A sanitary tube-in-tube exchanger runs the product through an inner tube and the utility through the annulus between that tube and an outer jacket. There are no baffles, no gaskets in the product path and no channel narrower than the product tube itself, so anything that fits through the inlet ferrule passes the exchanger. Modules are built in straight lengths and joined with sanitary return bends into a hairpin or serpentine bank, giving pure counterflow and a temperature cross that a single-shell exchanger cannot manage. Pressure capability runs to several hundred psi on the product side because the tube is a simple cylinder, and temperature is limited only by the gasket at the return bend.
Plates run out of room in two directions. Above roughly 500 cP the pressure drop through a plate channel grows faster than the heat transfer, and above a particle size of about 1/8" on chevron plates or 3/8" on wide-gap plates the pack plugs. Tube-in-tube has neither limit in practice: a 1-1/2" product tube passes diced vegetables, whole berries, pasta, rice and meat pieces, and a 2" to 4" tube passes whole fruit. Viscous products such as purees, pastes, ketchup, honey, cream cheese and yogurt with fruit are pumped through at whatever velocity the pump can supply, and the exchanger is sized to the actual coefficient at that velocity rather than to a plate assumption.
Because each module is a single pass in one direction and the modules are connected in series, the whole bank is in true counterflow. The product outlet can be brought above the utility outlet, a temperature cross that a single-shell exchanger cannot do, and the approach at the hot end can be a few degrees. Sensitive products also benefit from the modest wall temperature difference that counterflow allows: the utility is only as hot as the local product needs, which keeps proteins from denaturing on the wall and keeps fruit from cooking at the surface.
The number that governs a tube-in-tube design is product velocity. Viscous product in a smooth tube is laminar, and the coefficient in laminar flow depends on velocity and tube length in a way that rewards long, narrow tubes up to the pressure the pump can deliver. Particulate product has a different constraint: velocity high enough to keep solids suspended, generally 2 to 3 ft/s minimum, and low enough that shear does not damage the pieces. The sizing balances tube diameter, bank length and pressure drop against those limits, and the corrugated tube option is brought in when the laminar coefficient is too low for a practical length.
The bank is mounted with each module pitched toward its outlet and the return bends at the low points fitted with drains, so the product path empties by gravity. CIP is run through the product tube at pigging or brush velocity, and single-tube modules allow the inner tube to be withdrawn for inspection. On the utility side the annulus drains at the jacket connections. Because the inner tube and jacket run at different temperatures, one end of each module is free to move, either with a sanitary gland or an expansion element on the jacket, and that detail is what keeps a steam-heated bank from working the welds loose over a season.
For product that plates cannot pass and shells cannot keep clean, tube-in-tube is the construction that makes the process simple. Call and talk it through with an engineer: 1-805-484-2992
Anything viscous, above roughly 500 cP, and anything with particulates, pulp, fibers or whole pieces: fruit preparations, purees, ketchup and sauces, soups with pieces, yogurt with fruit, cream cheese, honey, baby food, pet food and plant-based products with inclusions. Clear liquids are usually more economical on plates.
Whatever fits through the product tube and its ferrule. A 1-1/2" tube passes diced product and berries; 2" to 4" tubes pass whole strawberries, peach halves and similar. The tube is chosen to the largest piece plus margin so nothing bridges at the return bends.
Yes. The jacket is a pressure vessel rated for plant steam, and steam-heated tube-in-tube banks are common for cooking and pasteurizing viscous product. Hot water is preferred where wall temperature must be tightly controlled to avoid scorching.
Product-to-product regeneration is possible by running cold product in the annulus, but the annulus is not as cleanable as the inner tube and this is done only with clean, low-viscosity product. Most viscous and particulate installations skip regeneration and accept the utility cost.
CIP through the product tube at a velocity that scours the wall, with the option to pig or brush the straight bores. Single-tube modules allow the inner tube to be pulled for direct visual inspection. Return bends are tri-clamped and can be removed.
150 psig is standard and several hundred psi is available because the product tube is a plain cylinder. High pressure matters with viscous product where the pump must push through a long bank.
Straight tube, U-tube and double tubesheet bundles built for steam, pressure and a clean CIP return.
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Close approach, regeneration and a pack that opens for inspection: the pasteurizer's construction.
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Two stainless sheets welded and inflated into a heat transfer surface that goes wherever the tank needs it.
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