Date

2008/06/12 11:35:42


Contents

1. File Report
    Table 1  File Information for module flow 2d round6_001
2. Mesh Report
    Table 2  Mesh Information for module flow 2d round6_001
3. Physics Report
    Table 3  Domain Physics for module flow 2d round6_001
    Table 4  Boundary Physics for module flow 2d round6_001
4. User Data
    Figure 1
    Figure 2
    Figure 3
    Figure 4
    Figure 5
5. Summary and Conclusions


1. File Report

Table 1.  File Information for module flow 2d round6_001
Case module flow 2d round6_001
File Path C:\Documents and Settings\hhwieman\My Documents\aps project\mechanical\short fatter flow 2d rounded\module flow 2d round6_001.res
File Date 11 June 2008
File Time 08:34:45 PM
File Type CFX5
File Version 11.0
Fluids Air at 25 C
Solids c dummy,si dummy
Particles None
 

2. Mesh Report

Table 2.  Mesh Information for module flow 2d round6_001
Domain Nodes Elements
air 345900 1401302
c 150768 768963
si 26751 135377
All Domains 523419 2305642
 

3. Physics Report

Table 3.  Domain Physics for module flow 2d round6_001
Name Location Type Materials Models
air B249 Fluid Air at 25 C Heat Transfer Model = Thermal Energy
Turbulence Model = k epsilon
Turbulent Wall Functions = Scalable
Buoyancy Model = Non Buoyant
Domain Motion = Stationary
c B513 Solid c dummy Domain Motion = Stationary
si B596 Solid si dummy Domain Motion = Stationary
 
Table 4.  Boundary Physics for module flow 2d round6_001
Domain Name Location Type Settings
air inlet inlet Inlet Flow Regime = Subsonic
Heat Transfer = Static Temperature
Static Temperature = 23 [C]
Normal Speed = 8 [m s^-1]
Mass And Momentum = Normal Speed
Turbulence = Medium Intensity and Eddy Viscosity Ratio
air air c Side 1 F265.249, F262.249, F246.249, F263.249, F253.249, F2... Interface Heat Transfer = Conservative Interface Flux
Wall Influence On Flow = No Slip
Wall Roughness = Smooth Wall
air air si Side 1 F235.249, F258.249, F256.249, F234.249, F260.249, F2... Interface Heat Transfer = Conservative Interface Flux
Wall Influence On Flow = No Slip
Wall Roughness = Smooth Wall
air outlet outlet Opening Flow Direction = Normal to Boundary Condition
Flow Regime = Subsonic
Opening Temperature = 23 [C]
Heat Transfer = Opening Temperature
Mass And Momentum = Opening Pressure and Direction
Relative Pressure = 0 [Pa]
Turbulence = Medium Intensity and Eddy Viscosity Ratio
air sym air sym Symmetry  
air air Default F217.249, F218.249, F219.249, F220.249, F221.249, F2... Wall Heat Transfer = Adiabatic
Wall Influence On Flow = No Slip
Wall Roughness = Smooth Wall
c air c Side 2 F502.513, F496.513, F508.513, F503.513, F495.513, F5... Interface Heat Transfer = Conservative Interface Flux
c si c Side 2 F501.513 Interface Heat Transfer = Conservative Interface Flux
c c Default F493.513 Wall Heat Transfer = Adiabatic
si air si Side 2 F591.596, F584.596, F586.596, F594.596, F588.596, F5... Interface Heat Transfer = Conservative Interface Flux
si si c Side 1 F593.596 Interface Heat Transfer = Conservative Interface Flux
si si Default F592.596 Wall Heat Transfer = Adiabatic
 

4. User Data

Figure 1.
Figure 1 - ReportHighRes/Figure001.png
Figure 2.
Figure 2 - ReportHighRes/Figure002.png
Figure 3.
Figure 3 - ReportHighRes/Figure003.png
Figure 4.
Figure 4 - ReportHighRes/Figure004.png
Figure 5.
Figure 5 - ReportHighRes/Figure005.png

5. Summary and Conclusions

This air cooling analysis includes both air flow and heat transfer. This is the first of the module structures to be run in high resolution mode. It is still more limited than previous runs in that the structure is shortened still more to fit memory constraints.

Figures:

1. Temperature contour at mid plane

2. Silicon surface temperature

3. Stream lines with color indicating velocity

4. Contour of flow velocities at mid plane

5. Contour of flow velocities at three planes along the module

This shows only a 3.4 deg rise in the silicon temperature over ambient. Significant cooling of the silicon is a result of the carbon support tube which conducts heat away from the silicon adding significant area for transferring heat to the cooling air.

Some input boundary conditions:

Thermal power input is generated in the inner silicon ladder at the center (100 mW/cm^2)

Air inlet velocity 8 meters/sec

Outlet boundary condition: open, relative pressure 0

In order to work with the FEE approach very thin structures have been modeled as much thicker structures. The thermal conductivity parameter has been adjusted accordingly to give the correct conductivity along the plane, but then too low conduction perpendicular to the plane.

Concerns about current version of the model:

Too short to show velocity development from initial fixed velocity boundary condition at the entrance.

Too short so that air does not see full power input.

Only one silicon ladder producing heat, so again not getting the full heating of the air, but this may not be too big an error. Consider the full volume of air at this velocity is 284 ft^3/min and the power from the silicon is 160 watts - this gives only a 1 deg C temperature rise in the air.

This low value for air heating suggests that design improvements may be possible that require less total air flow volume. The design challenge will be to maintain good surface air velocities with reduced total flow.

This work must be checked with more careful analysis and prototype testing, but if these low temperature rises turn out to be correct then this means that it should be possible to run the system at ambient temperature which is a much simpler task than operating below ambient where significant work is required to prevent accidental condensation. It also avoids the need for extensive thermal insulation of the system.