Between extraction and continuous processing

Juice buffer tanks and transfer

A process vessel receives the juice from extraction or separation and supplies the following operation through a matched transfer circuit. Level control and usable vessel volume help bridge variation between the press and continuous liquid-processing equipment.

Connected stainless process vessels with lower valves and product pipework
Process-vessel construction with accessible lower connections and pipework.
Sizing flow
Recovered juice at the tank inlet
Volume
Usable range between operating levels
Transfer duty
Product flow and downstream pressure

Use the level range to absorb a defined variation

Extraction and finishing do not always deliver a perfectly even flow. A buffer provides liquid inventory while the downstream feed follows its chosen operating rate. The low and high operating levels define the volume available for that purpose.

Set that volume from the duration and size of the expected imbalance. Excess inventory also brings product residence, cleaning and changeover consequences. It cannot correct a sustained mismatch between extraction and downstream capacity.

Select the vessel arrangement for the juice character

The photographed top-drive vessels illustrate an agitated configuration. Where pulp distribution must remain consistent, agitation can be evaluated alongside the outlet arrangement and permitted air entry. The chosen impeller and mixing duty follow the actual juice properties.

Clarified juice and pulp-containing juice can place different demands on holding and transfer. Include the incoming condition, intended operating temperature and permitted residence in the process specification. A general buffer tank is not an aseptic storage vessel simply because it connects to a thermal line.

Rows of process tanks with top drives, access covers, a walkway and overhead pipes
An agitated-vessel arrangement with top drives and service access.

Match the transfer circuit to its two ends

InputWhat it determines
Juice flow and viscosityRequired transfer duty at operating temperature
Fibre and permitted particlesPump passage and acceptable product handling
Suction arrangementAvailable inlet conditions and avoidance of unnecessary air entry
Receiving-machine pressurePump and pipe pressure duty
Operating levelsLow-level protection and upstream/downstream interlocks
Cleaning routeDrainage, valve positions and return path

Keep the tank duty separate from fruit intake

The flow after pressing and finishing depends on the prepared feed and the measured separation balance. Use that juice stream when selecting the buffer and transfer equipment. An incoming fruit figure in tonnes per hour cannot be entered directly as a tank feed in litres per hour.

Specify gross vessel volume and operating volume separately, then include the outlet, pump, bypasses and low points in the cleaning plan. Access for drain checks and instrument service should remain clear after pipe installation.

At this stage

Practical questions

Which pump type belongs after the juice buffer?

Select it from the juice properties, solids, flow, suction conditions and downstream pressure. The tank photograph or whole-fruit intake rate does not identify the pump duty.

Move your project forward

Make the connection
from fruit to juice.

Discuss a whole line, an extraction module or the next machine in your process.

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