modelFreeConvectionHeatTransfer_Gas

Heat Transfer due to natural Convection
Diagram of FreeConvectionHeatTransfer_Gas

Information

1. Purpose of model

This is a model of linear heat convection, e.g., the heat transfer between a plate and the surrounding air; see also: ConvectiveResistor. It may be used for complicated solid geometries and fluid flow over the solid by determining the convective thermal conductance Gc by measurements.

2. Level of detail, physical effects considered, and physical insight

(Description)

3. Limits of validity

(Description)

4. Interfaces

HeatPort_a: heat_solid

HeatPort_b: heat_fluid

5. Nomenclature

(no elements)

6. Governing Equations

The basic constitutive equation for convection is

Q_flow = A * alpha *(solid.T - fluid.T);

Q_flow: Heat flow rate from connector 'solid' (e.g., a plate)

to connector 'fluid' (e.g., the surrounding air)


A: Convection area (e.g., perimeter*length of a box)

alpha: Heat transfer coefficient

where the heat transfer coefficient alpha is calculated from properties of the fluid flowing over the solid. Examples:

Heat transfer by Free convection: External Flows (acording to W.Kast, et al.: VDI Heat Atlas, 2nd english edition, Springerl, 2010, p.667):

alpha = Nu*lamda/l;

Nu = f(Ra, Pr, Geometry)

where

alpha : Heat transfer coefficient

Nu : = alpha*l/lambda (Nusselt number)

Ra : = g*l^3*beta*dT (Rayleigh number)

Pr : = cp*eta/lambda (Prandtl number)

g : = Accelaration of gravity

l : characteristic length

height: height (characteristic lenght of vertical cylinder)

D : diameter of cylinder

rho : density of fluid (material constant)

eta : dynamic viscosity of fluid (material constant)

cp : specific heat capacity of fluid (material constant)

lambda : thermal conductivity of fluid (material constant)

7. Remarks for Usage

(none)

8. Validation

(no validation or testing necessary)

9. References

[1] W.Kast, et al.: VDI Heat Atlas, 2nd english edition, Springerl, 2010, p.667

10. Version History

Model created by Philipp Jahneke (philipp.koziol@tuhh.de), August 2018

Parameters

TypeNameDefaultDescription
TILMedia.GasTypes.BaseGasmedium
BooleanuseMassFractionDefaultfalse
Modelica.Units.SI.Pressurep101300pressure of fluid
Modelica.Units.SI.AreaAArea through which heat is transported by Convection
Modelica.Units.SI.LengthLspecific lenght of geometry

Connectors

TypeNameDefaultDescription
ClaRa.Basics.Interfaces.HeatPort_aheat_solid
ClaRa.Basics.Interfaces.HeatPort_bheat_fluid

Components

TypeNameDefaultDescription
Modelica.Units.SI.ThermalConductivitylamdagas.transp.lambdaThermal conductivity of fluid at T_m
Modelica.Units.SI.Densityrhogas.dDensity of fluid at T_m
Modelica.Units.SI.PrandtlNumberPrgas.transp.PrPrandtl number of the fluid
Modelica.Units.SI.KinematicViscositynuegas.transp.eta/gas.d
Modelica.Units.SI.DynamicViscosityetagas.transp.eta
Modelica.Units.SI.LinearExpansionCoefficientbetagas.betaIsobaric thermal expansion coefficient at given conditions
Modelica.Units.SI.CoefficientOfHeatTransferalphaNu*gas.transp.lambda/Lheat transfer coefficient of convection
Modelica.Units.SI.SpecificHeatCapacityAtConstantPressurecpgas.cpspecific heat capacity of fluid at given conditions
Modelica.Units.SI.RayleighNumberRaRayleighNumber(l = L, beta = beta, dT = dT, Pr = gas.transp.Pr, nue = gas.transp.eta/gas.d)
Modelica.Units.SI.NusseltNumberNuNusselt Number
Modelica.Units.SI.MassFraction[medium.nc - 1]xigas.gasType.xi_defaultMass Fraction
Modelica.Units.SI.HeatFlowRateQ_flowHeat flow rate from solid -> fluid
Modelica.Units.SI.TemperatureDifferencedT= solid.T - fluid.T
Modelica.Units.SI.TemperatureT_m(heat_solid.T + heat_fluid.T)/2
TILMedia.Gas_pTgas