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Testing and Benchmarking Discuss, design, and debate ways to evaluate the performace of he goods out there. |
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#82 |
Cooling Savant
Join Date: Oct 2001
Location: Wigan UK
Posts: 929
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Same model as here
Imput values : Water :- Cg=4171w/kg, Density=998.2kg/m^3, Cond=0.599w/m*c, Kinematic Viscosity=1.006e-6 m/s, (Calculated Thermal Diffusivity= 1.430e-7m^2/s, Calculated Prandtl No=6.99) 15% Antifreeze:- Cg=3962.w/kg, Density=998.2kg/m^3 Cond=0.545w/m*c,Kinematic Viscosity= 4.353e-6 m/s, (Calculated Thermal Diffusivity= 1.378e-7m^2/s, Calculated Prandtl No= 31.59) Values possibly a bit ugh but...... ![]() ![]() |
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#83 |
CoolingWorks Tech Guy Formerly "Unregistered"
Join Date: Dec 2000
Location: Posts: 2,371.493,106
Posts: 4,440
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0.004-5 °C/W diff @ 4lpm ?
seems a bit much (but I've never used 15% - or even 0.5% antifreeze) HydrX is 0.3% ethylene glycol when mixed per inst I have chillers with antifreeze, next fill I'll make a 15% soln and we can ck the theory |
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#84 | |
Cooling Savant
Join Date: Oct 2001
Location: Wigan UK
Posts: 929
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![]() Quote:
Incoherent's measured value is more like 0.003 - Incoherent's data |
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#85 |
CoolingWorks Tech Guy Formerly "Unregistered"
Join Date: Dec 2000
Location: Posts: 2,371.493,106
Posts: 4,440
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hmmm
you have more confidence in your calcs ? |
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#86 |
Cooling Savant
Join Date: Oct 2001
Location: Wigan UK
Posts: 929
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No, but think they ballpark.
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#87 | |
Cooling Savant
Join Date: Sep 2003
Location: Vallentuna, Sweden
Posts: 410
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I'll clean some of this data up later using an average of many measurements for the water only. Also I am not sure about the antifreeze. The Swedish part of the product description (which I can read) makes no mention of strength but the danish (which I cannot read properly) section mentions "60-100%" I don't quite know what this means. If the solution is already lower than 100% perhaps the numbers make some sense. There is the problem of my flowrate calculation. A fairly small shift (left or right on the graph) could affect the values. Flow measurement is a problem. Some methods work well at low flowrates, some at high, none work well over the whole range. Been bugging me for a while. Some more work is clearly needed. I will try and improve the resolution of my pressure drop sensor. Currently it is about 0.12kPa, way too low resolution for the lower flowrates. Not this weekend though. I'm off to Riga, Latvia. |
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