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January 8, 2007, 07:11 |
Turbulant heat transfer
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#1 |
Guest
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Hi.
I'm stuggling to get correct heat transfer using the k-e model. I'm trying to model heat transfer from fluid to a wall, using the k-e model, for a cylinder in a cross-flow. I've got y+ values in the range 30-300 as the good book suggests, but still the Nussult numbers are ten times higher than those suggested by an experimental correlation (Churchill & Bernstein, J Heat Trans. 99:300). Is there another criterion that I have to meet to make sure heat transfer is coorect? Anyone had similar experience? HELP!!! Thanks, Hugo. |
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January 9, 2007, 23:04 |
Re: Turbulant heat transfer
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#2 |
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Dear friend,
I think, as per my knowledge what ever are u getting is right. Wall function approach predictions for heat transfer is very poor though the fluid dynamic solution is very good. I have expierienced the same, when i applied for the offjet flows. particularly, in recirulating and strong curvature in strain rate. I suggest u to go for the non-equillibrium wall functions or RNG modelling. I got very poor results in tne recirculating region even qualitatively. |
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January 10, 2007, 05:00 |
Re: Turbulant heat transfer
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#3 |
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Hi Vishnu,
In fact I carried on and found that the Nusselt numbers Fluent was giving were rubbish, but the heat transfer was quite reasonable - if i calulated my own Nu numbers they were is very good agreement with the experimental correlation, as long as 30 < y+ <300, which is the general recommendation. I'll follow your suggestion and look at the non-equilib wall functions, but I want to avoid the RNG k-e model cos in my experience it didn't give good results for buoyancy driven flows, which is another part of the model. Cheers, Hugh. |
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January 17, 2007, 01:10 |
Re: Turbulant heat transfer
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#4 |
Guest
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Hi Hugo,
you could try the SST Model, too. It should be pretty usefull for buoyancy driven flows. Greetings! Fab |
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