Derive \epsilon - NTU Expression for Double-Pipe Counter Flow Heat Exchanger

AI Thread Summary
The discussion focuses on deriving the \(\epsilon - NTU\) expression for a double-pipe counter flow heat exchanger. The user is struggling to algebraically manipulate the equation from the logarithmic form involving temperature differences to the desired expression relating heat transfer rates and capacities. They have attempted to relate the heat transfer equations and efficiency but ended up with a complex mixture of terms involving \(C_{min}\) and \(C_{max}\). Key equations provided include the relationships for heat transfer rates and the definitions of \(C_{min}\) and \(C_{max}\). Assistance is requested to simplify the derivation process and clarify the algebraic steps needed.
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Homework Statement



I'm trying to derive the \epsilon - NTU Expression for a double-pipe counter flow heat exchanger. I know what I need to do the only problem I am having is:

I don't know how to algebraically go from

ln( \frac{\Delta T2}{\Delta T1} ) = -UA ( \frac{1}{Ch} + \frac{1}{Cc} )

to

ln( \frac{Th,o-Tc,i}{Th,i-Tc,o} ) = -\frac{UA}{Cmin}(1-\frac{Cmin}{Cmax})

2. Homework Equations & attempt at problem

I said (1/Ch + 1/Cc) = (\frac{Th,i-Th,o}{q} + \frac{Tc,o-Tc,i}{q})

Then I used the relationship: \epsilon = \frac{q}{qmax}

where qmax = Cmin(Thi-Tci)

...so q = \epsilon * qmax

substituted these equations in ...

I have a giant mess of Cmin and Cmax

Any help is greatly appreciated!

The only other equations that may be beneficial are:

q = mh*Cph*(Th,i - Th,o)
and
q = mc*Cpc*(Tc,i - Tc,o)
and
\frac{Cmin}{Cmax} = \frac{mh Cph}{mc Cpc} = \frac{Tc,o - Tc,i}{Th,i - Th,o}
 
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