Optional air-removal step

Vacuum deaeration before downstream processing

Vacuum deaeration exposes the product to reduced pressure to release entrained air and reduce dissolved gas under selected conditions. It can be evaluated where air pickup affects downstream processing. The appropriate duty depends on the product state and the measured benefit, rather than adding the vessel to every line.

Vertical vacuum deaeration vessel with upper condenser structure, sight glasses, pumps and a control cabinet
Vacuum deaeration assembly with a vertical vessel, upper structure, instruments and skid-mounted pumps.

Equipment selection at a glance

Is this the right machine for your product?

Use it for
Controlled air removal from juice or puree
Main selection decision
Connect product temperature, vacuum and discharge.
Discuss when enquiring
Foam, carryover and downstream inlet conditions.
Process objective
Controlled removal of entrained air and dissolved gas
Position
Selected after product preparation
Key checks
Foam, carryover, temperature and transfer stability

Define where the air enters and why it matters

Pulping, open transfers and poorly matched tank agitation can introduce air. Before selecting deaeration, identify the relevant air pickup and the point where removal would help. Correcting an avoidable leak or splash at transfer may also improve the inlet condition.

Vacuum level, product temperature, exposed surface and residence interact. These conditions need to suit the viscosity and foaming tendency of the sea buckthorn stream. There is no fixed oxygen endpoint or nutrient-retention percentage assigned to this unit.

Keep product out of the vacuum service

Foam can occupy vessel space and carry material into the vapour path. The selected arrangement needs a stable liquid level and a clear response to carryover. Observe startup as well as steady running because air and foam loading can change while the line fills.

Vacuum treatment can also remove volatile components. Evaluate the product after the proposed duty rather than assuming that a stronger vacuum always gives a better result. Vapour handling and condensate routing belong in the equipment interface.

Measure the benefit at defined operating conditions

VariableDesign questionVerification
Product temperature and viscosityWill the stream distribute and pump reliably?Record inlet condition during the trial
Vacuum and residenceWhat air-removal duty is useful?Compare the chosen gas or foam measure before and after
Foam and entrainmentCan the vessel retain product in its intended route?Observe level changes and vapour-path carryover
Product qualityDoes the duty alter the intended sensory profile?Assess samples under the same handling conditions

Protect the benefit during the next transfer

An open, splashing discharge can introduce air again. Coordinate the deaerator outlet, downstream buffer level and pump suction conditions so that the next operation receives a steady stream.

Deaeration and concentration are different duties. This vessel is shown as an air-removal assembly; a concentration requirement belongs in the evaporator duty with a separate water-removal and solids balance.

Further answers

Equipment and process questions

Does this deaerator concentrate sea buckthorn juice?

Concentration is not the specified duty. A concentration system is selected from water removal, product composition, heat transfer and the required final concentration.

Is deaeration always necessary before filling?

No. Evaluate the actual air pickup, foaming and downstream requirements. The product trial should show what the selected step contributes.

The next step in your process

Put the equipment scope together.

Discuss the ingredient, the incoming material and the part of the line you want to build.

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