. SS:1.5e-5, Steel new:4.6e-5, Steel old:2.0e-4, Concrete:1.5e-3
Modelica.Units.SI.DistancethicknessInsul (from PipePhysical)0insulation thickness
Modelica.Units.SI.DensityrhoWall (from PipePhysical)8000
Ports links
BooleanuseElevDifference (from TwoFluidPorts)trueintroduces, or not, an equation for the ports elevation. Use only in one connector
FreeFluids.Types.ElevationOptionelevCalcMethod (from TwoFluidPorts)FreeFluids.Types.ElevationOption.differentialif useElevDifference==true, selects the equation to use: differential, or absolute for PortB
Modelica.Units.SI.LengthelevDifference (from TwoFluidPorts)0.0used only if previously selected. Positive if PortB higher than PortA
Modelica.Units.SI.LengthportBelevation (from TwoFluidPorts)0.0used only if previously selected.
BooleancalcEnthalpyDifference (from TwoFluidPorts)trueif true, will calculate the enthalpy difference between ports. Use only in one connector
BooleanpassComposition (from TwoFluidPorts)trueif true, the equation PortA.X=PortB.X will be activated
Flow
IntegernumActiveTubes (from Pipe)numTubesnumber of parallel identical paths used with flow. Default=numTubes
RealpipeComplexity (from Pipe)0Approx. estimation of equivalent length,0=not used,0.25=supply lines,0.5=long runs, 1=normal,2=valves,4=complex valves
RealequivL_Di (from Pipe)0Equivalent length of accesories as multiples of Di
RealnumVelocityHeads (from Pipe)0number of velocity heads for pressure loss
Modelica.Units.SI.Areakv (from Pipe)0This allows for special head loses to be incorporated inside the pipe calculation via Kv
Fractionaperture (from Pipe)1Fraction of Kv used
BooleanfullBore (from Pipe)truetrue if the full pipe section is used for flow
BooleanisCompressibleFlow (from Pipe)falseindicates if kinetic energy and momentum are taken into account or not
BooleantwoPhaseFlow (from PipeFlowBase)falseindicates if there is a two phase flow
BooleanusePLossWallCorr (from PipeForcedConvection)true
Heat transfer
FreeFluids.Types.ThermalTypethermalType (from PipeFlowBase)FreeFluids.Types.ThermalType.detailedAlternatives: detailed, isenthalpic, adiabatic, isothermal, fixed W, fixed deltaT. If detailed, W calculation must be supplied
Modelica.Units.SI.HeatFlowRatefixedW (from PipeFlowBase)0Heat exchange if thermaltype = fixedPower. Positive if heat enters the tube
Modelica.Units.SI.TemperatureDifferencefixedDeltaT (from PipeFlowBase)0fixed T diff. between ports if thermalType = fixedDeltaT. Positive if Tb > Ta
Modelica.Units.SI.ThermalConductivitykWall (from PipeThermalBase)16Wall thermal conductivity. typical value for SS=16.7
Modelica.Units.SI.ThermalConductivitykInsul (from PipeThermalBase)0.04Insulation thermal conductivity. Typical value for glass fiber=0.04 W/(K·m)
Modelica.Units.SI.ThermalInsulancefoulingF (from PipeThermalBase)0.0002Tube side fouling factor.Typical: 0.00018 for thermal oil, or treated cooling water
BooleanuseWallsResistance (from PipeThermalBase)falseif true, will calculate Twall-Tsurf according to wall conduction, otherwise Twall=Tsurf
RealemissionCoef (from PipeThermalBase)0.26emission coefficient of surface typical values: Aluminium:0.1, SS:0.15, dirty metal: 0.45, non-metallic:0.94
BooleanfullHTperimeter (from PipeThermalBase)trueindicates if all active perimeter is used in heat transfer. It is false for halfpipes
BooleanfullHTlength (from PipeThermalBase)trueindicates if all tube length is used in heat transfer. For partial immersion or condensation
BooleanuseThermalConnector (from PipeThermalBase)trueif true, the thermal connector will be used for heat transfer. Otherwise a specific calculation must be coded
BooleanuseHTWallCorrFactor (from PipeForcedConvection)true
BooleanuseTwistedTapeInserts (from PipeForcedConvection)false
Modelica.Units.SI.LengthtapeWidth (from PipeForcedConvection)dionly if twisted tape inserts are used
Modelica.Units.SI.LengthtapeThickness (from PipeForcedConvection)thicknessonly if twisted tape inserts are used
RealtwistRatio (from PipeForcedConvection)6Length of a 180 degrees twist divided by Di, if twisted tape inserts are used

Connectors

TypeNameDefaultDescription
FreeFluids.Interfaces.FluidPortAPortA (from TwoFluidPorts)
FreeFluids.Interfaces.FluidPortBPortB (from TwoFluidPorts)
FreeFluids.Interfaces.HeatPortBPortH (from PipeThermalBase)

Components

TypeNameDefaultDescription
Modelica.Units.SI.DistanceCoilHeigth (from CoilPhysical)
Modelica.Units.SI.DistanceCoilFinalHeight (from CoilPhysical)
Modelica.Units.SI.DistanceLtotal (from CoilPhysical)total pipe length, as necessary for obtainning its total weight
Modelica.Units.SI.DiameterDi (from PipePhysical)pipe internal diameter only if circular, otherwise four times Section/Perimeter
Modelica.Units.SI.AreaPathSection (from PipePhysical)Internal section of the tube. But not the flow section if double pipe
Modelica.Units.SI.DistancePathPerimeter (from PipePhysical)Internal perimeter of the tube. But not the flow perimeter if double pipe
Modelica.Units.SI.DistanceLtube (from PipePhysical)pipe path length, as necessary for obtainning friction loss
IntegerNumTubes (from PipePhysical)number of parallel identical paths
Modelica.Units.SI.AreaSiTube (from PipePhysical)each tube internal surface
Modelica.Units.SI.AreaSiTotal (from PipePhysical)total pipe internal surface
Modelica.Units.SI.VolumeViTube (from PipePhysical)each tube internal volume
Modelica.Units.SI.VolumeViTotal (from PipePhysical)total pipe internal volume
Modelica.Units.SI.DiameterDo (from PipePhysical)pipe external diameter
Modelica.Units.SI.DiameterDinsul (from PipePhysical)pipe diameter with insulation
Modelica.Units.SI.AreaSoTube (from PipePhysical)each tube external surface
Modelica.Units.SI.AreaSoTotal (from PipePhysical)total pipe external surface
Modelica.Units.SI.VolumeVoTube (from PipePhysical)each tube external volume
Modelica.Units.SI.VolumeVoTotal (from PipePhysical)total pipe external volume
Modelica.Units.SI.AreaSinsulTube (from PipePhysical)each tube insulation surface
Modelica.Units.SI.AreaSinsulTotal (from PipePhysical)total pipe insulation surface
Modelica.Units.SI.MassMassPipeTotal (from PipePhysical)total mass of the pipe
Modelica.Units.SI.SpecificEnthalpyHdiff (from TwoFluidPorts)specific enthalpy difference: Port B - Port A
Modelica.Units.SI.PressureDifferencePdiff (from TwoFluidPorts)pressure difference: Port B - Port A
IntegerNumActiveTubes (from Pipe)number of parallel identical paths used with flow.
RealSlope (from Pipe)pipe slope as (PortB.Elevation-PortA.Elevation)/Ltube
Modelica.Units.SI.AreaSiActive (from Pipe)active pipe internal surface
Modelica.Units.SI.VolumeViActive (from Pipe)active pipe internal volume
Modelica.Units.SI.AreaSoActive (from Pipe)active pipe external surface
Modelica.Units.SI.VolumeVoActive (from Pipe)active pipe external volume
Modelica.Units.SI.AreaSinsulActive (from Pipe)active pipe external surface
Modelica.Units.SI.DistanceLeTube (from Pipe)equivalent length of the pipe for pressure loss
Modelica.Units.SI.AreaPathSectionActive (from Pipe)section of each tube used for flow calculation
Modelica.Units.SI.DistancePathPerimeterActive (from Pipe)perimeter of each tube used for flow calculation
Modelica.Units.SI.DiameterDh (from Pipe)four time the hydraulic radius
Modelica.Units.SI.MassMassProductTotal (from Pipe)Mass of product inside all the tubes
Modelica.Units.SI.PressurePLossFriction (from Pipe)friction head loss
Modelica.Units.SI.VelocityVa (from PipeFlowBase)
Modelica.Units.SI.VelocityVb (from PipeFlowBase)
Medium.DensityRhoA (from PipeFlowBase)density at Port A
Medium.DensityRhoB (from PipeFlowBase)density at PortB
Medium.ThermodynamicStateStateA (from PipeFlowBase)state at PortA
Medium.ThermodynamicStateStateB (from PipeFlowBase)state at PortB
Modelica.Units.SI.VolumeFlowRateQa (from PipeFlowBase)volume flow rate at PortA
Modelica.Units.SI.VolumeFlowRateQb (from PipeFlowBase)volume flow rate at PortB
Medium.TemperatureTa (from PipeFlowBase)
Medium.TemperatureTb (from PipeFlowBase)
Modelica.Units.SI.PowerW (from PipeFlowBase)heat transfer between fluid and wall. Positive if fluid inputs heat
Medium.TemperatureTwall (from PipeThermalBase)average wall temperature (tube inside)
Medium.TemperatureTsurf (from PipeThermalBase)average superficial temperature (tube outside)
Modelica.Units.SI.TemperatureDifferenceLMTD (from PipeThermalBase)Logarithmic mean temperature difference, referenced to Tsurf
Modelica.Units.SI.AreaSactiveHT (from PipeThermalBase)internal surface potentially active for heat transfer, due to partial perimeter usage
Modelica.Units.SI.AreaSusedHT (from PipeThermalBase)internal surface used for heat transfer, due to partial perimeter or partial length usage. Probably to be deprecated
Modelica.Units.SI.CoefficientOfHeatTransferH (from PipeThermalBase)average heat transfer coefficient of unique or main mechanism
Medium.ThermodynamicStateStateAvg (from PipeForcedConvection)average state for physical properties calculation
Modelica.Units.SI.DensityRho (from PipeForcedConvection)average density used in calculations
Medium.DynamicViscosityMu (from PipeForcedConvection)average dynamic viscosity used in calculations
Modelica.Units.SI.ReynoldsNumberRe (from PipeForcedConvection)Reynolds number at average conditions
RealFl (from PipeForcedConvection)laminar Darcy's friction factor at average conditions
RealFt (from PipeForcedConvection)turbulent Darcy's friction factor at average conditions
RealF (from PipeForcedConvection)Darcy's friction factor at average conditions
Modelica.Units.SI.VolumeFlowRateQ (from PipeForcedConvection)volume flow rate in each active tube at average conditions
Modelica.Units.SI.VelocityV (from PipeForcedConvection)velocity at average conditions. Normally between 0.9 and 3.0 m/s for liquids
Modelica.Units.SI.HeatCapacityCp (from PipeForcedConvection)
Modelica.Units.SI.ThermalConductivityK (from PipeForcedConvection)
Modelica.Units.SI.PrandtlNumberPr (from PipeForcedConvection)
RealPLossWallCorr (from PipeForcedConvection)
Medium.ThermodynamicStateStateW (from PipeForcedConvection)Thermodynamic state at wall
Medium.TemperatureT (from PipeForcedConvection)absolute temperature used for physical properties calc.
Medium.DynamicViscosityMuWall (from PipeForcedConvection)average wall viscosity
RealFsmooth (from PipeForcedConvection)smooth pipe friction factor
RealHTWallCorrFactor (from PipeForcedConvection)
Modelica.Units.SI.RayleighNumberRa (from PipeForcedConvection)Rayleigh number
RealSw (from PipeForcedConvection)Swirl number
Modelica.Units.SI.NusseltNumberNu (from PipeForcedConvection)