Fruitprocessingplant.com / Equipment and plant interfaces

Compare recovery, evaporation, treatment and filling routes

Select between equipment principles using product evidence, operating conditions and the proposed system boundary. This comparison does not substitute for a model-specific offer.

Recovering the useful intermediate

Sample or design evidence: Run representative material through the proposed recovery principle. Compare useful product, residue, clarity or texture and cleaning requirements on the same feed basis.

Belt Press Juicer

Consider when

Use mash trials to assess pressability, juice recovery, fines and pomace moisture.

Check the limit

A soft puree feed may blind the belt or behave poorly; nominal raw intake alone does not establish capacity.

Factory interface

Review belt washing, water demand, tensioning access and pomace conveyors with downstream juice buffering.

Double Stage Pulping Machine

Consider when

Select first-stage separation and second-stage screen duty from seed, peel, fibre and texture targets.

Check the limit

A finer second screen can reduce useful recovery or increase seed damage; two stages are not always necessary.

Factory interface

Plan rotor and screen inspection, safe screen changes, drainability and access for high-fibre deposits.

Decanter Centrifuge

Consider when

Request representative feed properties, trials, separation targets and solids-discharge behaviour.

Check the limit

A decanter and a polishing separator serve different solids ranges; clarification is not sterilization.

Factory interface

Review bowl and scroll service access, vibration provisions, solids handling and verified cleaning procedures.

Disc Stack Separator

Consider when

Set the required clarity, retained-cloud target, feed variation and solids discharge cycle.

Check the limit

It does not replace coarse preparation; removing cloud can conflict with the desired juice character.

Factory interface

Check bowl service access, safe operating procedures, discharge routing and cleaning verification.

Concentrating the recovered feed

Sample or design evidence: Supply concentration-dependent viscosity, fouling, feed range and quality limits. Compare the heat and mass balance at the same feed and final concentration.

Falling Film Evaporator

Consider when

Review film distribution, minimum wetting, heat sensitivity and fouling over the whole campaign.

Check the limit

High viscosity or poor wetting can defeat the selected film arrangement; assess turndown, not only maximum feed.

Factory interface

Plan distributor inspection, cleaning coverage, condensate segregation and steam, vacuum and cooling interfaces.

Forced Circulation Evaporator

Consider when

Assess viscosity rise, circulation rate, pump shear, fouling and allowable thermal exposure.

Check the limit

Circulation adds pumping and residence considerations; it is not automatically suitable for every viscous puree.

Factory interface

Review pump service, tube cleaning, seal access, drainage and product retained in the circulation loop.

Plate Evaporator

Consider when

Evaluate feed solids, plate gap, distribution, viscosity, fouling and the planned cleaning interval.

Check the limit

Particles or severe fouling may conflict with the plate geometry; the proposed feed must be reviewed.

Factory interface

Confirm plate-pack service clearance, gasket compatibility, leak management and cleaning inspection access.

Matching product treatment to its boundary

Sample or design evidence: Liquid treatment and sealed-package treatment are different routes. A qualified product-specific validation basis must cover the complete selected system.

Plate Sterilizer

Consider when

Review particle passage, heat duty, pressure relationship and product-specific validated holding conditions.

Check the limit

Narrow passages may not suit fibrous puree or larger particles; heat-exchanger choice alone does not validate the process.

Factory interface

Allow plate opening and gasket service; coordinate leak detection, CIP and sterile downstream transfer where required.

Tubular Sterilizer

Consider when

Review flow range, passage geometry, pressure drop, fouling and validated thermal requirements.

Check the limit

Product changes can invalidate an earlier holding or heat-transfer basis; published generic schedules are insufficient.

Factory interface

Coordinate tube inspection, instrument calibration, divert logic, cleaning and any defined sterile boundary.

Tube In Tube Sterilizer

Consider when

Use rheology at processing temperature, maximum particle size and hydraulic review to select the geometry.

Check the limit

Wider passages do not establish particle heating or holding performance; these require product-specific validation.

Factory interface

Check pump and valve access, retained product, cleaning return conditions and holding-section inspection.

Tunnel Pasteurizer

Consider when

Review container mass, loading density, heat penetration, closure integrity and zone balance.

Check the limit

Liquid flow rate cannot size the tunnel; package behaviour and validated container treatment govern the duty.

Factory interface

Review spray-zone access, conveyor service, water management, drainage and start/stop handling of packs.

Retort Sterilizer

Consider when

Define product heat penetration, package resistance, load pattern and process-authority requirements.

Check the limit

A generic time-temperature recipe is unsuitable; each product, pack and loading arrangement needs validation.

Factory interface

Plan basket handling, vessel inspection, interlocks, calibrated process recording and qualified maintenance.

Choosing the filling arrangement

Sample or design evidence: Compare cycle time, container exchange, preserved product supply and packaging conditions. State which systems establish the aseptic, hot-fill or chilled boundary.

Single-Head Aseptic Filling Machine

Consider when

Review bag fitment, product viscosity, particles, filling mass and container exchange time.

Check the limit

Head count is not a capacity guarantee; product supply, bag handling and sterile-boundary recovery also matter.

Factory interface

Agree CIP/SIP boundaries, fitment handling, steam and air requirements, access and sterile restart procedures.

Double-Head Aseptic Filling Machine

Consider when

Compare changeover overlap, feed availability, container movements and the complete filling cycle.

Check the limit

Two heads do not necessarily double delivered output; handling and sterile controls can be limiting.

Factory interface

Review independent head access, changeover isolation, CIP/SIP coverage and maintenance without unplanned product exposure.

Bottle Filling Machine

Consider when

Review bottle geometry, neck, net quantity, foaming, product temperature and container handling.

Check the limit

Bottle format does not imply aseptic or hot-fill capability; each system boundary must be specified.

Factory interface

Review product-contact cleaning, fill-valve access, change parts, conveyor interfaces and closure verification.

Non Aseptic Filling Machine

Consider when

Specify filling temperature, product rheology, package and closure tolerances, and downstream treatment.

Check the limit

A non-aseptic filler cannot alone establish ambient shelf stability; the complete preservation route must be validated.

Factory interface

Confirm nozzle and valve cleaning, drip control, closure handoff, drainage and container changeover access.

Discuss the selection evidence