Hello all, sorry about the off topic question
How can the heat transfer and Pressure drop of a STHE as follows be estimated?
Tube bundle 380 1.1/4" staggered tubes on a 1 m shell.
Tube side entrance: water
Tube side exit: water
Shell side entrance: steam
Shell side exit: 20%mass steam + 80%mass water
Number of chicanes: 8
I've been looking at the TEMA Standard and some regular heat tranfer books (i.e. Incropera) and can't seem to find a procedure for this kind of calculation.
I believe that spliting the the heat exchanger calculation along it's length might lead to the solution, but still can't figure out hoe to do it.
Regards,
Carlos Eduardo Received on Fri May 16 13:16:00 2003
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