A straight tube bundle has a tubesheet at each end. A U-tube bundle has one, because the tubes turn around inside the shell and come back. That halves the tubesheets, removes the rear head entirely, and removes the rear pressure-boundary joint.
The cleaning limitation. A brush, rod or lance will not negotiate a 180 degree bend. Tube interiors can be cleaned chemically and the straight sections reached with high-pressure water, but full mechanical cleaning end to end is not available. This is the single most important consequence of the geometry.
The pass limitation. Fluid enters one leg and leaves the other, so the pass count is always even. Where a duty needs a genuine temperature cross, an even-pass tube side cannot deliver true counterflow, and the answer is an F-shell, shells in series, or straight-tube construction.
Where the U-tube wins anyway. Free thermal expansion, no expansion joint, no rear seal, lower cost than a floating head, and full shell-side mechanical access. For duty with a clean tube side, that combination is hard to beat.
This is the practical rule that follows from everything above, and it is the reverse of the usual advice for straight-tube exchangers where the fouling fluid normally goes tube-side because it is easier to clean there.
On a U-tube unit the cleanable side is the shell side. Treated cooling water, clean steam, refrigerant and closed-loop glycol belong in the tubes. Process streams that foul belong in the shell where the bundle can be pulled and the surface reached.
U-tube compared with fixed tubesheet heat exchangers: cost, cleaning access, expansion joints, thermal cycling and how to decide between them.
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U-tube compared with floating head heat exchangers. Both remove the bundle and absorb expansion, so the decision turns on tube-side cleaning and joint
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U-tube shell and tube compared with plate and frame exchangers: approach temperature, footprint, pressure and temperature limits, fouling and gasket r
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