A sanitary exchanger is not simply an industrial exchanger built in stainless. It is a unit where every product-contact surface is smooth enough to clean, sloped enough to drain, and free of the crevices and dead legs where warm residue sits between production runs. The U-tube bundle helps here more than people expect, because it comes out of the shell in one piece and the shell has no rear head joint to hide a pocket behind.
This is the first decision and it drives everything after it. Running product through the tubes gives you a smooth, positively drained passage that CIP solution follows exactly, and it keeps the product volume small. The catch is the U-bend: you cannot mechanically clean through it, and on a viscous or particulate-bearing product that matters.
Running product on the shell side gives you a larger flow area, gentler velocities for shear-sensitive fluids, and a surface you can physically reach once the bundle is out. The cost is that shell-side drainage has to be engineered rather than assumed, because a horizontal shell will hold a puddle unless it is sloped to a low-point drain.
For clean utility duty — culinary steam heating a product stream, or chilled water cooling one — the usual answer is utility in the tubes and product in the shell, which also puts the fouling side where you can get at it.
Ra is shorthand for how easily a surface releases soil. A typical sanitary specification runs around 32 Ra on product contact and 40 Ra on exterior surfaces, with electropolishing available where a lower number is required. Below roughly 32 Ra the practical gains come more from consistency than from the number itself.
The important detail is where the finish can actually be achieved. The inside of a tight U-bend cannot be reliably mechanically polished or electropolished, which is a real argument for putting product on the shell side when a low Ra on every product-contact surface is a hard requirement. We would rather raise that at quotation than have it surface during qualification.
Tell us how the unit will be cleaned and the rest of the specification follows. CIP recirculation sets minimum velocities and therefore nozzle and pass arrangement. SIP with clean steam sets the slope, the vent and drain locations and the thermal cycling the bundle will see. Manual strip-down sets the clearance you need around the shell to pull the bundle.
Cleaning chemistry also drives alloy. Hot caustic is straightforward in 316L. Chlorinated sanitizers, brine-bearing streams and some acid cycles are not, and chloride stress-corrosion cracking is the failure mode that catches stainless in food plants. Where the chloride load is real, duplex or a higher alloy is the honest answer.
Regeneration, heating and cooling sections where pressure differential rules keep product above utility at all times.
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Bringing caustic, acid and rinse water to setpoint fast, in an exchanger that is itself fully CIP-able.
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Clean and culinary steam generation and condensing, where condensate purity is part of the product specification.
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