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When using ΔTLM for a shell and tube heat exchange...
1.
When using ΔTLM for a shell and tube heat exchanger, we cannot use the conventional formula for LMTD.
A.
True
B.
False
Answer» B.
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In a shell and tube heat exchanger, in the inner side fluid enters at 15℃ and leaves at 65℃. The shell has oil entering at 105℃ and leaving at 85℃. What is the value of correction factor F?
In a shell and tube heat exchanger, in the inner side fluid enters at 15℃ and leaves at 65℃. The shell has oil entering at 105℃ and leaving at 85℃. What is the value of correction factor coefficients R and P?
Which one of the following are correct relation of R and P?
In a shell and tube heat exchanger, in the inner side fluid enters at 15℃ and leaves at 65℃. The shell has steam at 1atm. What is the value of corrected LMTD and correction factor?
What is the value of Correction Factor?
When using ΔTLM for a shell and tube heat exchanger, we cannot use the conventional formula for LMTD.
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