Femtet Help/Manual
 

Home / Examples / Thermal Analysis [Watt] / Example 17: Temperature-Dependent Heat Source (Transient Analysis)

Example 17: Temperature-Dependent Heat Source (Transient Analysis)

  

General

  • The model is the same as Example 8: A heat source is placed on a substrate, and there is a forced air flow for cooling in parallel to the substrate.
    The heat transfer is analyzed under the transient condition. The heat source is temperature-dependent.
     

  • The coefficient of heat transfer of forced convection is acquired manually.
    To acquire it automatically, see [Ex.1 of Simple Fluid-Thermal Analysis].
     

  • The temperature distribution and the heat flux vectors are solved.
     

  • Unless specified in the list below, the default conditions will be applied.
     

  • Obtain this session's project file. (Right-click and choose 'Save link as')


  • Results will vary depending on Femtet version and the PC environment.

 

Analysis Space

Item

Settings

Analysis Space

3D

Model Unit

mm

 

Analysis Conditions

Item

Settings

Solver

Thermal analysis [Watt]

Analysis Type

Transient Analysis

Options

N/A

 

The transient analysis tab is set up as follows. The number of calculation steps is 20. The timestep is 30 sec.

Therefore, the temperature distributions for 600 sec are solved.

Tab

Setting Item

Settings

Transient analysis

Table

Number

Number of Calculation Steps

Output Interval

Timestep [s]

1

20

1

30

 

Initial Temperature

25 [deg]

Model

The same as example 7. The body attributes, the material properties and the boundary conditions are the same as well.

The substrate (VOL1) and the heat source (VOL2) are created as solid body box, and the heat quantity is defined in the body attribute of VOL2.

The coefficient of heat transfer for the top and bottom faces of the substrate and the top face of the heat source are calculated based on the simplified equation.

Body Attributes and Materials

Body Number/Type

Body Attribute Name

Material Name

0/Solid

VOL1

006_Glass_epoxy *

1/Solid

VOL2

001_Alumina *

* Available from the material DB

 

The heat quantity of VOL2 is set up as follows.

Body Attribute Name

Tab

Settings

VOL2

Heat Quantity

Heat Density

Temperature Dependency: Yes

 

Heat quantity is specified by heat density in the analyses where temperature-dependent heating materials are involved.

In example 8, we set 1[w] for the heat quantity of VOL2. As the volume of VOL2 is 800*10^-9 [m^3], the heat density is equal to

1.25 x 10^6 [W/m^3].

To evaluate the heat increase by temperature increase, use the Arrhenius equation. Using the following equation,

P(25) = 1.25 x 10^6 [W/m^3],

the following equation is given:

 

P(T) = 1.25 x 10^6 * exp(-0.15/(k*(T+273))) / exp (-0.15/(k*(25+273)))

 

where 0.15 [eV] is the activation energy and k is the Boltzmann constant.

Body Attribute Name

Item

Settings

VOL2

Nonlinearity Table

Select [Smooth Interpolation]

 

Temperature
[deg]

Heat Quantity
x10^6 [W/m^3]

Temperature
[deg]

Heat Quantity
x10^6 [W/m^3]

Temperature
[deg]

Heat Quantity
x10^6 [W/m^3]

25

1.25

155

7.365383041

605

59.18105993

35

1.51094343

205

11.26925562

655

65.85048973

45

1.804711948

255

15.90794507

705

72.47585198

55

2.132370783

305

21.15582761

755

79.02738627

65

2.494768691

355

26.88623825

805

85.48214754

75

2.892545312

405

32.98193112

855

91.82276684

85

3.326141169

455

39.339762

905

98.03640656

95

3.795809582

505

45.87196227

955

104.1138907

105

4.301629871

555

52.5055812

1005

110.0489868

 

Heat density's temperature plot is shown below.

Boundary Conditions

The coefficient of heat transfer for the forced convection is calculated as follows. The equation is given in Example 8: Heat Radiation by Forced Convection (Transient Analysis).

For the details, please refer to the Coefficient of Heat Transfer for Forced Convection

To acquire it automatically, see [Ex.1 of Simple Fluid-Thermal Analysis].
 

Boundary Condition Name/Topology

Tab

Boundary Condition Type

Settings

BC1/Face

Thermal

Heat Transfer/Convection

Coefficient of Heat Transfer: 17.26 [W/m2/deg]

Ambient Temperature: 25 [deg]

BC2/Face

Thermal

Heat Transfer/Convection

Coefficient of Heat Transfer: 27.3 [W/m2/deg]

Ambient Temperature: 25 [deg]

Results

The temperature distributions at each elapsed time are shown in the left figures below. The right figures are the results of Example 8.

The unit of the color scale is [deg].

At Minimum/Maximum Value on the Contour tab of [Graphics Setup], deselect [Automatic] and set 25 => 150.

There is almost no difference from Example 8 in 60 sec.

However, the temperature increases more than in example 8 at 300 and 450 sec as the heat increases with higher temperatures.

In 60 sec

In 300 sec

 

In 450 sec

 

 

Temporal change of temperature is shown below.

 

Unlike Example 8 where the convergence is seen at around 600 sec,

here in this example, the temperature continues to rise, indicating that thermal runaway is taking place.