Application · Biodegradable & PLA
PLA Pelletizing: Temperature Window & Drying
PLA has a 30 °C working window. Ten degrees low and it will not melt homogenously; ten degrees high and molecular weight drops in a step, not a slope. A reference pla pelletizing page from Kerke.
Quick answer
PLA compounding and pelletizing needs precise temperature control (140–190 °C), vacuum devolatilization and moisture below 250 ppm to avoid hydrolysis. Output 100–800 kg/h on KTE-50B/65B with air-cooled strand pelletizing.
Workshop photos and a running video — shot on our own lines, not stock images.
What sets the limit
PLA is crystallized and dried, metered into a low-shear melt zone, devolatilized, filtered and strand-pelletized with air cooling. Residence time is kept short to protect IV.
| Parameter | Value / range |
|---|---|
| Temperature | 140–190 °C |
| Moisture target | < 250 ppm after drying |
| L/D | 40–44 |
| Devolatilization | Vacuum vent, 2 stages for high IV grades |
| Output (reference) | 100–800 kg/h |
| Model | KTE-50B, KTE-65B |
Output figures are measured on the reference material stated above. Filler grade, bulk density and moisture move output by ±15% — that is why every quotation we issue is tied to a trial report.
Process flow, step by step
- FeedingLoss-in-weight dosing of polymer and filler; side feeder or liquid injection where the formulation needs it.
- Melting and dispersingScrew geometry with 45°/90° kneading blocks; barrel profile 140–190 °C.
- DevolatilizationVacuum vent at −0.06 to −0.09 MPa removes moisture and volatiles before the die.
- Pressure build-upThrottle or discharge section stabilises die pressure; a melt pump where gauge control matters.
- Pelletizing and packingdie-face or strand pelletizing, see the pelletizing page; then centrifugal dryer, vibrating screen and bagging.
Equipment configuration
| Stage | Equipment | Why this choice |
|---|---|---|
| Main machine | Co-Rotating Twin Screw Extruder | Architecture follows the filling level and the mixing duty, not the required tonnage. |
| Screw geometry | Building-block elements, W6Mo5Cr4V2, bimetallic liner | Wear package for abrasive filler; mixing blocks only where dispersion demands them. |
| Feeding | Loss-in-weight feeder, side feeder where needed | Recipe accuracy: ±0.5% short term on the weighed component. |
| Pelletizing | Pelletizing system | Chosen by polymer and filler ceiling — water contact is the deciding column. |
| Downstream | Centrifugal dryer, vibrating screen, bagging | Fines below 2% and moisture below the specification of your downstream process. |
Output by model
| Model | Dia. (mm) | Speed (rpm) | Motor (kW) | Torque (N·m) | Output (kg/h) |
|---|---|---|---|---|---|
| KTE-50B | 50.5 | 500–600 | 55–75 | 2×525 | 80–200 |
| KTE-50D | 50.5 | 300–800 | 75–90 | 2×860 | 100–300 |
| KTE-52B | 51.4 | 500–600 | 55–75 | 2×720 | 80–200 |
| KTE-52D | 51.4 | 500–600 | 75–110 | 2×1050 | 100–400 |
| KTE-65B | 62.4 | 500–600 | 90–110 | 2×860 | 200–450 |
| KTE-65D | 62.4 | 300–800 | 132–160 | 2×1530 | 350–600 |
| KTE-75B | 71 | 500–600 | 132–160 | 2×1530 | 300–800 |
| KTE-75D | 71 | 300–800 | 200–315 | 2×2100 | 500–1000 |
| KTE-85B | 85 | 500–600 | 220–315 | 2×2100 | 550–1000 |
| KTE-95B | 93 | 500–600 | 250–315 | 2×3000 | 800–1500 |
| KTE-95D | 93 | 500–800 | 315–500 | 2×4800 | 1000–2000 |
| KTE-135B | 135 | 500–600 | 315–500 | 2×4800 | 1500–3000 |
| KTE-135D | 135 | 500–800 | 500–1000 | 2×7800 | 1500–4000 |
Three mistakes that cost the most
1. Skipping crystallization before drying fuses the pellets into a block.
Skipping crystallization before drying fuses the pellets into a block.
2. High shear screws raise melt temperature and drop IV measurably.
High shear screws raise melt temperature and drop IV measurably.
3. Water bath above 25 °C
Water bath above 25 °C — strands embrittle and break, and the pellets start hydrolysing before they reach the bag; hold the bath at 15–25 °C.
FAQ
How much IV loss per pass?
0.02–0.05 dL/g with a properly dried feed and low-shear screw; more than 0.1 means the drying or temperature is wrong.
Can the same line run PBAT?
Yes — PBAT runs at lower temperature and needs a different screw profile, but the platform is the same.
What output can you guarantee for this application?
The reference band is 100–800 kg/h, measured on the stated material. We quote a guaranteed figure only after a trial on your own material, because filler grade, bulk density and moisture move output by ±15%.
Can we run our material before ordering?
Yes — send 25–50 kg. We return pellets, a running video and a report with temperatures, screw speed, feeder settings and output per hour. The trial is free; you cover the freight.
What is the delivery time?
30–45 working days for standard configurations, 45–70 for custom screw geometry and ODM work. Voltage and frequency are built for the destination country.
Where these numbers come from
Parameters are taken from the Kerke product parameter table and the product master data sheet, and cross-checked against commissioning records for lines in the same application. Formulations and temperature windows are typical industry values, not a recommendation for your specific compound — every figure marked reference must be confirmed on a material trial before it becomes a contractual number.
Reviewed by the Kerke process team, Nanjing. Page updated 6 November 2026.
Send 25–50 kg and we run it on our lab extruder: pellets, running video and a capacity report back in 3–7 days.
PLA pelletizing — the short version
Note on pla pelletizing: the numbers above are reference ranges from Kerke's own trial runs, not catalogue promises. Screw geometry, wear package and pelletizing method are set on the trial bench first, so the output you compare is the output you get. If your grade is not in the tables, send it — the closest configuration is usually a change of screw set, not a different machine.
Related on this site: Machine range: KTE-50B to 135D · Pelletizing methods compared · quotation and free trial · Wikipedia: Masterbatch






