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mustang_steve said:I thought HydrX was antifreeze?
from having to siphon prime my loop a few times in the past...tehy sure do both taste the same![]()
TwEaKd said:the increased viscosity and density of a 10% solution would make a +1.6% difference in the Reynolds number of the flow, this would increase the heat transfer coefficient by 1.5% and decrease flow bysomewhere close to the same. the higher viscosity isn't going to hurt you any more than it will help
Show how you calculated that.TwEaKd said:the increased viscosity and density of a 10% solution would make a +1.6% difference in the Reynolds number of the flow, this would increase the heat transfer coefficient by 1.5% and decrease flow bysomewhere close to the same. the higher viscosity isn't going to hurt you any more than it will help
Ahhh, there it is. The Reynolds number is higher with water than glycol, but you're saying it's even higher than water with 10% glycol...TwEaKd said:Water 1166081.871 *velocity*diameter
ethylene gylcol 70955.41401 *velocity*diameter
16.43400842 times as high
10% solution 1.643400842 times as high
Are you calculating your Nusselt number with 0.8*Re or Re^0.8? And you have to take into account the change in the Prandtl number from the changes in both thermal conductivity and specific heat, can't just use conductivity.heat transfer coefficient is calculated using (Reynolds number)0.8
and the thermal conductivity of the fluid, which is about twice as much for water
1.301523718
The pipes/tubing/blocks we use generally have a relative roughness <0.0001. If you look at your Moody diagram, you'll see that flow won't become fully turbulent until Re>10^6. We operate solidly in the transitional realm where the Darcy friction factor increases rapidly with decreased Re.Using the turbulent flow equation and the Moody chart, (trust me on this one)
The flow rate will be reduced by about 5 or 6 %
HeThatKnows said:Ahhh, there it is. The Reynolds number is higher with water than glycol, but you're saying it's even higher than water with 10% glycol...
Are you calculating your Nusselt number with 0.8*Re or Re^0.8? And you have to take into account the change in the Prandtl number from the changes in both thermal conductivity and specific heat, can't just use conductivity.
The pipes/tubing/blocks we use generally have a relative roughness <0.0001. If you look at your Moody diagram, you'll see that flow won't become fully turbulent until Re>10^6. We operate solidly in the transitional realm where the Darcy friction factor increases rapidly with decreased Re.