modelHeatTransferInsideReactor

Model calculating the heat transfered between fluid and vessel walls
Diagram of HeatTransferInsideReactor

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^2/4 + D*height)Area through which heat is transported by Convection
Modelica.Units.SI.DiameterD1inner Diameter of reactor
Modelica.Units.SI.Heightheight1Height of fluid inside reactor

Connectors

TypeNameDefaultDescription
ClaRa.Basics.Interfaces.HeatPort_aheat_solidheat port for heat transfer between fluid and vessel walls
ClaRa.Basics.Interfaces.HeatPort_bheat_fluidheat port for heat transfer between fluid and vessel walls

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.NusseltInsideCSTR(Re = Re, Pr = fluidProperties.Pr, eta = fluidProperties.eta, eta_w = eta_w, C1 = C1)Nusselt Number
Modelica.Units.SI.ReynoldsNumberReReynolds number
RealC1geometrical Coefficient in Nusselt-Equation
Modelica.Units.SI.HeatFlowRateQ_flowHeat flow rate from solid -> fluid
Modelica.Units.SI.TemperatureDifferencedT= 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