Purchasing scenario
Suitable for B2B buyers comparing a complete industrial line, a new product route, an expansion line or a replacement of key process modules.
Apple processing line for cloudy juice, clear juice, puree, concentrate and aseptic ingredient products, with route selection based on crushing, pressing, enzymatic treatment, clarification and Brix target.



We manufacture turnkey apple processing lines for clear juice, cloudy juice, NFC juice, puree and concentrate production from fresh apples. The complete line can include raw fruit receiving, washing, sorting, crushing, pressing or pulping, enzyme handling, deaeration, pasteurization, optional concentration and bottle, pouch or aseptic bulk filling. The equipment route is defined by finished product first because clear juice, cloudy juice and puree use different downstream separation logic.
Suitable for B2B buyers comparing a complete industrial line, a new product route, an expansion line or a replacement of key process modules.
Typical reference only for preliminary planning: 0.5-10 t/h fresh apple intake; confirm by season, yield target and shift schedule.
The line can include receiving, washing, sorting, extraction, tanks, deaeration, heat treatment, evaporation when required, filling, CIP, utilities and PLC control.
Use the finished product table to separate process routes before asking for quotation.
| Finished Product | Process Route | Packaging Option | Key Engineering Concern |
|---|---|---|---|
| Clear apple juice | Crush, press, enzyme treatment, clarification, filtration and pasteurization | Bottle, pouch, hot-fill or aseptic bulk | Browning control, clarity, filtration load and oxygen exposure |
| Cloudy apple juice | Crush, press, deaerate, stabilize suspended solids and pasteurize | Bottle, pouch or chilled/NFC packaging | Cloud stability, sediment control and aroma protection |
| Apple concentrate | Juice extraction, clarification, evaporation, cooling and aseptic filling | Aseptic bag-in-drum or bulk tank | Target Brix, color protection, evaporator fouling and energy use |
| Apple puree | Crush, heat, pulp, refine, deaerate and sterilize | Aseptic bag, drum, pouch or jar | Particle size, browning, viscosity and sterilization holding time |
Reference route: Fresh apple receiving → washing → sorting → crushing → enzymatic treatment if required → pressing → juice clarification or cloudy juice holding → filtration if required → evaporation for concentrate → pasteurization / sterilization → filling → CIP.
Receive apples by crate, bin or bulk container and check variety, maturity, defects, starch or pectin risk and raw material temperature before setting the hourly feed rhythm.
Use soaking, bubble washing, spray washing or brush-assisted washing to remove soil, leaves and orchard debris before the apples enter inspection.
Remove rotten, bruised, moldy or immature fruit so browning, off-flavor and filtration load are not carried into the juice or puree section.
Crush apples into controlled mash for pressing or puree preparation. Knife or hammer setting should protect yield without grinding seeds or creating excessive fine solids.
For clear juice or concentrate routes, enzyme treatment can reduce pectin and improve pressing, clarification and filtration. Cloudy juice may use a different stabilization approach.
A belt press or suitable juice extraction system separates juice from pomace. Pomace moisture, juice yield and suspended solids should be checked during process design.
Clear juice uses clarification and separation logic; cloudy juice needs controlled holding and stabilization to retain natural body without heavy sediment.
Filtration is added for clear juice or concentrate feed. Filter load depends on variety, pectin, enzyme plan and upstream pressing quality.
Use evaporation only when apple concentrate is required. Feed Brix, target Brix, aroma retention, color and fouling risk decide evaporator selection.
Select plate, tubular or aseptic heat treatment according to juice clarity, pulp, viscosity, pH, shelf life and packaging format.
Choose bottle, pouch, hot-fill, chilled, carton or aseptic bulk filling after the shelf-life and distribution route are clear.
Plan CIP circuits for press, tanks, filters, heat exchangers, pipelines and fillers so sugar, pectin and pulp residues can be cleaned reliably.
Each equipment module below should be confirmed from product data, layout, sanitary target and utility conditions.
The washing and sorting system removes soil, leaves, stones, damaged fruit and unstable raw material before extraction. It normally combines soaking, bubble washing, brush washing or spray washing with inspection conveying. For apple processing line, this section protects downstream pulpers, pumps and heat exchangers from foreign material. It also gives operators a practical quality-control point before high-value processing begins.
Apple routes often start with controlled crushing before pressing. A hammer crusher can prepare mash, while a belt press juicer separates juice from pomace. If the target is puree, a double stage pulping machine is used instead of a pure pressing route. The choice affects juice yield, pomace moisture, solids load and downstream clarification.
A vacuum deaerator removes entrained air before sterilization or filling. This helps reduce oxidation, foaming and color loss, especially in juice, puree and nectar-base products. Deaeration must be selected by viscosity, temperature, flow rate and whether the product contains pulp. It is not only a quality device; it also stabilizes downstream filling behavior.
An evaporator is only required when the buyer wants concentrate, higher solids storage or ingredient density. A falling film evaporator is considered for lower-viscosity juice streams, while a forced circulation evaporator may be discussed for viscous or fouling-prone products. The RFQ should include feed Brix, target Brix, viscosity, heat sensitivity and cleaning interval expectations.
Heat treatment is selected from product viscosity, pulp content, particle size, pH and packaging route. A plate sterilizer can suit low-viscosity juice, while a tubular sterilizer or tube-in-tube sterilizer is used when pulp, fiber or viscosity increases. Sterilizer sizing should consider holding time, fouling behavior, CIP access and filling temperature.
An aseptic filling machine is used when the finished product needs shelf-stable bulk packaging in bags, drums or bins. It must be planned together with the sterilizer, sterile transfer line and SIP logic. For higher throughput, a double-head aseptic filling machine can be discussed. Packaging size, cap type, bag specification and filling temperature should be confirmed before quotation.
The CIP system cleans product-contact surfaces such as tanks, heat exchangers, pulpers, pipelines and fillers. Fruit products may leave sugar, fiber, seed residue, pectin, pulp or heat deposits, so cleaning circuits should be planned by soil type and sanitary risk. CIP design affects pipe routing, valve groups, water demand, chemical dosing and downtime between products or shifts.
A PLC control system connects process modules into a stable production sequence. It can manage pump interlocks, tank levels, sterilizer temperature, filling readiness, CIP recipes and alarms. Automation level should be defined by operator skill, batch traceability, data recording and whether the buyer needs recipe management. It is a quotation item, not an afterthought.
Values marked as typical reference only are for preliminary planning and must be confirmed by sample tests, buyer specifications and final engineering review.
| Parameter | Typical Reference | Why It Matters |
|---|---|---|
| Raw material | Fresh apples, mixed apple varieties, sorted industrial-grade apples, chilled apple raw material | Variety, maturity, defect level and receiving condition affect washing, yield and quality. |
| Finished product | Juice, puree, pulp, concentrate, nectar base or aseptic bulk product as applicable. | The finished product determines extraction, heat treatment, filling and utility scope. |
| Capacity | Typical reference only for preliminary planning: 0.5-10 t/h fresh apple intake; confirm by season, yield target and shift schedule. | Throughput drives equipment size, buffer tanks, utility demand and floor layout. |
| Initial Brix | Typical reference only for preliminary planning: about 10-14 Brix; test each harvest lot before equipment sizing. | Feed Brix affects mass balance, evaporation load and finished product standardization. |
| Target Brix | NFC or cloudy juice follows natural Brix; concentrate target must be specified by buyer and confirmed by product standard. | Target Brix determines whether concentration, dilution or blending is required. |
| Viscosity | Low for clarified juice; higher for cloudy juice or puree. Viscosity affects pump, deaerator and sterilizer selection. | Viscosity changes pump type, heat exchanger choice, deaeration and filling speed. |
| Fiber / seed / particle requirement | Seed damage and excess peel fragments should be limited; cloudy juice needs controlled fine pulp, puree needs stable particle size. | Particle limits determine pulper screens, refining stages and sterilizer type. |
| Heat treatment | Pasteurization, UHT, tubular, plate or tube-in-tube route to be confirmed from product and packaging. | Thermal process protects shelf life but can affect color, aroma and fouling. |
| Packaging | Bottle, pouch, can, jar, aseptic bag-in-drum, bag-in-bin or bulk tank. | Packaging affects filling machine, sterilization logic and storage conditions. |
| Steam | Confirm available pressure, capacity and boiler condition. | Steam shortage limits preheating, sterilization, evaporation and CIP. |
| Power | Confirm voltage, phase, frequency and installed power limit. | Electrical design affects motors, controls, pumps and installation cost. |
| Compressed air | Confirm pressure, dryness and air capacity. | Air is needed for pneumatic valves, filling machines and control instruments. |
| Cooling water | Confirm cooling tower, chilled water or process water availability. | Cooling capacity affects pasteurizer balance, filling temperature and product stability. |
| CIP | Define manual cleaning, semi-auto CIP or automatic CIP circuits. | Cleaning design affects hygiene, downtime, labor and long-term operating reliability. |
Choose a clear juice route when the buyer values transparency, filtration stability and concentrate compatibility. Choose cloudy juice when natural body and fruit character matter more than clarity. Choose puree when fiber and texture are part of the product value, and add evaporation only when concentrate storage or export is required.
Low-viscosity juice, pulpy puree and concentrated product do not use the same heat exchanger or holding logic. Confirm pH, viscosity, particles, packaging and shelf-life target before selecting plate, tubular or tube-in-tube sterilization.
Steam, cooling water, compressed air, power and CIP should be sized with the route. A line that is mechanically complete can still fail in operation if cleaning time, utility peak load or buffer capacity is underestimated.
These links help buyers review the process modules that normally drive quotation scope.
This section is written for RFQ preparation. Values are reference only until raw material tests, product specifications and final layout review confirm the process route.
Apple variety, firmness, storage condition and defect level affect crushing behavior, juice yield, browning risk and pomace moisture. Receiving and sorting should remove rotten fruit before the press section.
Juice routes usually use washing, sorting, crushing, enzymatic treatment where required, belt pressing, clarification or filtration, deaeration, sterilization and filling. Puree routes use pulping and tubular heat treatment instead.
The complete scope may include washing and sorting system, hammer crusher, belt press juicer, enzymatic tank, vacuum deaerator, falling film evaporator, sterilizer and aseptic filler. Confirm steam, power, compressed air, cooling water, drainage, CIP level and automation requirement before judging price.
This crop-specific review separates the main process decisions before capacity and equipment are finalized.
| Design Checkpoint | Reference Data or Decision | Effect on the Line |
|---|---|---|
| Product route | Define the pressing route versus puree route before sizing extraction equipment. | Juice needs crushing, pressing and optional clarification; puree needs pulping, refining and viscosity-aware heat treatment. |
| Press performance | Record fruit firmness, mash condition, press yield and pomace discharge moisture. | Pomace discharge behavior affects belt loading, wash demand, press stability and downstream solids balance. |
| Juice specification | Confirm cloudy, naturally settled or clear juice and the required clarification endpoint. | The endpoint determines enzyme holding, separation, filtration, evaporator feed quality and aroma exposure. |
| RFQ Item | Reference Information to Provide | Engineering Reason |
|---|---|---|
| Finished products | cloudy apple juice, clear apple juice, apple puree, apple concentrate and aseptic apple ingredient | Different products may share the same front end but require different pulping, heat treatment, filling and storage logic. |
| Critical concern | browning, press yield, pomace moisture, enzymatic treatment, clarification load, aroma retention and evaporator selection | This is usually where equipment sizing, material selection, cleaning design and quality risk become different from a generic line. |
| Capacity and season | Hourly intake, operating hours per day, harvest season or frozen raw material plan. | Capacity affects buffer tanks, utility peak load, staffing, front-end width and aseptic filler size. |
| Brix, pH, viscosity and particles | Use measured data when available. If not, mark values as preliminary planning references only. | These values decide pump type, heat exchanger style, deaeration, evaporation and filling behavior. |
| Packaging and shelf life | Aseptic drum, bag-in-bin, bottle, pouch, can, jar, frozen pack or chilled distribution. | Packaging changes sterilization, filling machine, SIP/CIP scope, logistics and finished product storage. |
Use these internal links to move from raw material route to equipment scope and quotation preparation.
The review focuses on the difference between pressed juice, clarified juice, concentrate and puree routes, including browning control, pomace handling and evaporation decisions.
The page supports early project evaluation. Typical values are reference-only; final equipment selection requires product data, utility conditions and RFQ confirmation. Read our engineering content methodology.
Direct answers below explain the decisions that change process scope, equipment selection and quotation quality.
Use a pressing route when the main product is apple juice or juice concentrate and separation of pomace is required. Use pulping and refining when the target is apple puree or a fiber-containing base. Variety, maturity, desired yield, solids target and downstream heat treatment should be confirmed before selecting either route.
Browning control starts with short transfer times, controlled crushing, limited air pickup and stable product temperature. Deaeration, antioxidant strategy and prompt heat treatment may also be discussed according to the recipe and market requirements. Equipment alone cannot correct long holding times or uncontrolled exposure between open processing steps.
Clear juice requires clarification and filtration targets that remove suspended solids, while cloudy juice retains selected fruit body and needs stable turbidity management. The choice changes enzyme treatment, separation equipment, heat exchanger selection, tank agitation and final appearance. It should be specified before a complete line and utility load are calculated.
An evaporator is required when the finished product is apple juice concentrate or when soluble solids must be raised for storage or transport. Feed Brix, target Brix, aroma recovery, heat sensitivity, viscosity and cleaning interval determine the evaporator discussion. NFC juice and ordinary single-strength juice do not automatically require concentration.
Pomace discharge should be planned around press throughput, residual moisture, floor drainage and the intended by-product route. It may be collected for pectin, feed, composting or disposal according to local conditions. Conveyors and collection areas need enough capacity to prevent pomace buildup from restricting the washing and pressing section.
For a useful Apple Processing Line quotation, include raw material, finished product, capacity, initial Brix, target Brix, viscosity, packaging format, utility conditions, factory layout, automation requirement and expected project timeline.