jabenj
Chemical
- Jul 14, 2009
- 1
Hi,
I'm working on calculating the heat transfer coefficient of a highly viscous polymer. I know the surface area of my reactor, the time it takes to cool a certain volume of the material, the cooling water supply temp and flow rate. I do not know the temperature differential of my cooling water.
Using batch data, I initially calculated the total BTUs/time of the cooling water supplied, then use that total BTU output in my heat transfer coefficient for the polymer material being cooled in my reactor:
q = h*a(delt T)
where q is my total BTU output of water used,
a is my reactor cooling surface area
and T is the change in temp of the material.
Am I approaching this correctly? I may have oversimplified the problem but not sure. I get 1417 BTU/h ft^2 per Deg F of material.
Does that value even make sense?
Any help would be greatly appreciated.
Thanks
I'm working on calculating the heat transfer coefficient of a highly viscous polymer. I know the surface area of my reactor, the time it takes to cool a certain volume of the material, the cooling water supply temp and flow rate. I do not know the temperature differential of my cooling water.
Using batch data, I initially calculated the total BTUs/time of the cooling water supplied, then use that total BTU output in my heat transfer coefficient for the polymer material being cooled in my reactor:
q = h*a(delt T)
where q is my total BTU output of water used,
a is my reactor cooling surface area
and T is the change in temp of the material.
Am I approaching this correctly? I may have oversimplified the problem but not sure. I get 1417 BTU/h ft^2 per Deg F of material.
Does that value even make sense?
Any help would be greatly appreciated.
Thanks