TEMA defines seven shell types. Three of them account for nearly all U-tube work: the E shell for ordinary single-pass duty, the F shell where a longitudinal baffle restores counterflow, and the K shell where boiling requires vapor disengagement space. The front head is a separate decision and turns almost entirely on how often the tube side needs to be opened.
Shell type sets the flow path; baffles set the velocity and the heat transfer coefficient along it. Segmental baffles are standard, with the cut and spacing chosen together to get useful cross-flow without excessive pressure drop or unsupported tube span.
On a U-bundle the bend region needs its own support arrangement, because tubes there are longer, curved and more prone to vibration than anywhere else in the bundle.
A longitudinal baffle only delivers two genuine shell passes if it seals against the shell. Leakage across it short-circuits flow and erodes the counterflow advantage you paid for, and the leakage tends to worsen as the unit ages and the baffle distorts.
Where the temperature cross is severe, two shells in series is a more robust answer than one F shell, at the cost of more hardware and more nozzles.
TEMA U-tube designations explained. BEU, AEU, BKU and DEU differ only in the front head, and that difference decides cost, access and pressure rating.
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Orientation and mounting for U-tube heat exchangers. How horizontal, vertical and tank-mounted arrangements change venting, draining, supports and bun
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Honest comparisons of U-tube against fixed tubesheet, floating head, straight tube and plate and frame designs, including where the U-tube is the wron
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