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Heating, holding and cooling

Tomato paste thermal-treatment system

Tomato paste needs a product circuit that remains controllable as viscosity and particle content change. Tubular and tube-in-tube configurations provide family options for heating, holding and cooling such streams. Select the passage, pumping and controls around the validated product process and the package that follows.

Thermal skid with horizontal tube banks, a central vessel, valves, instruments and a right-side cabinet
Continuous thermal-treatment skid with tube banks, a central vessel and accessible controls.
Family options
Tubular and tube-in-tube heat transfer
Temperature reference
72–150 °C, selected configuration
Holding reference
15–120 seconds, selected configuration

Match the product passage to viscosity and particles

Concentrated paste, screened puree and formulated ketchup do not create the same pressure drop or heat-transfer behaviour. Specify the product condition and maximum accepted particle profile for the selected passage. The product-side pump and the heat exchanger must be assessed together.

The process diagram defines the heating, holding, cooling and product-routing functions. It should identify instruments and vessel connections, including the response to a loss of heating service or an interruption at the filler.

Configuration references, not a production recipe

These values describe the configurable equipment family. The required operating point comes from the actual formulation, flow, package and process validation. It is not selected by applying the same temperature and holding time to every tomato product.

ParameterFamily referenceCondition to establish
Temperature72–150 °CRequired validated product duty
Holding time15–120 secondsHolding geometry and verified product flow
Heating and coolingHot water or steam; cooling water or chilled service optionsAvailable utilities and required outlet condition
Contact material304 or 316L optionsProduct and cleaning exposure, selected seals

Control residence and temperature together

For a fixed holding arrangement, changing product flow changes residence. The flow measurement, temperature sensing and route for out-of-condition product therefore form one control task. Reducing throughput to suit a filler should not be treated as an unrelated adjustment.

Define the criteria for startup release, interruption recovery and return from cleaning. Records should associate the observed process condition with the production lot; a displayed setpoint alone does not establish that every portion followed the required process.

Separate bulk aseptic filling from retail processing

An aseptic bulk route needs a maintained product boundary through the downstream transfer and filling head. A retail can route instead coordinates the selected filling condition, closure and any postfill treatment with the complete package process. The two interfaces should not share an assumed shelf-life claim.

CIP must reach the selected product circuit, with a defined return and access to seals, valves and serviceable tube connections. Break preheating is an earlier preparation duty and remains distinct from this final product treatment.

Further detail

Questions about this equipment and process

Does the family temperature range guarantee commercial sterility?

No. Equipment range and validated product process are different. The formulation, product flow, thermal history, packaging and hygienic boundary determine the required validation.

Can this be combined with an existing filler?

It can be assessed around the filler’s inlet conditions, interruption behaviour, hygienic interface and control signals. Those connections must be defined before fixing the thermal configuration.

Make the next connection

Put the production scope together.

Discuss the feed material, the product and the machines you need for the next stage.

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