modelHeatTransferInsideReactor_tubeBundle_array

Model calculating the heat transfered between fluid and heating system
Diagram of HeatTransferInsideReactor_tubeBundle_array

Information

1. Purpose of model

(Description)

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

(no equations)

7. Remarks for Usage

(none)

8. Validation

(no validation or testing necessary)

9. References

[1] Kim, Y., & Parker, W. (2008). A technical and economic evaluation of the pyrolysis of sewage sludge for the production of bio-oil. Bioresource technology, 99(5), 1409-1416.

[2] Vesilind, P. A., & Martel, C. J. (1989). Thermal conductivity of sludges. Water research, 23(2), 241-245.

10. Version History

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

Parameters

TypeNameDefaultDescription
Modelica.Units.SI.AreaAModelica.Constants.pi*d*lArea through which heat is transported by Convection
Modelica.Units.SI.DiameterD1inner Diameter of reactor
Modelica.Units.SI.Diameterd0.1tube diameter
Modelica.Units.SI.LengthlModelica.Constants.pi*(D - d)
Realn8number of turns of tube
IntegerN_cv8Number of control volumes

Connectors

TypeNameDefaultDescription
ClaRa.Basics.Interfaces.HeatPort_a[N_cv]heat_solid
ClaRa.Basics.Interfaces.HeatPort_bheat_fluid

Components

TypeNameDefaultDescription
TransiEnt.Producer.Gas.BiogasPlant.MaterialValues.SuspensionProperties_pTfluidProperties
TransiEnt.SimCentersimCenter
TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluid_pTvleFluidWall
Modelica.Units.SI.NusseltNumberNuTransiEnt.Producer.Gas.BiogasPlant.HeatTransfer.ForcedConvection.NusseltCSTR_Coil(Re = Re, Pr = fluidProperties.Pr, eta = fluidProperties.eta, eta_w = eta_w, C2 = C2, D = D, d = d)Nusselt Number
Modelica.Units.SI.ReynoldsNumberRe
RealC2
Modelica.Units.SI.HeatFlowRate[N_cv]Q_flowHeat flow rate from solid -> fluid
Modelica.Units.SI.TemperatureDifference[N_cv]dT= solid.T - fluid.T
Modelica.Units.SI.CoefficientOfHeatTransferalphaNu*fluidProperties.lambda/Dheat transfer coefficient of convection
Modelica.Units.SI.DynamicViscosityeta_wDynamic Viscosity of fluid at wall temperature