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Material Property

Material properties are volume conditions in the Heat module pertaining to selected Volumes.

Specify the material properties (Conductivity or Enthalpy Model), as follows:

  • Geometric Entities Panel > Volumes > [Desired Volume]
  • Properties Panel > Model Tab > Heat > (Conductivity or Enthalpy Model)
 

Figure 5.121 - Material properties

Conductivity

The thermal conductivity model must be defined, when Heat Module is active.

The models in the Conductivity drop down list are:

Constant Prandtl Number

The Prandtl number is a dimensionless number defined as the ratio of momentum diffusivity to thermal diffusivity. The thermal conductivity () for a selected volume can be specified with constant Prandtl Number () given under Prandtl Number as shown in Figure 5.122.

Here, and is the dynamic viscosity and specific heat capacity of the fluid flow, respectively.

 

Figure 5.122 - Constant Prandtl number

Constant Conductivity

The Constant Conductivity () is specified for a selected volume under Conductivity.

Polynomial Function of T

Conductivity is modelled as a function of temperature by selecting Polynomial Function of T model for a selected volume.

In Simerics-MP, conductivity is specified as a function of temperature with polynomial functions using three coefficients.

 

Figure 5.123 - Polynomial Function of T model

Polynomial equation for heat capacity as a function of temperature is expressed as:

5.392

 

= Temperature ()

= Reference Temperature ()

= Conductivity at Reference T ()

= Linear Temperature Coefficient ()

= Quadratic Temperature Coefficient ()

= Cubic Temperature Coefficient ()

 

User needs to provide following parameters in the Polynomial function of T model:

Cartesian Conductivity (X, Y, Z)

The Cartesian Conductivity option in Simerics-MP solves the conduction equation in solids with the anisotropic thermal conductivity specified in cartesian coordinate.

Different components of thermal conductivity are entered for a selected volume under K(X, Y, Z) as shown in Figure 5.124.

 

Figure 5.124 - Cartesian Conductivity (X, Y, Z)

Orthotropic Conductivity

In Simerics-MP, an orthotropic thermal conductivity in solids is defined under Orthotropic Conductivity for selected volume. When the orthotropic thermal conductivity is used, the thermal conductivities (,,) in the principal directions (,,) are specified. The conductivity matrix is then computed as,

5.393

 

Figure 5.125 - Orthotropic Conductivity

Since the directions (,,) are mutually orthogonal, only the first two need to be specified for three-dimensional problem. The constant thermal conductivities need to be specified for all three directions.

Cylindrical Conductivity

The thermal conductivity of solids can be specified in cylindrical coordinates. To define the thermal conductivity in cylindrical coordinates, select Cylindrical Conductivity in the drop-down list for Conductivity in Heat module.

As shown in Figure 5.126, the center and the direction of the cylindrical coordinate system must be specified along with the radial, tangential, and axial direction conductivities.

 

Figure 5.126 - Cylindrical Conductivity

K Matrix

For anisotropic diffusion, the thermal conductivity matrix can be directly specified. Matrix components of the thermal conductivity as shown in Figure 5.127 can be specified in Simerics-MP.

 

Figure 5.127 - K Matrix

 

  Note: For information on how to perform tensor transformations of the thermal conductivity, refer 2022 ASME conference proceedings .

 

Enthalpy Model

This specifies a model for computing the relationship between temperature and enthalpy.

The models in the Enthalpy Model drop down list are:

 

Constant Capacity

The Constant Capacity (specific heat at constant pressure ) is specified for a selected volume under Capacity.

Polynomial Function of T

Enthalpy is modelled as a function of temperature by selecting Polynomial Function of T model for a selected volume.

In Simerics-MP, enthalpy is calculated based on heat capacity of the material, which is specified as a function of temperature with polynomial functions using three coefficients.

 

Figure 5.128 - Polynomial Function of T model

Polynomial equation for heat capacity as a function of temperature is expressed as:

5.394

Polynomial equation for enthalpy as a function of temperature is expressed as:

5.395

where,

= Temperature ()

= Constant Pressure Heat Capacity ()

= Linear Temperature Coefficient ()

= Cubic Temperature Coefficient ()

= Specific Enthalpy ()

= Reference Temperature ()

= Capacity at Reference T ()

= Quadratic Temperature Coefficient ()

= Reference Enthalpy ()

 

User needs to provide following parameters in the Polynomial function of T model:

JANAF Table

The Enthalpy Model for a selected Volume can be specified directly using the JANAF Table. The coefficients for a polynomial function of temperature are entered corresponding to values from JANAF data.

This JANAF model handles a larger temperature range up to 30000 K. The temperature dependent values of specific heat (), Enthalpy () and Entropy () are calculated with three polynomials using 9 coefficients.

 

Figure 5.129 - JANAF Table

 

5.396

 

5.397

 

5.398

 

Phase Change

In Simerics-MP, phase change of the material is modelled using Phase Change model for selected volume. The enthalpy is calculated based on the specific heat (function of temperature) and phase of the material. The specific heat variation with temperature is provided for both phases.

  • State Change: Allows three options Melt/Evaporation, Solid/Condensation and Both.
  • Melt/Evaporation: Considers the change of phase from solid to liquid or liquid to gas.
  • Phase Change temperature: This is the temperature at which phase change occurs.
  • Latent Heat: This is the heat release or absorbed during the phase change.
  • T Range (DT) of phase Transition: This is the transition region at which phase change occurs.
  • Reference Enthalpy: It is the enthalpy at reference temperature.
  • Reference Temperature: The is the reference temperature for calculating specific heat.
  • Capacity (Low T Phase): It is the capacity at the reference temperature for lower phase. For example, lower phase corresponds to solid state during melting process and liquid state during evaporation process. It is the constant value in the polynomial function of specific heat for the lower phase.
  • Linear T Coefficient (Low T Phase): This is the coefficient of linear term in the polynomial function of specific heat for the lower phase.
  • Quadratic T Coefficient (Low T Phase): This is the coefficient of quadratic term in the polynomial function of specific heat for the lower phase.
  • Capacity (High T Phase): It is the capacity at the reference temperature for higher phase. For example, higher phase corresponds to liquid state during melting process and gaseous state during evaporation process. It is the constant value in the polynomial function of specific heat for the higher phase.
  • Linear T Coefficient (High T Phase): This is the coefficient of linear term in the polynomial function of specific heat for the higher phase.
  • Quadratic T Coefficient (High T Phase): This is the coefficient of quadratic term in the polynomial function of specific heat for the higher phase.
 

Figure 5.130 - Phase Change model

  Note: For information on how to model phase change, refer Windshield Defrost Tutorial.

 

User Defined Enthalpy

The enthalpy can be specified as a function of pressure and temperature i.e., using the Expression Editor under Value by selecting User Defined Enthalpy. It can have only variable such as temperature.

The input text file for two variables (pressure and temperature) data are created in 2-D table format and accessed using expression editor. For single variable (temperature) using 1-D table.

If user has and temperature data and wants to provide using User Defined Enthalpy. First, fit a curve for as function of temperature and then integrate the curve to get the enthalpy.

 

Figure 5.131 - User defined enthalpy

 

Example

The gas enthalpy is specified as function of pressure and temperature in 2D table format, as shown in Figure 5.132. In the solver, temperature is accessed from heat module as temp=heat.T and pressure is accessed from flow module as pres = flow.P as shown in Figure 5.133. It also shows the example of how to read table from expression editor.

Figure 5.132 - Pressure and temperature data in 2D table format

 

Figure 5.133 - Accessing table from expression editor

  Note: For information on how to model user defined enthalpy, refer Rolling Piston Compressor with Real Gas Tutorial.

 

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