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Search: Posts Made By: Lukas
Forum: STAR-CCM+ September 11, 2009, 11:45
Replies: 21
Views: 17,356
Posted By Lukas
I neednīt the heat exchanger tool, because Iīm...

I neednīt the heat exchanger tool, because Iīm not interested in heat transfer. For me is only the velocity relevant for analyzing the flow induced tube vibration.
Forum: STAR-CCM+ September 11, 2009, 11:24
Replies: 21
Views: 17,356
Posted By Lukas
Ok, I have the solution. Bramv101, thanks for...

Ok, I have the solution.
Bramv101, thanks for your help.
Forum: STAR-CCM+ September 11, 2009, 09:54
Replies: 21
Views: 17,356
Posted By Lukas
Ok, I will go for one constant Pi and Pv. Iīve...

Ok, I will go for one constant Pi and Pv.
Iīve got a tube bundle heat exchanger with liquid media. The tube bundle should be replaced by a porous media.

If I plot the dp/L (y- axis) and v...
Forum: STAR-CCM+ September 11, 2009, 04:24
Replies: 21
Views: 17,356
Posted By Lukas
I want to make the coefficients a function of the...

I want to make the coefficients a function of the velocity outside of the porous media, because this velocity isnīt constant.
Forum: STAR-CCM+ September 10, 2009, 06:17
Replies: 21
Views: 17,356
Posted By Lukas
Yes, the velocity is distributed over the face of...

Yes, the velocity is distributed over the face of the porous media. Because of this I think, that I will make a failure, if I calculate one coefficient for this different velocities.
Forum: STAR-CCM+ September 8, 2009, 10:09
Replies: 21
Views: 17,356
Posted By Lukas
This is fact. Iīm aware of this. But the velocity...

This is fact. Iīm aware of this. But the velocity of my fluid, before it permeates the porous media, is between 0 and 2,5 m/s. And for this velocity I have to define my coefficients. If i have a...
Forum: STAR-CCM+ September 2, 2009, 12:15
Replies: 21
Views: 17,356
Posted By Lukas
The problem is ,that my velocity isnīt constant,...

The problem is ,that my velocity isnīt constant, so my Pi changes, too.

Lukas
Forum: STAR-CCM+ September 1, 2009, 09:17
Replies: 21
Views: 17,356
Posted By Lukas
Ok, it sounds plausible, but Iīm not a expert...

Ok,
it sounds plausible, but Iīm not a expert in using Star-CCM+ :)
Can you give me a step by step manual to do that.
I just managed to create a table where the porous inertial resistance is...
Forum: STAR-CCM+ September 1, 2009, 04:30
Replies: 21
Views: 17,356
Posted By Lukas
Thanks for your answer, but how I have to...

Thanks for your answer,

but how I have to declare the field function, that it is according to my table?

Lukas
Forum: STAR-CCM+ August 31, 2009, 10:44
Replies: 21
Views: 17,356
Posted By Lukas
I calculated the pressure drop with equations...

I calculated the pressure drop with equations from the VDI heat atlas.
The porous inertial resistance can be calculated like this:

Pi = dp/dl * 1/vē

Is it allowed to remove the porous viscous...
Forum: STAR-CCM+ August 31, 2009, 06:57
Replies: 21
Views: 17,356
Posted By Lukas
porous inertial resistance

Hallo,

I want to model an tube bundle heat exchanger. The tube bundles are replaced by a porous media.
My problem is, that the porous inertial resistance is a function of to the fluid velocity.
...
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