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Sheet Extrusion

Sheet direct extrusion is what USEON is known for in sheet and film: polymer, filler and additives are fed, mixed and devolatilized in one twin screw extruder and leave the die as finished sheet, without pelletizing or pre-drying in between. Single screw sheet and board lines complete the range.

  • Packaging sheet
  • Technical sheet & board
  • Film
Melt leaving a sheet die onto the polished roller of a calender
Sheet
ABS / HIPS / PMMA board production line
Board
Winder of a PVB film extrusion line
Film

The lines side by side

Thickness tells the lines apart: from 12 μm stretched film to 8 mm board.

Packaging sheetTechnical sheet & boardFilm

Logarithmic scale. Ranges as stated on each line page.

LinePolymersSheet widthOutputExtruderLeaves the line as
Packaging sheet
PET sheetPET, APET, RPET, CPET, PETG600–3,000 mm500–2,000 kg/hSAT twin screwRolls
PP / PS / PLA / PBAT / PHA sheetPP, PS, HIPS, PLA, PBAT, PHA600–3,000 mm350–1,500 kg/hSAT twin or TDD single screwRolls
Barrier sheetPP, PE, PS, EVA, EVOH600–900 mm200–600 kg/hSingle screwRolls
Technical sheet & board
ABS sheetABS600–1,200 mm—Single screwRolls
ABS / HIPS / PMMA boardABS, PS, HIPS, PMMA1,200–2,100 mm550–750 kg/hThree single screwsBoards cut to length, stacked
WPC sheetPP with 40% wood fiber1,400–1,600 mmup to 600 kg/hSAT twin screwSheets, stacked
Film
PVB / SGP filmPVB, SGPup to 4,000 mm300–600 kg/hSAT twin screwRolls
POE / EVA solar filmNew EnergyEVA, POE1,250 / 2,500 mm300–500 kg/hTwin screwRolls
BOPET filmPET7,500 mm5,000 kg/hSAT twin screwMelt for the stretching line

Why direct extrusion

The traditional way to make sheet or film depends on the formula. For two of the three kinds of formula it takes a step before the sheet extruder.

FormulaTraditional processDirect extrusion
Simple formulationSuch as PE with a small added quantity of masterbatch or additivesPremix all componentsSingle screw extruderSheet or filmOne stepGravimetric feedingTwin screw extruderSheet or filmOne step. Less energy, better dispersion and less waste at a colour change than the single screw.
Complex formulationSuch as PP with 40% filler or wood fiberCompounding in a twin screw extruderPelletizingPremixSingle screw extruderSheet or filmTwo stepsSplit feedingTwin screw extruderSheet or filmOne step. The polymer is melted once; the recipe is changed at the feeders.
Water-sensitive materialSuch as PET or PAPre-drying, 3–5 hoursSingle screw extruderSheet or filmTwo stepsUndried materialTwin screw extruder with vacuumSheet or filmOne step. No crystallizer and no dryer.

What the traditional process costs

More energy

For pre-drying, for the two-stage process, or for the single screw extruder itself.

More manpower

And more factory space and investment.

Poorer dispersion

For additives and for polymers of different MFI.

Overheating and shearing

Of natural wood fiber.

Over-shearing of glass fiber

In the D-LFT process.

Polymer degradation

In the two-step process.

Twin screw against single screw, in numbers

Up to 30%

Energy saved. Stated for the HDPE sheet line and the BOPP film line, against single screw extrusion.

5,500 kg/h

From the same 1,200 kW motor. BOPP film: a single screw extruder reaches 4,200 kg/h at most.

One instead of two

One twin screw extruder replaces two single screw extruders, which the traditional BOPP line connects in series.

3–5 hours

Of pre-drying no longer needed. PET and PA are extruded undried.

Lower additive percentage

Better dispersion performance leads to a lower percentage of additives.

Less colour-change waste

Due to the self-cleaning effect of the twin screw.

Less polymer degradation

Less residence time in the extruder.

Six formulas we have run

Each one is a delivered direct extrusion line: the formula, the sheet it makes, and what the line had to solve.

01 · Packaging sheet

PP with talc

Sheet for thermoformed food packaging. COPP compounded with 40% talc and 2% colour masterbatch.

  • Vacuum loading and split feeding keep dust off the finished sheet. PP and masterbatch enter the first barrel; talc is fed separately through two side force feeders.
  • No lubricant, because the sheet packs hot food. Above 600 kg/h friction raises the melt temperature, so a special cooler and screw design bring it down before the T-die.
  • The sheet can run straight into the thermoforming line, bypassing the winder: no preheating before forming.

SolutionPP / PS / PLA / PBAT / PHA sheet line Project900 kg/hUSA

Width
850 mm
Thickness
0.6–1.0 mm
Line speed
10–17 m/min
Max. output
900 kg/h

02 · Technical sheet

PP with wood fiber

Protection layer of wall and ceiling panels. PP compounded with 40% wood fiber, colour masterbatch and additives.

  • PP melts above 190 °C, so the wood fiber, premixed with the additives, enters through a side force feeder after the PP has melted.
  • The screw design mixes without over-shearing, so the fiber keeps its length.
  • Wood fiber flows poorly: a special gear pump and an inner lubricant carry the melt to the die. Both sides are coated with non-woven fabric.

SolutionWPC production line Project600 kg/hLatvia

Width
1,400–1,600 mm
Thickness
0.8–1.5 mm
Line speed
4–10 m/min
Max. output
600 kg/h

03 · Technical sheet

HDPE waterproof sheet

Floor moisture barrier and roofing underlayment. HDPE compounded with colour masterbatch and additives.

  • Vacuum loading, gravimetric feeding, then the twin screw extruder for sheet extrusion.
  • Against a single screw extruder: energy saving up to 30%, better dispersion, less waste when the colour changes.

Project800 kg/h HDPE sheet line

Width
1,200 ± 2 mm
Thickness
0.65–1.40 ± 0.05 mm
Line speed
8–17 m/min
Max. output
800 kg/h

04 · Film

BOPP / BOPA film

Packaging film, structure A/B/A. PP compounded with additives: anti-slip, anti-static, anti-oxidant.

  • The traditional line connects two single screw extruders in series to reach the output. One twin screw extruder replaces both.
  • Better degassing, and better dispersion with a lower percentage of additives.

Project5,500 kg/h BOPP film line

SAT-X150 · 1,200 kW
5,000–6,000 kg/h
SAT-X175 · 2,000 kW
7,000–10,000 kg/h

05 · Film

EVA film

Solar cell encapsulation. EVA with a VA content ≤ 33, additives in liquid or powder form.

  • EVA and the premixed additives enter the first barrel by loss-in-weight feeder; liquid additives are fed into the 4th barrel.
  • The screw design mixes well and avoids over-shearing.
  • A hot calibration system keeps the shrinking rate below 3%. The automatic winder controls tension from 10 to 100 N.

SolutionPOE / EVA solar film line Project500 kg/h EVA film line

Width
2,300 mm
Thickness
0.2–0.9 ± 0.02 mm
Line speed
> 6 m/min
Max. output
500 kg/h

06 · Film

PVB / SGP film

Laminated glass for automotive and building. PVB or SGP, additives, and the on-line waste material of the line.

  • A cooling jacket on the feeding system keeps the sticky raw material from choking the inlet.
  • Co-extrusion for a second colour on the edge of the film.
  • Automatic T-die, interlocked with the thickness tester.

SolutionPVB / SGP film line Project500 kg/h PVB film line

Width
up to 4,000 mm
Thickness
0.3–1.5 mm
Output
300–600 kg/h

Get a quote

Tell us the sheet, board or film you sell and the formula behind it. We tell you whether it runs as direct extrusion, and quote the complete line.

  1. 01Polymer and formula: fillers, fibers or additives and their percentage
  2. 02Product: thickness, width, layer structure, output per hour
  3. 03Extruder type, line configuration and quotation
Souder Chen

Souder Chen

Head of Compounding Division

With USEON since 2008. Twin screw compounding, devolatilization and recycling lines.

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Sheet Extrusion

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