Home / Examples / Coupled Analysis / Fluid-Thermal Analysis [Bernoulli/Watt] / Example 16: Thermal-Fluid Analysis of Porous Medium

Example 16: Thermal-Fluid Analysis of Porous Medium


General

 

Analysis Space

Item

Settings

Analysis Space

3D

Model Unit

mm

 

Analysis Condition

Item

Settings

Solver

Fluid Analysis [Bernoulli]

Thermal Analysis [Watt]

Analysis Type

Fluid Analysis: Steady-state Analysis

Thermal Analysis: Transient analysis

Laminar Flow/Turbulent Flow

Select Turbulent Flow

Meshing Setup

General Mesh Size: 10 [mm]

 

The setting on the transient analysis tab are as follows. The total calculation steps is 200. The timestep is 0.1 [s].

Therefore, the temperature distributions for 200 [s] following an initial temperature of 25 deg are analyzed.

Tab

Setting Item

Setting

Transient Analysis

Table

Number

Calculation Steps

Output Interval

Timestep [s]

1

200

1

0.1

 

Initial Temperature

Use ambient temperature (25 [deg])

 

Model

The cylinder is a solid with its center part having larger diameter. The material of air (000_Air) is defined.
The body attribute of the center part of the body is a porous domain.

 

  

Setting of Body Attributes, Materials, and Mesh Sizes

Body Number/Type

Body Attribute Name

Material Name

2/Solid

Porous

000_Air

5/Solid

Pipe

000_Air

6/Solid

Pipe

000_Air

* Available from the material DB

 

The porous part is set on the fluid tab as follows medium.

Body Attribute Name

Tab

Settings

Porous

Fluid

Fluid Body Type: Porous Medium

Velocity Dependency: Calculate from porosity

Porosity: 0.39

Particle Diameter: 10 [mm]

Shape Factor: 1.0

Material of Solid: [001_Al]

 

Boundary Condition

Boundary Condition Name/Topology

Tab

Boundary Condition Type

Settings

Inlet/Face

Fluid-Thermal

Inlet

Specify flow velocity

Flow Velocity: 10 [m/s]

Inflow Temperature: Direct Entry, 100[ deg]

Outlet/Face

Fluid-Thermal

Outlet

Natural Outflow

 

Results

By switching the solver from thermal to fluid, the results related to the fluid analysis such as flow velocity and pressure are obtained.

 

The velocity vectors on the cross section at y=0 are shown.

The averaged flow velocity is displayed for the inside of the porous part. (The velocity in the porous part is at its highest value according to the porosity)

 

 

Below is the plotting of the flow velocity from the coordinates (0,0,0) to the coordinates (500,0,0).

 

The averaged flow velocity inside of the porous part is about 1.58 [m/s].

 

Below is the pressure (static pressure) distribution.

The pressure in the porous part shows a large drop in the porous portion toward the outlet.

 

 

If [Calculate from Porosity] is selected in the setting, the coefficient of porous is obtained by the Ergun equation.

The calculation log shows the details.

 

 

With the averaged flow velocity of 1.58 [m/s] in the porous part and the porous part’s length of 200 [mm], the pressure loss in the porous part can be roughly calculated as follows.

 

Pressure loss ΔP = (170.873 * 1.58 + 2058.73 * 1.58 * 1.58 ) * 0.2 = 1094 [Pa]

 

 

Pressure drop in the pressure distribution matches very well.

 

Now, let’s switch the solver type to thermal analysis from fluid analysis to examine the thermal analysis results.

 

The results at 0.1 [s], 5 [s], and 20 [s] are shown below. The maximum and minimum values of the contour diagram are 100 [deg] and 20 [deg], respectively.

 

The temperature at the inlet rises to 100 [deg] over the time as short as 0.1 [s].

The heat spreads through the inside of the porous part over a long period of time.

That is due to the fact that the specific heat and the density of aluminum are much larger than those of air.

 

0.1 [s]
5 [s]
20 [s]