Frequently Asked Questions

A shell and tube exchanger whose tubes are bent into a U so both ends terminate in a single tubesheet. One fluid enters the channel, travels down one leg of every tube, turns through the bend and returns through the other leg. The other fluid flows around the outside of the bundle in the shell. Because the bend end is free-floating inside the shell, the tubes can expand and contract without stressing anything, and the whole bundle can be withdrawn for cleaning.

Two questions decide it. Does the shell side need mechanical cleaning, and is the temperature difference between shell and tubes large or cycling? If either answer is yes, a U-tube is usually the better exchanger. Fixed tubesheet is cheaper per square foot and lets you rod the tubes end to end, but the shell side can only be cleaned chemically and a large differential temperature forces an expansion joint into the shell.

Because the fluid physically enters one leg of the U and leaves the other, so it always makes at least two passes. Four, six and eight pass arrangements are built with pass partition plates in the channel, but they remain even. This matters when the process needs a temperature cross, where the cold outlet is hotter than the hot outlet. A two-pass tube side cannot achieve a true countercurrent profile, so the answer is an F-shell with a longitudinal baffle, two shells in series, or a different rear head type.

The shell side is cleaned mechanically: pull the bundle and hydroblast or brush the outside of the tubes. The tube side is a different story, because nothing rigid will pass through the bend. Tube interiors are cleaned chemically, with high-pressure water lances that reach only into the straight sections, or with flexible-shaft equipment that has real limits. This is why the standing advice is to put the clean fluid on the tube side of a U-tube exchanger.

As a working rule the centerline bend radius should be at least twice the tube outside diameter. Bending tighter than that thins the tube wall on the outside of the bend, so the tube gauge often has to increase to compensate. The innermost rows set an untubed lane down the center of the bundle, which is why a U-tube unit carries slightly fewer tubes than a straight-tube unit in the same shell.

Yes, and it is usually the cheaper move. The shell is a pressure vessel with no moving parts and frequently outlives several bundles. If you can send a nameplate photograph, the original drawing or the U-1 data report we can match the bundle to the existing shell, and replacement is a good moment to upgrade the tube alloy without changing anything about the fit.

Flow rate and identity of both fluids, inlet and required outlet temperatures, operating and design pressures, the allowable pressure drop on each side, and any code, alloy or hygienic requirements. Beyond that the useful information is practical: how far the duty turns down, what fouls, how the unit will be cleaned, and how much clearance exists to pull the bundle. If some of it is unknown, say so and we will size against a stated assumption.

Three letters for three components: front head, shell, rear head. On a U-tube unit the third letter is always U. BEU is a bonnet front head with a single-pass shell; AEU swaps the bonnet for a channel with a removable cover; BKU uses a kettle shell for boiling duty.

3-A is a sanitary equipment design standard with third-party verification and a symbol authorization, used mainly in dairy and food. ASME BPE is the bioprocessing equipment standard, governing surface designations, weld examination, dead-leg control and documentation. They are not interchangeable.

Yes. Our wider business covers fixed tubesheet and floating head shell and tube, plate and frame, brazed plate, air cooled, spiral and double pipe equipment. If your duty is better served by one of those, that is the recommendation you will get.