andrejen88
Mechanical
- Jul 14, 2016
- 2
I'm doing an analysis of a fermentation process, where cooling water is used to cool down the fermenter, through some cooling coals and a coat.
I've found the Q needed to cool the fermenter: Q = dT*M*Cp
And I've found the overall heat transfer coefficient by using Q = U*A*dTm
During the process the mass flow rate changes, and in my analysis I observe, that U also varies a long with it.
So I have two basic questions: Firstly, is the overall heat transfer coefficient applicable when dealing with a cooling water system?
Secondly, does the overall heat transfer coefficient vary with flow rate, because the mass stream gets more turbulent and thus lowering the film resistance inside the pipe?
Sorry for my English (not originally English-speaking)
I've found the Q needed to cool the fermenter: Q = dT*M*Cp
And I've found the overall heat transfer coefficient by using Q = U*A*dTm
During the process the mass flow rate changes, and in my analysis I observe, that U also varies a long with it.
So I have two basic questions: Firstly, is the overall heat transfer coefficient applicable when dealing with a cooling water system?
Secondly, does the overall heat transfer coefficient vary with flow rate, because the mass stream gets more turbulent and thus lowering the film resistance inside the pipe?
Sorry for my English (not originally English-speaking)