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Blast Freezing Time is the time required for a product to reach a specified core temperature from its initial temperature. Product thickness, composition, packaging, entry temperature, airflow and the system’s capacity under actual operating conditions must be evaluated together. A reliable time estimate combines engineering calculations with product temperature measurements under representative loading conditions.
Before answering “How many hours does it take to freeze one tonne of product?”, the preparation and loading arrangement must be defined. One tonne of thin portions and one tonne of thick blocks should not be assumed to require the same processing time.
Prepared by: Hamza Ilıman
Last updated: 30 September 2026
The endpoint of a freezing cycle should be assessed at the product’s thermal centre. This is the point that remains warmest at the end of freezing; it does not necessarily coincide with the geometric centre under every product and loading condition.
For quick-frozen foods within its scope, Codex CXC 8-1976 specifies a thermal-centre temperature of −18°C or colder after temperature stabilization. Product quality and storage specifications may require a lower target. This temperature must not be confused with the room’s air-temperature setting. www.fao.org
For example, an air temperature of −35°C does not demonstrate that every package has reached −18°C at its core. Evaluating Blast Freezing Time requires records of both air and product temperatures.
| Factor | Information required for evaluation |
|---|---|
| Product geometry | Maximum thickness, shape and size variation |
| Product composition | Water, fat, sugar and other constituents |
| Initial and final temperatures | Entry temperature and required core temperature |
| Packaging | Material, thickness, container depth and air gaps |
| Air conditions | Temperature and velocity of the air reaching the product |
| Loading arrangement | Tray spacing, package orientation and airflow passages |
| Refrigeration system | Available capacity at the design operating conditions |
Removing heat from the centre of a thick product takes longer. Doubling the thickness does not necessarily mean that freezing time will only double. Maximum product thickness should therefore be specified alongside product weight.
Different formulations behave differently during freezing. The same heat-removal value per kilogram should not automatically be used for meat, fruit purée and a sweetened product.
ASHRAE explains that the thermal properties of foods depend on their composition and temperature. handbook.ashrae.org
A warmer incoming product requires more heat to be removed. The entry temperature stated in the quotation should represent the conditions measured during production.
Cartons, lids and trapped air within packages influence heat transfer. Testing should use the packaging intended for commercial production.
FAO’s freezing-time guidance identifies packaging and product thickness among the principal variables affecting the process. www.fao.org
Air velocity at the fan outlet does not, by itself, describe the velocity experienced by the product. Assessment should include airflow through the loaded racks.
Air can bypass the load through surrounding open spaces. Baffles and rack clearances should direct it through the gaps between products.
Compressor horsepower alone is insufficient. Refrigeration capacity should be compared at stated refrigerant, evaporating and condensing conditions. www.fao.org
The calculation involves two checks: the quantity of heat that must be removed and the rate at which heat can move from the product’s interior to its surface.
The product heat-removal requirement can be calculated using the enthalpy difference between the initial and final conditions:
Heat to remove, kJ = Product mass, kg × Enthalpy difference, kJ/kg
The enthalpy difference should include both temperature reduction and the heat released as water freezes. A simple calculation based only on temperature difference can omit the phase-change requirement.
When the target time is known, the average refrigeration capacity required for the product is:
Average product refrigeration capacity, kW = Heat to remove, kJ ÷ (3,600 × time, hours)
Use enthalpy data appropriate to the product composition and temperature range. ASHRAE’s thermal properties guidance explains the relationship between enthalpy, sensible heat and latent heat. handbook.ashrae.org
The following values are assumptions used to demonstrate the method. They are not measured properties of a particular food or a TunelGroup performance commitment.
| Calculation input | Assumed value |
|---|---|
| Net product mass | 1,000 kg |
| Enthalpy difference between initial and final conditions | 250 kJ/kg |
| Planned freezing time | 4 hours |
Total heat to remove = 1,000 × 250 = 250,000 kJ
Average product refrigeration capacity = 250,000 ÷ (3,600 × 4) = 17.36 kW
This result represents only the average product load. Heat entering through the room envelope, air infiltration, fans, packaging, trays and other loads must be evaluated separately.
If the other average loads, calculated over the same time period, are assumed to total 8 kW, the combined requirement becomes 25.36 kW. This is not sufficient on its own for final equipment selection: changing loads throughout the cycle and the actual operating conditions also require assessment.
These values describe thermal refrigeration capacity, not electrical input power.
Having sufficient total capacity does not prove that the centre of a thick package will reach its target within four hours. A separate time assessment using product geometry and thermal properties is necessary.
Plank’s equation and more advanced freezing models can support preliminary estimates. Their assumptions, packaging effects and irregular product shapes influence the result. The calculated Blast Freezing Time should be verified through product trials. www.fao.org
For further technical background, see FAO’s guide to freezing fruits and vegetables.
Daily production planning must include loading, unloading and other required downtime in addition to freezing. The following schedule is an illustrative planning example, not a record from an operating facility.
| Activity | Assumed duration |
|---|---|
| Loading | 20 minutes |
| Validated freezing process | 240 minutes |
| Unloading | 15 minutes |
| Preparation and downtime allowance per cycle | 25 minutes |
| Total cycle | 300 minutes / 5 hours |
Under these assumptions, a 20-hour available production window allows four completed cycles. If each cycle processes 1,000 kg, the scheduled capacity is 4,000 kg/day.
Quoting 5,000 kg/day based only on the four-hour freezing period leaves no time for the other activities. If the actual defrost and cleaning schedule requires more time, the daily target must be revised.
This comparison provides a practical checklist for preparing project acceptance specifications.
A commissioning record can include the following information:
| Record field | Example details |
|---|---|
| Product identification | Product code, formulation and batch number |
| Packaging | Dimensions, material and net fill weight |
| Loading | Rack layout and total product mass |
| Starting conditions | Start time and product entry temperatures |
| Measurements | Probe identification, location and temperature record |
| Completion | Time to reach the target and product inspection |
| Deviations | Door openings, alarms or interruptions |
Probe locations should represent products and load positions expected to cool most slowly. Recording several locations during initial trials helps establish the monitoring plan for routine operation.
The applicable food safety plan also needs separate consideration: freezing should not be treated as a process that eliminates all microorganisms. www.fao.org
TunelGroup’s shock-type evaporators and refrigeration units are product groups that can be evaluated together when planning a system. Tunelgroup Cooling Systems
A quotation request should go beyond describing a “one-tonne blast freezer.” A more useful specification is:
We require a blast freezing system for … kg of net product per batch, entering at … °C, with a maximum product thickness of … mm, using … packaging, and a target process time of … hours to reach the specified core temperature.
Add the room dimensions, number of daily batches, project location and available electrical supply.
For application information, explore TunelGroup’s blast freezer for meat and blast freezer for seafood pages, or contact TunelGroup to discuss the project.
No. A freezing time is meaningful only when the product and operating conditions are defined together. Different thicknesses, packaging or entry temperatures require reassessment.
No. The product’s heat-removal requirement matters, but so does the rate at which heat can be removed from its centre.
A capacity calculation alone should not be used to guarantee a freezing time. Any commitment should define the product, packaging, loading arrangement, operating conditions and acceptance test.
Products should be transferred promptly to frozen storage that meets the specified holding conditions. Transfer and storage arrangements should also be included in the production plan.
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