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The log mean temperature difference (LMTD) correction factor is not required during heat transfer rate calculation in

  • A.plate heat exchanger
  • B.1 shell pass and 1 tube pass heat exchanger
  • C.1 shell pass and 2 tube pass heat exchanger
  • D.2 shell pass and 4 tube pass heat exchanger

Answer: B

No correction factor is needed for a 1 shell pass and 1 tube pass heat exchanger.

The LMTD formula is exact only for pure parallel flow or pure counterflow. A 1-1 shell-and-tube exchanger is one of these: the shell fluid and tube fluid each make a single pass, so the exchanger is analysed directly as counterflow (or parallel flow) with F = 1.

In 1-2 and 2-4 shell-and-tube exchangers the tube fluid reverses direction, so part of the exchanger runs in parallel flow and part in counterflow; the true mean temperature difference is less than the counterflow LMTD and a correction factor F below 1 is applied. Plate heat exchangers are also normally treated with a correction factor, because their pass and channel arrangements depart from pure counterflow; the key takes the 1-1 shell-and-tube exchanger as the case that needs none.

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