Heat exchanger output temperature calculation

AI Thread Summary
The discussion revolves around performing CFD simulations for a stainless steel cylindrical heat exchanger, focusing on calculating the average outlet flow temperature using hand calculations. The user seeks guidance on which equations to apply, given the parameters of tank diameter, feed pipe diameter, surface temperature, inlet flow rate, and inlet temperature. They express confusion regarding the application of the Q=m(h2-h1) principle and the differences between Qw and qw. Responses suggest using the LMTD or ε-NTU methods for analyzing heat exchangers, specifically if the type is cross-flow or counter-flow. Clarification on the specific type of heat exchanger and parameters is needed for accurate assistance.
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Homework Statement



I have been asked to perform CFD simulations of a basic stainless steel cylindrical heat exchanger. I have to test a range of inlet temperatures and flow rates where external heat applied is constant.

I wish to perform basic hand calculation to verify my results by calculating the average outlet flow temperature but am unsure which equations to use for this. For example variables are as follows,

tank diameter 0.5m
feed pipe diameter 0.02m
tank surface temperature 135 degrees c
inlet flow rate 1l/min
Inlet temperature 50 degrees c

The tank thickness is not specified. The tank is heated by steam and the internal fluid is water.

Homework Equations



Thus far I have tried using variations on the Q=m(h2-h1) principle but have not been able to calculate this as i do not have enough information.

Should I be using Fw = Tw*pi*dl
then
Qw = qw*pi*dl=(Fw*cp*theta m)/Um

and how does qw differ from Qw?

I have basic knowledge of fluid flow and have not before this come into contact with thermodynamics.

Thanks in advance
 
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What type of heat exchanger are you talking about? I only know how to analyze two, cross-flow and counter flow.

Both are analyzed using the LMTD method or the ε-NTU method.

So if your exchanger is one of those two, I can probably give you some help. But I am not sure as to the parameters in your equations that you posted.
 
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