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Water Block Design / Construction Building your own block? Need info on designing one? Heres where to do it |
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#1 |
Cooling Neophyte
Join Date: Apr 2004
Location: Europe/Slovenia
Posts: 6
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It is raining
![]() Click here Maybe in the future I will do a real fluid/solid thermal coupling analysis in ANSYS. (I'm having a little trouble with convergence & solid fuid coupling right now). |
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#2 |
Cooling Savant
Join Date: Dec 2003
Location: France
Posts: 291
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hrmm interesting.
Not too sure about the jet bore, I thought it was closer to 0.8mm. Also can you redo the sim for different flow rates? (if its still raining ![]() 1000l/min (even l/hour) might be a wee bit unrealistic... AFAIK 600l/h is about the max? |
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#3 |
Cooling Savant
Join Date: Nov 2002
Location: State College, PA
Posts: 338
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That's a pretty darn cool analysis. I'm not enough of a :geek: to understand all the theory behind it, but I am a math geek so I can follow the equations. The sim software is some very cool stuff!
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Goliath: 3.4E@3.91/Abit IC7, Maze4 (temporarily) + custom splitter to crazy 4-way watercooling parallel loop: X800XT @ 520/1280 + AC Twinplex, AC Twinplex Northbridge, Silenstar Dual HDD Cooler, Eheim1250, '85 econoline van HC + 2x120, 1x120 exhaust - polished aluminum frame panaflo L1As, 2x18GB 10K RPM U160 SCSI, 4GB PC4000. I wanna be BladeRunner when I grow up! Project Goliath - nearing completion. |
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#4 |
Cooling Neophyte
Join Date: Apr 2004
Location: Europe/Slovenia
Posts: 6
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Sorry my mistake -> 1000l/min is a typing mistake, 1000l/h is the right number.
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#5 |
Thermophile
Join Date: Sep 2002
Location: Melbourne, Australia
Posts: 2,538
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Something amiss with the projected value for h.
Testing shows that h, in practise, is estimated to be about 10x higher than what you have determined. Somewhat hard to follow without some dialogue, but I think what you've done is apply basic flow-across-a-surface convection calculations as if the cups were essentially a pipe with water running over the walls, which really isn't what's going on here. The difficulty here is that for constrained submersed jet impingement is that there is limited applicable theory available with which to work from. |
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#6 |
Cooling Savant
Join Date: Oct 2003
Location: Sussex
Posts: 109
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Edit:
Just read through the calcs more carefully and realised you mean thermal conductivity instead of heat transfer coefficient Last edited by WAJ_UK; 04-20-2004 at 11:38 AM. |
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#7 |
Cooling Savant
Join Date: Oct 2003
Location: Sussex
Posts: 109
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just out of interest what is the film coefficient. Sorry I'm being dim I just haven't heard of it before (probably due to being asleep in the lecture
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#8 |
Cooling Neophyte
Join Date: Apr 2004
Location: Europe/Slovenia
Posts: 6
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To Cathar
1. What do you mean by h ? 2. If the cup is long enough (i'd say if cup heigth > diameter) than the cascade is just heat transfer in a tube (i will give you an example of the velocitiy of water flowing trough a jet in a cup later), except of course for the base of the cup, for which I just assumed that the film coefficient is the same as in the tube (I could be way wrong here). To WAJ_UK 1. The film coefficient (type this in GOOGLE) is about the same as the heat transfer coefficient (W/m*K)only this time in the join between two different mediums (copper/water, copper/air) and is measured in W/m^2*K. lets say for heat transfering in the same medium (= heat conduction) Q=heat transfer coefficient *medium length*temperature difference lets say for heat transfering between copper/air (= heat convection, forced convection) Q=film coefficient *area*temperature difference |
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#9 |
Cooling Neophyte
Join Date: Apr 2004
Location: Europe/Slovenia
Posts: 6
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Examples for different block base thickness (Q=1000l/h, block dimensions the same as before).
1mm ![]() 2.5mm ![]() 5mm ![]() 7.5mm ![]() 10mm ![]() |
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#10 |
Cooling Neophyte
Join Date: Apr 2004
Location: Europe/Slovenia
Posts: 6
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And different flow rates:
1000l/h ![]() 900l/h ![]() 800l/h ![]() 700l/h ![]() 600l/h (the flow gets laminar, film coefficient only 730W/m^2K, something stinks here I know) ![]() |
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#11 |
Cooling Savant
Join Date: Oct 2003
Location: Sussex
Posts: 109
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RKB2 I think you are getting heat transfer coefficient confused with thermal conductivity
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#12 |
Cooling Neophyte
Join Date: Apr 2004
Location: Europe/Slovenia
Posts: 6
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>> RKB2 I think you are getting heat transfer coefficient confused with thermal conductivity
You are right, sorry english is not my mother language. And for Cathar: Water velocity trough the cup (warning the solution did not converge after 5000 iterations, so results may be wrong). ![]() ![]() |
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#13 |
Cooling Savant
Join Date: Sep 2003
Location: Vallentuna, Sweden
Posts: 410
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Some very good work here rkb2. I think with some tuning of your parameters you could start generating some really good data. The base thickness behaviour is particularly interesting, some higher resolution modelling when the jet dimensions are established more accurately, please?
Good stuff. Cheers Incoherent |
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