An HTST system heats product to a defined temperature, holds it for a defined time in the hold tube, and cools it back down, recovering much of the heat through regeneration on the way. Each section is a separate thermal problem and the regulation governs the middle one.
Regeneration is where the economics live. Incoming cold product is heated by outgoing hot product, which cuts utility consumption dramatically. It also creates the condition that governs the entire system: two product streams at different microbiological status separated by a single wall.
The pressure differential rule. Pressure on the pasteurized side must exceed pressure on the raw side at all times, so that any leak in the regeneration section flows from safe to unsafe rather than the reverse. This is a regulatory requirement, not a design preference, and it constrains pump placement, valve arrangement and the entire system layout. It also stresses gasketed equipment, which is one reason tubular units earn their place here.
Where tubular beats plate. Plate exchangers dominate HTST regeneration because their close temperature approach makes regeneration efficient, and on clean low-viscosity products they are the right choice. Where they struggle is with particulates, fibres and viscous products, all of which block narrow plate channels, and with the pressure differentials the safety case demands. On juices with pulp, soups, sauces and products carrying inclusions, tubular is frequently the more reliable answer.
Fouling is protein burn-on. Denaturation at the heating surface depends on surface temperature rather than bulk temperature, so a hotter medium with less surface produces shorter run times between cleans. Reducing the heating medium temperature and adding surface area usually lengthens run length significantly, and on dairy duty that is the difference between cleaning once a shift and cleaning once a day.
The hold tube belongs to the design. Residence time at temperature is what actually achieves pasteurization, and it depends on the slowest particle rather than the average. Hold tube sizing, slope and the velocity profile through it are part of the same conversation as the exchanger, not a separate piping question.
Related pages: sanitary product cooling, product heating, 3-A sanitary construction and double tubesheet exchangers.
Pasteurized product must sit at higher pressure than raw product at all times, so any leak in the regeneration section flows the safe direction.
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