Post-Pasteurization Cooling

Rapid Cooldown After Heat Treatment

Pasteurized product has to clear the danger zone fast

RAPID PRODUCT COOLDOWN

Out of the
Danger Zone, Fast

Pasteurized product has to clear the danger zone fast - the cooling side of the line is as time-critical as the heating side.

Pasteurization only accomplishes its job once the product is also cooled quickly afterward. Product held too long in the intermediate temperature range after heat treatment gives surviving organisms time to recover, so plate-and-frame or tubular heat exchangers on the cold side of a pasteurizer need a chilled fluid supply from an Advantage chiller, cold enough and steady enough to hit the required cooldown time every batch, every shift.

The Advantage chiller's job here is consistency under a swinging load: cooldown demand spikes when a batch comes off the pasteurizer and drops between runs, and a chiller sized only for average load will fall behind on the fluid temperature right when the product needs it most.

  • Rapid cooldown after heat treatment limits time in the food-safety danger zone
  • Chiller must hold fluid temperature through load spikes, not just average demand
  • Plain chilled water or glycol depending on the target product temperature
Sealed yogurt cups on a stainless conveyor after post-pasteurization cooldown

Depending on the target product temperature, this loop runs on plain chilled water or on a glycol solution - see Central Chillers for plant-wide chilled water or Glycol Chillers where the target temperature runs below what water alone can deliver.

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Sizing Post-Pasteurization Cooldown

Pasteurization cooldown is a race against the food-safety clock: product has to drop through the danger zone within a defined time window, which makes this one of the highest-peak, shortest-duration loads on a food plant's cooling system. The Advantage chiller has to deliver cold fluid fast enough to hit that window on every batch, not just on average.

Because cooldown typically happens in a plate-and-frame or tubular heat exchanger right after the pasteurizer, the chiller's flow rate and approach temperature both matter as much as raw tonnage - undersizing either one stretches the cooldown time even if total capacity looks adequate on paper.

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  • Product throughput and required cooldown time
  • Target leaving fluid temperature at the heat exchanger
  • Heat exchanger type (plate-and-frame or tubular)
  • Whether cooldown overlaps with other process loads on the same loop

What Post-Pasteurization Cooldown Requires

Danger-Zone Window

Flow & Approach Temp

28-38°F LFT

Plate Heat Exchanger

TYPICAL RANGES BY PRODUCT

Product Type Leaving Fluid Temp Load Profile Typical Fluid
Dairy / beverage pasteurization 28-34°F Batch, very high peak 30-35% propylene glycol
Juice / liquid egg pasteurization 30-36°F Batch, high peak 30-35% propylene glycol
Sauce / prepared-food pasteurization 34-38°F Batch, moderate peak 25-30% propylene glycol

The cooldown window you have to hit, at your throughput, is what sets the leaving fluid temperature - the table only shows where that usually lands.
Call and talk it through with an engineer: 1-805-484-2992.

Regeneration, vat cooldown and stored cold glycol

Most of it, which is why its condition matters. Take an HTST line running 3,000 gal/hr of milk held at 161°F, with raw milk entering at 38°F. At 90% regeneration the pasteurized milk leaves the regen plates near 50°F, and the glycol section only finishes it to 36°F: about 340,000 BTU/hr, or 28 tons. Let fouling drag regeneration to 85% and the milk arrives near 56°F; the same finish now needs about 41 tons. The chiller did not change - the plates did. We size with margin for a regen section partway through its run, not freshly cleaned.

Usually not. A 500-gallon vat of milk cooled from 145°F to 40°F gives up about 420,000 BTU; doing all of it on glycol in one hour is a 35-ton peak for a few hours of use a day. Many plants run tower or city water through the jacket first, down to about 90°F, then switch to glycol for the last 50°F. The glycol share falls to roughly 200,000 BTU, about 17 tons if that stage gets an hour, and the Advantage chiller is selected for that. Keep the water stage quick, though: the product is in the danger zone the whole time.

Around 32°F, with flow sized to match. A plate section typically closes to within a few degrees of the incoming fluid, so a 36°F target with a 4°F approach puts the glycol supply near 32°F. For the 28-ton HTST duty above, use about 470 BTU/hr per GPM per °F for 30% propylene glycol rather than 500 for water: at a 6°F glycol rise that is about 120 GPM. Halve the flow and the rise doubles to 12°F, the glycol leaves the plates warmer, and product comes out above target even though the chiller still has capacity.

Yes, when bursts are short and spaced out. Say the vat's glycol stage needs 200,000 BTU in one hour, once every four hours. Averaged, that is 50,000 BTU/hr, a little over 4 tons. A tank of 30% glycol allowed to warm 10°F holds about 79 BTU per gallon, so roughly 1,900 gallons covers the 150,000 BTU the small chiller cannot supply during the hour, and the chiller recharges it over the next three. That trades a 17-ton chiller for a 4-5 ton unit and a larger reservoir. It fails when batches come closer together than planned, so size storage for the tightest schedule rather then the average day.

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