| Single-Screw Extruder |
PE, PP, PVC, PS, ABS, PLA and other relatively uniform thermoplastics |
Pipe, profile, film, sheet, wire coating, pelletizing and basic compounding |
Approximately 5–1,500 kg/h, depending on screw diameter, material and die |
Usually 150–260°C; PVC and heat-sensitive materials require controlled profiles |
Simple design, lower capital cost, easy operation and good continuous conveying |
Limited mixing, feeding and devolatilization capability compared with twin-screw systems |
| Co-Rotating Twin-Screw Extruder |
Filled polymers, recycled materials, color concentrates, engineering plastics and reactive formulations |
Compounding, masterbatch production, reactive extrusion, devolatilization and pelletizing |
Approximately 10–10,000 kg/h, depending on machine size and formulation |
Commonly 180–350°C; engineering polymers may require higher controlled zones |
Excellent distributive and dispersive mixing, flexible feeding and strong process control |
Higher equipment cost, greater energy demand and more complex screw configuration |
| Counter-Rotating Twin-Screw Extruder |
Rigid PVC, wood-plastic compounds and formulations needing gentle, controlled conveying |
Rigid pipe, window profile, siding, technical profile and selected sheet applications |
Approximately 20–1,200 kg/h, depending on screw diameter and product geometry |
Typically 160–210°C for PVC-based processing; exact settings depend on formulation |
Stable conveying, high filling capability and relatively low shear for heat-sensitive PVC |
Less suitable for intensive dispersive mixing and broad formulation changes |
| Two-Stage or Tandem Extruder |
Materials requiring separate melting and homogenizing stages, including recycled blends |
Recycling, film production, sheet extrusion, degassing and temperature-sensitive processing |
Approximately 100–3,000 kg/h, depending on configuration and material preparation |
Usually 160–300°C, with separate control of melting and cooling sections |
Improved temperature management, lower melt stress and enhanced degassing potential |
Larger footprint, higher installation cost and more complicated synchronization |
| Ram Extruder |
Ultra-high-viscosity materials, paste-like compounds, PTFE and selected specialty formulations |
Specialty profiles, preforming and processes where conventional screw conveying is unsuitable |
Usually batch or low-throughput; commonly below 100 kg/h |
Material-specific; PTFE processing is generally performed below its melting point |
Can process materials that do not flow readily through conventional screw extruders |
Lower continuous productivity and limited suitability for general thermoplastic production |
| Sheet and Film Extrusion Line |
PE, PP, PET, PS, PLA, TPU and multilayer barrier structures |
Cast film, blown film, flat sheet, multilayer film and thermoforming sheet |
Approximately 20–2,500 kg/h, depending on width, thickness and layer count |
Commonly 160–320°C; PET and some engineering polymers require drying before extrusion |
Designed for precise thickness control, web handling and high surface quality |
Requires downstream equipment such as chill rolls, air rings, haul-off and winding systems |
| Profile and Pipe Extrusion Line |
PVC, PE, PP, ABS, TPU, TPE and wood-plastic compounds |
Pipe, tubing, window frames, seals, cable ducts and custom profiles |
Approximately 10–1,500 kg/h, depending on product size and material |
Commonly 150–230°C; profile stability depends strongly on die and calibration design |
Continuous dimensional production with calibrated cooling and controlled haul-off |
Die design and downstream calibration must be matched closely to the product geometry |
| Recycling Extruder with Degassing |
Post-industrial or post-consumer PE, PP, PS and selected mixed plastic streams |
Film recycling, rigid-flake recycling, repelletizing and material recovery |
Approximately 50–2,500 kg/h, depending on contamination and feed preparation |
Usually 160–260°C; temperature must be balanced against contamination and polymer degradation |
Vacuum degassing can remove moisture and volatile compounds during melt processing |
Feed quality, moisture, contamination and filtration requirements strongly affect output |