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Two pass shell heat exchanger with longitudinal baffle.

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Twink21

Chemical
Joined
Dec 3, 2018
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CZ
Hello engineers,

I am trying to find the coefficient called the "Correction Factor" for Log Mean Temperature Difference (LMTD) for this type of a heat exchanger. I cannot find the coefficient or any diagrams for this particular one in the literature. Does anyone know how to determine it? It is almost perfect countercurrent, I suppose it should be near 0,9.

u_tube2_fm8pfu.png
 
Based on there being a perfect seal of the long baffle, and two tube passes, I would use a LMTD correction factor of 1.0.
 
See also discussion and caveats on page 11-5 of Perry Chem Engg Handbook 7th edition.
 
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