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Shell and Head Options

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.

  • E shell. Single pass, shell-side fluid enters one end and leaves the other. The default, and correct whenever pressure drop and temperature profile are not fighting you.
  • F shell. A longitudinal baffle divides the shell into two passes, giving something close to true counterflow. The remedy for a temperature cross a two-pass tube side cannot handle.
  • K shell. Enlarged above the bundle for boiling duty, with a weir setting liquid level and free space above for vapor to disengage.
  • J shell. Divided flow, halving the shell-side path length and cutting pressure drop sharply. Used where shell-side drop is the binding constraint.
  • Bonnet front head. Fewest joints and lowest cost. Opening the tube side means breaking the piping.
  • Channel front head. Removable cover exposes the tubesheet face with the piping intact. Worth the premium when the tube side gets regular attention.
E-Shell Single Pass:
U-Tube Construction
  • Removable bundle
  • Free thermal expansion
  • ASME code available
e-shell single pass u-tube heat exchanger
F-Shell Two Pass:
U-Tube Construction
  • Removable bundle
  • Free thermal expansion
  • ASME code available
f-shell two pass u-tube heat exchanger
K-Shell Kettle:
U-Tube Construction
  • Removable bundle
  • Free thermal expansion
  • ASME code available
k-shell kettle u-tube heat exchanger
Bonnet & Channel Heads:
U-Tube Construction
  • Removable bundle
  • Free thermal expansion
  • ASME code available
bonnet & channel heads u-tube heat exchanger

Shell and Head Options

Baffles Belong to the Shell Decision

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.

The F Shell Caveat

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.


Shell and Head Options


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Quotes - Engineering - Sales