1. What APET Fresh Food Tray Sheet Is and Why Supermarkets Depend on It
Supermarket fresh departments sell meat, poultry, fish, cut vegetables, salad, fruit and deli items that must look appealing, stay hygienic and survive the cold chain from the shelf to the home refrigerator. A large share of these products now sit in rigid transparent trays formed from APET sheet, the amorphous grade of polyethylene terephthalate that is clear, stiff enough to stack, and easy to thermoform into a shallow tray. The sheet itself is the base web: a thermoforming machine heats it and draws it into the tray shape, so the quality of every tray begins at the extrusion line that makes the sheet.
This article explains how to build and run a dedicated APET fresh food tray sheet extrusion machine, the kind of line that produces the clear or barrier sheet used for supermarket meat and vegetable packaging base material. We cover material structures, full line architecture, each major unit with a price estimate in US dollars, drying and process setpoints, quality and food-contact rules, plant sizing, and the investment needed to reach payback. Wanplas, with its network of specialized factories, supplies APET sheet extrusion lines together with the downstream thermoforming, recycling and packaging machines that turn resin into finished tray programs.
APET is chosen over older alternatives because it stays clear, resists grease, seals well, and accepts both printed lidding and modified atmosphere. For red meat the tray is often a barrier structure that keeps the product red and fresh; for vegetables the tray may be a simpler clear or sealable sheet that lets the pack breathe. In every case the sheet must be uniform in thickness, free of gels and black specks, and compliant with food-contact law, because the tray touches food directly.
Why rigid trays replaced foam and film in the fresh aisle
Foam trays lost favor over environmental rules and shopper perception, while film overwrap alone offers little protection and poor stacking. Rigid APET trays give a stable base, a premium look, and a surface for labels and printed film. They also survive the mechanized fill-and-seal lines used by large retail packers, which demand consistent sheet gauge so the thermoformer can hold cycle time and reject rate low.
2. Why a Dedicated APET Sheet Extrusion Line Beats a Generic Sheet Line
APET is not a forgiving material. It is an amorphous polyester that absorbs moisture from air, softens early, and degrades quickly if processed wet or too hot. A line built for polypropylene or polystyrene usually lacks the crystallizer, the deep drying, and the gentle melt path that APET needs, so it produces brittle, hazy, gel-filled sheet. Designing the extrusion machine around APET from the hopper up is the difference between a tray that sells and a tray that is rejected at the filler.
A dedicated line controls four things a generic line neglects: moisture, melt temperature window, shear history, and gauge uniformity. PET must enter the screw below 30 parts per million water, be melted in a narrow 260 C to 285 C band, be moved with low shear to protect molecular weight, and exit the calendar at a tight thickness tolerance so the thermoformer draws an even wall. Each of these needs a specific unit that a repurposed line simply does not have.
What a generic sheet line gets wrong with APET
Without a crystallizer the amorphous chips clump in the dryer and bridge the hopper. Without a deep desiccant dryer the melt hydrolyzes, dropping impact strength and making the tray crack at the corners. Without a gear pump the screw pulsation shows up as thickness bands that the thermoformer reads as thin spots. Without a proper T-die and calendar the sheet waves and the tray wall varies, causing leaks and weak flanges. The fix is not a tweak; it is a purpose-built APET sheet extrusion machine.
3. APET Material Choices and Co-Extrusion Structures with Cost Analysis
The same extrusion line can make several sheet structures by changing the number of layers and the resins fed. The structure decides the tray function and the material cost per kilogram, so the choice should follow the pack specification rather than habit. The table below lists the common fresh-food structures and a typical converted cost range in US dollars, which already includes resin plus conversion.
| Sheet structure | Typical use | Layer ratio | Converted cost, US dollars per kg |
|---|---|---|---|
| Mono-layer virgin APET | Clear display trays, premium meat and bakery | 100 percent single layer | 1.45 to 1.80 |
| Recycled-core APET, virgin skin | Everyday vegetable and fruit trays, sustainability claim | 15 / 70 / 15 skin-core-skin | 1.05 to 1.35 |
| Barrier APET or EVOH or APET | Red meat modified atmosphere packs with long shelf life | 10 / 5 / 85 / 0 with thin barrier | 1.70 to 2.20 |
| Sealable APET or PE | Lidded vegetable and salad trays with heat-seal film | 80 / 20 with sealing layer | 1.55 to 1.95 |
Mono-layer APET for clear display trays
Mono-layer sheet is the simplest and clearest option. A single screw feeds one resin, the line runs clean, and the tray shows the product with high gloss. The trade-off is cost, because all the material is virgin resin, and there is no barrier, so the pack relies on the lidding film for protection.
Recycled-core APET for lower material cost
By placing recycled PET flake in the core and a thin virgin skin on both faces, the tray keeps a food-contact-safe surface while cutting resin spend. The core can reach 70 percent or more recycled content when the flake is washed, filtered and stabilized. This structure is the workhorse for vegetable and fruit trays where a barrier is not needed.
Barrier APET or EVOH or APET for meat modified atmosphere
Red meat is packed in a low-oxygen atmosphere to keep the myoglobin red and slow bacterial growth. A central ethylene vinyl alcohol layer blocks oxygen far better than PET alone, and the thin APET skins protect the barrier and give a sealable, printable face. The extrusion line needs a feedblock and a second or third extruder to place that layer accurately.
Sealable APET or PE for lidded vegetable packs
Vegetables and salads are often sealed with a peelable film lid. A thin polyolefin layer on the sheet lets the lid film heat-seal at low temperature without distorting the tray. The co-extrusion adds one more resin stream but opens the large lidded-salad segment for the same line.
4. Full APET Sheet Extrusion Line Architecture and Component Price List
A complete APET fresh food tray sheet extrusion machine is a sequence of units from the resin silo to the finished roll. In order, the line is material handling and drying, the extruder with melt conditioning, the co-extrusion feedblock and T-die, the three-roll calendar, cooling and edge handling, gauging, and the winder. Controls tie the units together so gauge, speed and layer ratio stay locked during a long production run.
| Line component | Specification for a 1000 mm tray sheet line | Price, US dollars |
|---|---|---|
| Crystallizer and dehumidifying dryer | 500 to 800 kg per hour, minus 40 C dew point | 28,000 to 55,000 |
| Single-screw sheet extruder | 120 to 150 mm, 33 to 35 L/D, barrier screw | 120,000 to 260,000 |
| Melt gear pump | Matched to 600 to 1400 kg per hour | 25,000 to 60,000 |
| Continuous screen changer | Double-bolt, 20 to 100 micron screen | 18,000 to 40,000 |
| Co-extrusion feedblock | 2 to 3 layer, adjustable ratio | 30,000 to 70,000 |
| Coat-hanger T-die | 1000 mm wide, flex lip, heated | 45,000 to 120,000 |
| Three-roll polishing calendar | Polished chrome rolls, gap control | 60,000 to 140,000 |
| Edge-trim recycler and winder | Online grinder plus automatic winder | 52,000 to 115,000 |
| Scanning thickness gauge and controls | IR or beta scan, PLC line control | 45,000 to 95,000 |
Material handling and drying
Resin arrives in bulk bags or silos and is conveyed to the crystallizer, then to the dehumidifying dryer that feeds the extruder throat. This front end is where APET quality is won or lost, because the melt cannot recover from wet resin once it has hydrolyzed in the barrel.
Extrusion and melt conditioning
The extruder plasticates the resin, the screen changer removes contamination, the gear pump stabilizes flow, and the static mixer evens temperature before the melt reaches the die. Conditioning the melt here protects clarity and molecular weight and sets the stage for a flat sheet.
Die, calendar and forming
The feedblock splits and recombines layers, the T-die lays a uniform curtain, and the three-roll calendar fixes the thickness and surface. Roll temperature and gap are the last chance to control gloss, flatness and gauge before the sheet cools.
Downstream, gauging and winding
After the calendar the sheet is trimmed, measured across the width, and wound into rolls of consistent tension and diameter. Edge trim returns to the hopper through the recycler, so almost nothing is wasted.
Controls and line integration
A single controller manages temperatures, pump speed, roll gap, line speed and layer ratio, and logs the run. Good integration means a change from mono to barrier sheet is a recipe load rather than a rebuild, which matters when a packer runs several tray programs on one line.
5. Crystallizer and Dehumidifying Dryer: Controlling PET Moisture with Cost
Drying is the single most important preparation step for APET sheet, and it is also the step most often skipped on a repurposed line. Amorphous PET chips hold surface and bound moisture, and they soften and clump below the temperature where ordinary dryers operate, so they must first be crystallized into a form that can sit in hot air without fusing.
Why PET chips must be crystallized first
Virgin amorphous PET has a glass transition near 70 C to 80 C, so in a hot dryer it sticks together and blocks the hopper. A crystallizer heats the chips to about 160 C to 180 C for one to two hours so the polymer rearranges into a more ordered, higher-temperature form. After that the same material can be dried at 120 C to 140 C without agglomerating, which is impossible before crystallization.
Drying setpoints and residence time
The goal is a moisture content below 30 parts per million, with below 50 parts per million acceptable for many tray grades. That needs a desiccant dryer delivering air at a minus 40 C dew point, a residence of four to six hours, and a steady feed so the extruder throat never sees a wet slug. A dew-point sensor and a hopper level controller keep the setpoint honest during long runs.
Cost of crystallizer and dehumidifying dryer
A crystallizer and dehumidifying dryer sized for 500 to 800 kg per hour of APET typically costs 28,000 to 55,000 US dollars, depending on automation, silo integration and energy recovery. This is a small share of the total line yet it protects the entire output, because wet resin ruins every kilogram that follows it.
6. Single-Screw Sheet Extruder: Screw, Drive, Venting and Cost
The extruder is the heart of the APET sheet extrusion machine. For fresh food tray sheet a single-screw design with a barrier section and a long enough L/D to melt gently is the common choice, with a twin-screw option when recycled content is high enough to need compounding and intense degassing inside the same train.
Barrier screw geometry
A barrier screw keeps solid and melt in separate channels so the resin is fully plasticated with low shear and a short residence at peak temperature. For APET that protects intrinsic viscosity and limits acetaldehyde formation, both of which matter for taste-free, strong tray sheet. Typical diameters are 120 mm to 150 mm with a 33 to 35 L/D ratio for a 1000 mm tray line.
Venting and devolatilization
APET releases trace moisture and volatiles even after drying, so the barrel carries an atmospheric vent and a vacuum vent. The vacuum stage pulls out the last water and low-boiling compounds before the melt reaches the pump, which keeps gels and haze down and supports food-contact quality. A properly vented barrel is why a dedicated line beats a closed non-venting screw.
Drive, motor and torque
Tray sheet needs steady torque rather than peak speed. A line making 600 to 1400 kg per hour of APET draws a drive in the 200 kW to 450 kW range, fed by a vector or servo motor through a hardened gearbox. The control holds screw speed against load swings when a layer ratio changes, so gauge stays flat.
Single-screw versus twin-screw for recycled content
With mostly virgin resin a single screw is enough. When the core is high-percentage recycled flake, a twin-screw unit can be added to compound, strip volatiles and lift molecular weight before the sheet die, which widens the recycled window without losing tray properties. Wanplas supplies both single-screw sheet extruders and twin-screw compounding extruders so the line can grow with the recycled-content target.
7. Melt Gear Pump, Screen Changer, Static Mixer and Feedblock with Cost
Between the extruder and the die sits the melt conditioning package that turns a pulsating screw output into a flat, clean, layered sheet. It is made of a gear pump, a screen changer, a static mixer and, for multi-layer, a co-extrusion feedblock. Each piece earns its place by protecting gauge, purity or layer placement.
Melt gear pump for stable gauge
The gear pump takes the fluctuating pressure from the screw and delivers a near-constant volumetric flow to the die. That steadies thickness across the roll and lets the die run at lower pressure, which lowers shear heating and protects intrinsic viscosity. A pump matched to 600 to 1400 kg per hour costs about 25,000 to 60,000 US dollars.
Continuous screen changer
A double-bolt continuous screen changer swaps the filter screen without stopping the line, catching gel, carbon and foreign particles that would otherwise mark the sheet. For tray sheet a 20 to 100 micron screen is common, and the unit runs from 18,000 to 40,000 US dollars depending on width and actuation.
Static mixer for layer uniformity
A fixed-element static mixer evens temperature and layer distribution with no moving parts, removing the hot and cold streaks that show up later as gloss variation. It is a modest item at 6,000 to 14,000 US dollars yet it is central to a uniform clear sheet.
Co-extrusion feedblock for multi-layer
The feedblock splits the main melt and injects the skin or barrier streams, then recombines them into the layered curtain the die expects. A 2 to 3 layer feedblock with adjustable ratio costs 30,000 to 70,000 US dollars and is what lets one line make mono, recycled-core and barrier sheet by recipe rather than rebuild.
8. Coat-Hanger T-Die and Three-Roll Polishing Calendar with Cost
The die and calendar decide the final sheet thickness, flatness, gloss and surface. For fresh food tray sheet these two units must hold a tight window because the thermoformer reads sheet gauge directly into tray wall thickness, and any variation becomes a weak flange or a leak.
Coat-hanger T-die design
A coat-hanger T-die distributes melt from the center feed out to both edges through a tapering channel so pressure is equal across the width. The die body is heated and insulated, with a choker bar that fine-tunes the cross profile. For a 1000 mm tray line the die runs about 45,000 to 120,000 US dollars, more for wider or multilayer versions.
Flex-lip die adjustment
A flex-lip die uses bolts or thermal elements along the lip to bow the exit locally, correcting thin or thick bands without stopping the line. This is the tool that turns a good profile into a flat one, and it is worth specifying on any line aimed at tight tray tolerance.
Three-roll polishing calendar
The calendar pulls the molten curtain between three polished chrome rolls that set thickness and imprint a high-gloss or matte face. Roll gap, speed and temperature are controlled independently, and the middle roll often sets the sheet path. A three-roll polishing stack for tray sheet costs 60,000 to 140,000 US dollars and determines whether the tray looks premium on the shelf.
9. Cooling, Edge-Trim Recycling, Thickness Gauging and Winding with Cost
After the calendar the sheet is solid but still warm, and the next units fix its dimension, measure it, and package it into rolls the thermoformer can load. This section is where scrap is captured and where the line proves its consistency to the packer.
Cooling and edge trimming
A cooling rack or additional roll stand removes residual heat, then trim knives cut both edges to a clean width. Edge trim is not waste; it is the same virgin-grade material and is routed straight back into the process through the recycler, closing the loop on the line.
Online edge-trim recycling
An inline grinder drops the trim back into a side hopper that meters it into the extruder or the core layer. For recycled-core structures this same path handles post-industrial offcut, cutting material cost with no separate step. The grinder and feed package runs 12,000 to 25,000 US dollars.
Scanning thickness gauge
A scanning gauge rides across the sheet measuring thickness by infrared or beta absorption and feeds the number back to the die and rolls. It flags drift before the thermoformer sees it, and it builds the thickness record a food packer expects from a qualified supplier. Expect 20,000 to 45,000 US dollars for the sensor and scanner.
Automatic winding and roll handling
An automatic winder builds rolls at constant tension, changes rolls without stopping, and stages them for the thermoformer or warehouse. For thicker sheet a stacker may replace the winder. The winder plus trim recycler package is 52,000 to 115,000 US dollars, and it is the unit that decides daily output and roll quality.
10. Process Parameters and Process Control
Running APET tray sheet is a balance of dry feed, tight melt temperature, controlled roll temperature and locked line speed. The table below gives a working window for a virgin or recycled-core APET line; exact numbers shift with width, thickness and layer count, but the relationships hold.
| Parameter | Typical range | Why it matters |
|---|---|---|
| Resin moisture before screw | Below 30 parts per million | Prevents hydrolysis and brittle tray |
| Melt temperature | 260 C to 280 C | Keeps viscosity and limits acetaldehyde |
| Die temperature | 265 C to 280 C | Sets flow and edge stability |
| Calendar roll temperature | 40 C to 90 C by layer | Controls gloss, flatness and release |
| Line speed | 20 to 45 meters per minute | Sets throughput with thickness |
Drying and gravimetric feeding
Each layer is fed by weight, not volume, so the layer ratio holds whether the run is mono or barrier. Gravimetric dosing also tracks resin use per roll, which the cost model needs for a true per-kilogram figure.
Melt and die temperature profile
The barrel warms gradually to the melt setpoint and the die sits a few degrees above it. Staying under about 290 C protects intrinsic viscosity and keeps acetaldehyde low, while dropping below the window risks unmelt and gels. The controller ramps and holds this profile through start-up and grade change.
Roll temperature and line speed
The top roll often runs cooler to set the show face, the middle roll carries the path, and the bottom roll finishes. Speed is tied to thickness by the mass balance, so the operator picks a target thickness and the line finds the matching speed for the chosen width.
Layer ratio control
For recycled-core or barrier sheet the feedblock ratio is locked by the gravimetric feeders and checked by the gauge and, where needed, an online layer sensor. A stable ratio is what lets a packer claim a recycled content percentage with confidence.
11. Quality Control and Food-Contact Compliance for Tray Sheet
Tray sheet touches food, so quality control covers both the physical sheet and the legal basis for contact. A disciplined line measures gauge, optics, molecular properties and migration, and keeps records that a retail packer or auditor can read.
| Property | Target for tray sheet | How it is checked |
|---|---|---|
| Thickness variation | Within 3 to 5 percent | Scanning gauge across width |
| Haze | Below 2 to 3 percent | Haze meter on sample |
| Gels and black specks | Few per square meter | Visual count and screen record |
| Intrinsic viscosity drop | Less than 0.02 to 0.03 dl per g | Capillary viscometer |
| Acetaldehyde | Below 1 to 3 parts per million | Headspace gas analysis |
Gauge uniformity
The thermoformer needs even sheet so every tray wall is the same. The scanning gauge records variation across width and length, and the die flex lip and roll gap are adjusted until the band sits inside the 3 to 5 percent target. Out-of-band rolls are diverted rather than shipped.
Optical clarity and gel count
Retail trays are judged by eye, so haze stays low and gels are counted per square meter. Good drying, a fine screen and a clean melt path keep both in range; a spike points straight back to moisture, contamination or a worn screen.
Intrinsic viscosity and acetaldehyde
Intrinsic viscosity tracks molecular weight and therefore tray toughness; a drop below the target means the melt was too hot or too wet. Acetaldehyde is a taste and odor compound that rises with thermal load, so the line is tuned to the lowest temperature that still melts the resin cleanly.
Food-contact compliance
APET tray sheet is regulated for direct food contact under rules such as the United States food contact resin specification and the European framework for plastic food contact materials. The sheet must show low overall migration, no heavy metal release, and a documented formulation. Wanplas supplies material and process documentation so the packer can file the needed declarations.
Recycled-content certification
When recycled flake enters the core, the supply must be from a supervised chain with washing and filtration, and the output should meet the applicable recycled plastic food-contact position. The line supports this with filtration, inline measurement and batch records that tie each roll to its resin lot.
12. Capacity, Plant Utilities, Layout, Investment and Wanplas Equipment
Sizing the line means matching width and thickness to the packer’s tray volume, then costing the space, power and people around it. A well-matched APET tray sheet extrusion machine runs steadily for years, so the capacity decision drives both the investment and the per-kilogram cost that sets the payback.
Throughput by width and thickness
Output follows a simple mass balance: width times thickness times density times line speed. A 1000 mm line making 0.5 mm sheet at 30 meters per minute yields roughly 670 kg per hour of APET, and a thicker or faster set can reach 1000 to 1400 kg per hour. Running 6000 hours a year that is about 4,000,000 to 8,400,000 kg of sheet, enough for a large tray program.
Utilities: power, water and compressed air
The line draws about 350 kW to 650 kW depending on width and whether a twin-screw recycler is attached. Cooling water demand is around 20 to 40 cubic meters per hour for the calendar, chiller and compressor, and the plant needs steady compressed air for actuators and the winder. Budgeting these up front avoids an under-sized service that caps output.
Plant layout and labor
A tray sheet line needs roughly 25 m to 40 m of length and 600 m2 to 1200 m2 of floor space including resin storage, drying, the extrusion hall and roll warehouse. Crew is typically two to four operators per shift plus quality and maintenance cover, which feeds the per-kilogram labor cost.
Per-kilogram conversion cost
Beyond resin, conversion cost is energy of about 0.08 to 0.14 US dollars per kg, labor of 0.02 to 0.04 US dollars per kg, overhead of 0.03 to 0.06 US dollars per kg, and depreciation of 0.05 to 0.12 US dollars per kg on a mid-size line. With virgin APET resin near 1.30 to 1.60 US dollars per kg, the converted mono sheet lands near the 1.45 to 1.80 US dollars per kg shown earlier, while a recycled-core structure cuts the resin line and lowers the total.
Payback example
A 1000 mm line with a total installed cost near 600,000 to 900,000 US dollars, running 6000 hours a year at 800 kg per hour, makes about 4,800,000 kg annually. If the converted sheet carries a margin of 0.10 to 0.25 US dollars per kg over resin plus conversion, the annual contribution is roughly 480,000 to 1,200,000 US dollars, giving payback in about one to three years before counting the saved edge trim and the option to sell barrier grades at a premium.
Wanplas equipment families for this line
Wanplas supplies the full tray sheet program from one platform: the crystallizing dryer and dehumidifying dryer, the single-screw sheet extruder and optional twin-screw compounding extruder, the melt gear pump, continuous screen changer, static mixer and co-extrusion feedblock, the coat-hanger T-die and three-roll polishing calendar, the edge-trim recycler and automatic winder, and the scanning thickness gauge with integrated line controls. Wanplas also supplies the downstream thermoforming machine that forms the trays, the PET recycling line that prepares flake for the core, and the bottle blow molding and filling machines for the wider fresh packaging line, so a packer can obtain the whole chain under one brand.
Service and support commitments
The Wanplas brand backs its machinery with a 72-hour continuous running test before shipment, on-site installation and commissioning, operator training, remote support, and a policy of 500 US dollars in free spare parts every year with free replacement of damaged parts inside the warranty period. The group factory is open for customer visits and sample trial runs, so a buyer can validate tray sheet on the actual line before committing to volume.
13. Common Questions About APET Tray Sheet Lines
Can one line make both mono and barrier APET sheet?
Yes. With a co-extrusion feedblock and a second or third extruder the same line switches from mono to recycled-core to barrier sheet by loading a recipe, without a mechanical rebuild. The die and calendar stay the same; only the layer streams and ratios change.
How dry must the PET be before extrusion?
Target below 30 parts per million moisture, with below 50 parts per million acceptable for many tray grades. That requires a crystallizer followed by a desiccant dryer at a minus 40 C dew point and four to six hours of residence.
What sheet thickness works for fresh food trays?
Most thermoformed trays use 0.2 mm to 1.2 mm sheet, with the thin end for light vegetable trays and the thick end for deep meat or poultry trays. The line sets this at the calendar gap and holds it with the gauge loop.
Can I use recycled PET in the sheet?
Yes, in the core layer, often 70 percent or more, provided the flake is washed, filtered and stabilized. A twin-screw recycler helps when recycled content is high, and batch records support the recycled-content claim.
Why is a melt gear pump necessary?
The pump smooths the screw pulsation into steady flow, which tightens thickness tolerance and lets the die run at lower pressure with less shear. That protects gauge and intrinsic viscosity at the same time.
How does the line support red meat modified atmosphere packs?
By adding a thin ethylene vinyl alcohol barrier layer through the feedblock, the sheet slows oxygen entry and helps the pack keep the meat red and safe. The same line can drop the barrier for vegetable trays that do not need it.
What is the energy use of a tray sheet line?
A 1000 mm line draws about 350 kW to 650 kW, plus cooling water of 20 to 40 cubic meters per hour. Energy is a major part of conversion cost, roughly 0.08 to 0.14 US dollars per kg, so drive and dryer efficiency matter to margin.
How much floor space does the line need?
Plan for 25 m to 40 m of line length and 600 m2 to 1200 m2 including storage, drying, extrusion and roll warehouse. A wider or twin-screw line sits at the upper end of that range.
What lead time and commissioning should I expect?
Wanplas runs a 72-hour continuous test before shipment and provides on-site installation, commissioning and training. Lead time depends on width and layer count, and a sample trial run can be arranged at the factory before volume orders.
How do I start a tray sheet project?
Send the target tray size, structure, annual volume and any barrier or recycled-content requirement. Wanplas returns a line configuration, a per-kilogram cost estimate in US dollars, and an invitation to validate the sheet on a running line at the factory.
14. Conclusion and Next Steps
A dedicated APET fresh food tray sheet extrusion machine is the foundation of every clear or barrier tray in the supermarket fresh aisle. By crystallizing and deep-drying the PET, melting it gently in a barrier screw, conditioning the melt with a gear pump and screen changer, laying it through a flex-lip T-die onto a three-roll calendar, and closing the loop with edge-trim recycling and scanning gauging, the line delivers uniform, clean, food-contact sheet that the thermoformer can trust.
The investment is real but contained: a mid-size 1000 mm line with drying, extrusion, co-extrusion, calendar and winding typically totals 600,000 to 900,000 US dollars installed, with conversion cost of roughly 0.18 to 0.36 US dollars per kg on top of resin, and payback in about one to three years at volume. Structures from mono virgin to recycled-core to barrier APET or EVOH or APET let one line serve meat, vegetable, salad and deli programs.
Wanplas supplies the complete tray sheet platform and the surrounding machines, from the crystallizing dryer and single-screw sheet extruder through the co-extrusion feedblock, T-die and polishing calendar to the edge-trim recycler, winder and thickness gauge, plus the downstream thermoforming machine, PET recycling line and bottle and filling equipment for the full fresh packaging chain. Backed by a 72-hour pre-shipment test, installation and training, 500 US dollars of free spare parts each year, and an open factory for trial runs, the Wanplas brand gives a packer a single accountable partner for the whole program.
To move from plan to production, share your tray dimensions, target structure, annual volume and any barrier or recycled-content goal. Wanplas will return a matched line configuration, a per-kilogram cost in US dollars, and an invitation to run your sheet on a live line before you commit to volume.

