CylindricalThickWall L4

Created Thursday 13 June 2013

Model energy storage and heat flow in radial direction through a cylindric wall


1. Purpose of Model

This model is appropriate if energy storage in a wall is of relevance and if the temperature gradients in radial direction are large compared to the gradients in longitudinal direction. Typical examples are unheated, thick-walled components like headers.


2. Level of Detail, Physical Effects Considered and Physical Insight


2.1 Level of Detail

Referring to Brunnemann et al. [1], this model refers to the level of detail L4 because the system is modelled with the use of balance equations, which are spatially discretised. The discretisation scheme can be defined by the user.

2.2 Physical Effects Considered

2.3 Level of Insight

No different levels of detail available.

3. Limits of Validity

In case of rapid temperature transients at the connectors, discretisation should be chosen sufficiently fine (=small thermal capacities), such that adjacent cells quickly reach thermal equilibrium.

4. Interfaces


4.1 Physical Connectors



5. Nomenclature


6. Governing Equations


By construction, the model agrees in the stationary case with the analytic solution for temperature distribution and heat flow.
This holds independently of the discretisation.

In the stationary case, at constant and temperature independent heat conductivity one obtains for one solid cylinder the temperature distribution:

and a constant radial heat flow:

Here we have introduced the effective heat conduction surface

If heat conductivity varies from shell to shell (e.g. due to temperature dependence) then

which is nothing but the heat flow through a series arrangement of heat resistors (one for each shell). Notice that here due to the finite volume approach the material properties are taken as spatially constant across each shell.


6.1 System Description and General model approach

The wall is decomposed into radial shells, numbered from the inner side to the outer side from .
Shell number has the thickness an cell borders and . Moreover it has a temperature state , which is located at radius , which is the center of the cell.


6.2 General Model Equations


Energy Conservation


Each shell has a dynamic energy balance

where the inner energy changes due to the heat flows across the shell borders and is given by

If the parameter then it is multiplied with the heat capacity and distributed evenly to the inner energy of each shell.
In the model it is assumed that the radial discretisation is sufficiently fine, such that the heat flow between two adjacent cells can be assumed as stationary.
However, since in principle the heat conductivity in each cell can vary with temperature, each heat flow across a shell border is modelled as a serial connection of two heat resistors (one for each half shell)
(i=2...n) :

where the first term on the right hand side accounts for the distance between cell center i-1 and cell border and the second terms accounts for the distance between the cell border and the cell center i.
For the heat flow at the inner side (i=1) and outer side (i=n+1) we take:

Accordingly the effective heat conduction surfaces are computed as (i=1..n)



7. Remarks for Usage

By construction, the model agrees in the stationary case with the analytic solution for temperature distribution and heat flow.
This holds independently of the discretisation.

8. Validation


9. References

[1] Johannes Brunnemann and Friedrich Gottelt, Kai Wellner, Ala Renz, André Thüring, Volker Röder, Christoph Hasenbein, Christian Schulze, Gerhard Schmitz, Jörg Eiden: "Status of ClaRaCCS: Modelling and Simulation of Coal-Fired Power Plants with CO2 capture", 9th Modelica Conference, Munich, Germany, 2012

10. Authorship and Copyright Statement for original (initial) Contribution

Author:
DYNCAP/DYNSTART development team, Copyright 2011 - 2022.
Remarks:
This component was developed during DYNCAP/DYNSTART projects.
Acknowledgements:
ClaRa originated from the collaborative research projects DYNCAP and DYNSTART. Both research projects were supported by the German Federal Ministry for Economic Affairs and Energy (FKZ 03ET2009 and FKZ 03ET7060).
CLA:
The author(s) have agreed to ClaRa CLA, version 1.0. See https://claralib.com/pdf/CLA.pdf
By agreeing to ClaRa CLA, version 1.0 the author has granted the ClaRa development team a permanent right to use and modify his initial contribution as well as to publish it or its modified versions under the 3-clause BSD License.

11. Version History

2013-06-28 - v 0.1 - Initial implementation - Johannes Brunnemann, XRG Símulation
24.04.2017 - v1.2.2 - parameter mass_struc added, the additional mass is evenly distributed to each shell - Timm Hoppe, XRG Simulation
04.02.2019 - v1.4.0 - renamed init option "no Init" to "fixed temperature" - Timm Hoppe, XRG Simulation


Backlinks: ClaRa:Basic Concepts of Modelling:Finite Volume Approach ClaRa:Components:HeatExchangers:HEXvle2gas L3 1ph BU simple ClaRa:Components:HeatExchangers:HEXvle2vle L3 1ph BU simple ClaRa:Components:HeatExchangers:HEXvle2vle L3 2ph BU simple ClaRa:Components:HeatExchangers:HEXvle2vle L3 2ph CH simple ClaRa:Components:HeatExchangers:HEXvle2vle L3 2ph CU simple ClaRa:Components:MechanicalSeparation:BalanceTank L3 ClaRa:Basics:ControlVolumes:SolidVolumes:ThinWall L4 ClaRa:Components:VolumesValvesFittings:Fittings:SprayInjectorVLE L3 ClaRa:Components:VolumesValvesFittings:Pipes:Header ClaRa:Components:VolumesValvesFittings:Pipes:PipeFlowGas L4 Advanced ClaRa:Components:VolumesValvesFittings:Pipes:PipeFlowGas L4 Simple ClaRa:Components:VolumesValvesFittings:Pipes:PipeFlow L4 Advanced ClaRa:Components:VolumesValvesFittings:Pipes:PipeFlow L4 Simple