modelTubeStream

Extends from Interfaces.flowTwoPorts_pwh.

Parameters

TypeNameDefaultDescription
Booleanpbhi (from flowTwoPorts_pwh)falseif true dp is pb-pa,otherwise pa-pb
SI.LengthL10length
SI.LengthD0.05diameter
SI.Lengthdz0height of port b (out) over port a (in)
SI.MassFlowRatewnom0.5nominal flow rate
Realkdp0.1nominal dp [bar] per km at nominal flow
Integern5No. of lumps
SI.TemperatureTstart293.15initial T, all lumps
SI.CoefficientOfHeatTransfergamma02min gamma (still fluid)
BooleanfluidHeatstrueT if fluid heats the outside, F otherwise
BooleanhasInertiafalseaccount for fluid inertia

Connectors

TypeNameDefaultDescription
AES.ProcessComponents.Thermal.Interfaces.pwhPortpwh_a (from flowTwoPorts_pwh)
AES.ProcessComponents.Thermal.Interfaces.pwhPortpwh_b (from flowTwoPorts_pwh)
AES.ProcessComponents.Thermal.Interfaces.vectorHeatPortsurf

Components

TypeNameDefaultDescription
System_settings.System_liquidsystem (from flowTwoPorts_pwh)
SI.PressureDifferencedp (from flowTwoPorts_pwh)
SI.MassFlowRatew (from flowTwoPorts_pwh)
SI.SpecificEnthalpyhai (from flowTwoPorts_pwh)
SI.SpecificEnthalpyhbi (from flowTwoPorts_pwh)
SI.SpecificEnthalpyhao (from flowTwoPorts_pwh)
SI.SpecificEnthalpyhbo (from flowTwoPorts_pwh)
SI.Velocityufluid velocity
RealRe
RealNu
RealPr
SI.TemperatureTa
SI.TemperatureTb
SI.CoefficientOfHeatTransfergamma
SI.Temperature[n]Tfluid T, 1->n is a->b side
SI.PowerQ_surf_tot