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Engineering Plastic

Engineering plastic compounding is a main application of the twin screw extruder. These polymers are sensitive to overheating and hydrolytic degradation, so we build for high torque and high speed: more output with less residence time, better dispersion and accurate temperature control. From short glass fibre to long-fibre thermoplastics.

  • Short fibre
  • LFT-G
  • UD tape
  • Direct LFT
Glass fibre length in short-fibre pellets
0.2–0.3mm
LFT-G pellets, fibre as long as the pellet
6–16mm
Modulus and impact of LFT-G vs. short-fibre compounds
2× · 4×
U6 line in Germany, up to 50% glass fibre and powder
~800kg/h

Materials and applications

The basic formula: a general or advanced engineering plastic, reinforced and modified with fibres and additives.

General engineering plastics

  • PA6
  • PA66
  • PA46
  • PPA
  • ABS
  • POM-C
  • POM-H
  • PET
  • PC
  • PBT
  • PE-(U)HMW

Advanced engineering plastics

  • PBI
  • PAI
  • PEEK
  • PPS
  • PEI
  • PSU
  • PVDF

Additives

  • Glass fibre
  • Carbon fibre
  • Flame retardant
  • UV stabiliser
  • Anti-oxidant
  • Anti-static
  • Colour pigment
Automotive

Intake manifolds, header tanks, filters, fans and shrouds, engine covers

Electrical

Terminal blocks, cable ties, connectors, power tools, MCCB, relays, lights

Film & pipe

BOPA, BOPET, PET sheet, pipe

Fibre

PA fibre, PSF, FDY

Other industrial

Construction, housewares, furniture, toys

Processing of engineering plastic

Ask for a configuration →

High torque, short residence time

Engineering plastic is sensitive to overheating and hydrolytic degradation. Our SAT-X series extruder, with 13 Nm/cm³ specific torque and 800 rpm screw speed, reaches higher output with less residence time, better dispersion and more accurate temperature control.

EquipmentU+ Series Twin Screw ExtruderOur high-torque platform for PEEK, PPSU and glass-fibre compounds.
ModelDiameter (mm)Max. Speed (rpm)Motor (kW)L/DOutput (kg/h)
SAT-X5251.480016040–44450–700
SAT-X6562.480028040–44750–1200
SAT-X7571.460035540–44850–1500

Output depends on polymer, fibre content and pelletizing.

Cartridge heaters inside the barrel of the SAT twin screw extruder

Heating inside the barrel

Cartridge heaters made in Germany sit inside the barrel instead of cast heaters outside. The polymer melts mostly by heat, not by kneading, so screw and barrel last longer and the compound is better.

Saves energy
Cooling channels with two inlets and outlets on each barrel

Two-way barrel cooling

Two inlets and outlets on each barrel give more uniform and faster cooling.

Temperature control
Barrel supported at its centre line on the SAT supporting frame

Supported at the centre

A barrel supported underneath expands upward by 0.2–0.5 mm when heated, leaving uneven gaps. Ours is supported in the middle, so it expands evenly up and down and the gaps stay even.

Even screw clearance
Under water strand pelletizing system

Under water strand pelletizing

Water flow carries the strands into the pelletizer, even when they break during a filter change: almost no waste. Above about 25 strands (around 800 kg/h), hot strands are hard to handle by hand.

> 800 kg/h

Four ways to reinforce with fibre

The longer the fibre stays in the part, the higher the mechanical properties. Each route keeps a different fibre length.

0.1 mm1 mm10 mm100 mm1 mcontinuous →Fibre length in the product · log scale Short fibre0.2–0.3 mm 4 mm pellet LFT-G6–16 mm Direct LFTno intermediate pellet UD tapecontinuous rovings
  1. 01 · Compounding

    Short fibre reinforced

    Roving or chopped glass fibre goes straight into the twin screw extruder and is compounded with the polymer.

    Fibre in
    Roving, or chopped 4–6 mm
    Entry
    5th barrel
    Product
    4 mm pellets
    Fibre in pellet
    0.2–0.3 mm
  2. 02 · Indirect LFT

    LFT-G

    Rovings pass through an impregnation die and are coated by PP melt from the twin screw extruder. The pellets go to any injection moulding machine.

    Fibre in
    Glass rovings
    Product
    6–16 mm pellets
    vs. short fibre
    2× modulus · 4× impact
    Low temperature
    Keeps function at −30 °C
  3. 03 · Tape

    UD tape

    Glass or carbon rovings enter a T-die and are coated by PE / PP / PET / PA melt. For building wall panels and truck and trailer bodies.

    Fibre
    50–60%
    Width
    610 or 1,220 mm
    Thickness
    0.25–0.35 ±0.02 mm
    Line speed
    6–12 m/min
  4. 04 · Direct LFT

    LFT-D-IMC / LFT-D-ECM

    Fibre and matrix are combined right before the moulder, with no intermediate product and a single heat history.

    D-IMC
    Attached to an injection machine
    D-ECM
    Two extruders + hydraulic press
    Additions
    Fillers, flame retardants, additives

Short-fibre and long-fibre lines in detail

01 · Short fibre

Two ways to feed the glass

Roving and chopped fibre both enter at the fifth barrel, after the polymer has melted.

Roving

  • 20 rovings on a support frame with a Mettler Toledo weighing transducer.
  • The fibres enter the venting port on the fifth barrel and are drawn in by the twin screws.
  • A weight controller shows the feed rate; adjust it by screw speed or number of rovings.

Chopped · 4–6 mm

  • Fed into the fifth barrel by a two-stage side feeder.
  • Top stage: loss-in-weight feeder with output control.
  • Bottom stage: fixed-speed force feeding.
02 · LFT methods

Three processing methods for LFT parts

LFT parts are typically made by one of three methods: indirect (LFT-G pellets for injection moulding), direct injection moulding compounding (LFT-D-IMC), or extruder compression moulding (LFT-D-ECM).

  • D-ECM advantage 1Compounding and fibre mixing are separated, so each extruder is optimised for its own job.
  • D-ECM advantage 2The material sees less stress than in injection moulding, which keeps the fibre long: critical for automotive parts.
LFT manufacturing technologies: indirect LFT-G, direct LFT-D-IMC and LFT-D-ECM
Figure 1 · LFT manufacturing technologies.
Flow chart of the LFT-G line
LFT-G line
Flow chart of the LFT-D-ECM line
LFT-D-ECM line
03 · UD tape

Thermoplastic UD tape extrusion line

SAT40 or SAT52 twin screw extruder. For PP base sheet a single screw extruder is fine; for PA or PET base it should be a twin screw.

  1. Fibre creel
  2. Traction unit
  3. Gravimetric batch mixer
  4. LIW feeder
  5. Twin screw extruder
  6. Melt filter
  7. Impregnation die
  8. Pressure calibrating
  9. Cooling stack & edge cutting
  10. Winder
Layout drawing of the UD tape extrusion line
Line layout, side and top view.
Videos

See the lines running

Glass-fibre compounding, LFT-G on three extruder sizes, LFT-D-ECM and a continuous-fibre tape line.

Project · Germany

Up to 50% glass fibre and powder at ~800 kg/h

A German compounder of PBT, PA and PP needed a line for high glass-fibre and mineral loadings, CE-compliant and linked to its SAP system.

Extruder
U6-48
Drive
Siemens 280 kW
Gearbox
Zambello · 900 rpm
Pelletizing
Under water strand
  1. Base resin 12–90%, inorganic powder 10–50%, glass fibre 10–50%, additives 1–5%.

  2. Wear-resistant alloy barrel liners and screw elements in the working section.

  3. A single-stage side feeder downstream lets the fibre join after the resin has melted.

  4. Stable pelletizing at around 800 kg/h on site.

Engineering plastic reinforcing compounding line in Germany.

Get a quote

Tell us the polymer, the fibre or filler and its content, and how the compound will be moulded. Short-fibre pellets, LFT-G pellets, UD tape and direct LFT need different lines; we start from the part and the fibre length it needs.

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  1. 01Polymer, fibre & additives
  2. 02Route: pellets, tape or direct LFT
  3. 03Extruder, feeding & pelletizing
Souder Chen

Souder Chen

Head of Compounding Division

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

Engineering Plastic

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