Application · Thermoplastic Elastomer
TPE/TPU/TPR Pelletizing: Hardness 30–90A
Elastomer compounding is dominated by oil: SEBS takes 100–300 phr, and injecting it all at once makes the screw slip instead of mix. Split the injection and the same machine behaves. A reference tpe tpu tpr pelletizing page from Kerke.
Quick answer
TPE, TPU and TPR compounds from Shore 30A to 90A run on a twin screw with L/D 44–52 and underwater pelletizing for round, free-flowing pellets. Output 200–1,500 kg/h. SEBS oil absorption and TPV dynamic vulcanization need different screw designs.
Workshop photos and a running video — shot on our own lines, not stock images.
What sets the limit
SEBS or base polymer is fed with oil in a dedicated absorption zone, compounded with PP and filler, then underwater pelletized. TPV requires a dynamic vulcanization zone with controlled residence time.
| Parameter | Value / range |
|---|---|
| Hardness | Shore 30A–90A (TPE/TPU/TPR range) |
| L/D | 44–52 |
| Oil absorption | Up to 3× rubber weight for SEBS |
| Pelletizing | Underwater (round pellets, no blocking) |
| Output (reference) | 200–1,500 kg/h |
| Model | KTE-65B, KTE-75B |
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 set by the polymer.
- 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 packingUnderwater (round pellets, no blocking); 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. Oil added too early
Oil added too early — the feed throat slips and output fluctuates.
2. Strand pelletizing TPE gives sticky, blocking pellets; underwater is the practical choice.
Strand pelletizing TPE gives sticky, blocking pellets; underwater is the practical choice.
3. TPU run wet
TPU run wet — 0.1% moisture gives bubbles in the pellet and drifting hardness; dry 80–90 °C for 2–3 h and keep the opened bags resealed.
FAQ
Can one line run TPE and TPV?
Yes with a screw set change; TPV needs a longer vulcanization zone and tighter temperature control.
What oil ratio is feasible?
Up to 3:1 oil to rubber for soft grades; above that the melt strength is too low for pelletizing.
What output can you guarantee for this application?
The reference band is 200–1,500 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.
TPE TPU TPR pelletizing — the short version
Note on tpe tpu tpr 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






