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Old   January 8, 2007, 07:11
Default Turbulant heat transfer
  #1
Hugo
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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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Old   January 9, 2007, 23:04
Default Re: Turbulant heat transfer
  #2
vishnu
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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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Old   January 10, 2007, 05:00
Default Re: Turbulant heat transfer
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Hugo
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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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Old   January 17, 2007, 01:10
Default Re: Turbulant heat transfer
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Fab
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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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