TPU Production Systems
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TPU Compounding Line | HFFR Cable Grades

Gravimetric TPU and mineral-additive feeding with configured compounding, venting and pelletizing for cable-grade development.

Low-Smoke Zero-Halogen (HFFR) Extrusion & Pelletizing

High-Filler Low-Shear Compounding for Flame-Retardant Cable TPU

Gravimetric TPU and mineral-additive feeding with configured compounding, venting and pelletizing for cable-grade development.

Gravimetric TPU and mineral-additive feeding with configured compounding, venting and pelletizing for cable-grade development.

Pellet feed, staged powder side feeds, liquid additives, compounding extruder and pelletizing stages; cable extrusion, final formulation and finished-cable qualification are separate.

This is pellet/additive compounding rather than a primary liquid reactive-polymerization route. UL 94 V-0 at 0.8 mm and oxygen index concern the tested compound/specimen; they do not establish cable qualification or machine certification. Feeder accuracy and final dispersion are different measures.

Concept illustration: Generated concept illustration for process discussion; not a photograph of the specified machine, a customer facility or a delivered project.

High-Filler Low-Shear Compounding for Flame-Retardant Cable TPU

Material Flow and Working Principle

Gravimetric Loss-in-Weight Base Polymer Feeding

TPU base resin pellets and functional processing aids are metered into the main extruder throat via twin-screw gravimetric loss-in-weight feeders under digital mass-flow control.

Polymer Plasticization & Melt Homogenization

The base resin is gently melted across the initial five barrel zones through forward-conveying elements, establishing a sealed, molten polymer pool before filler entry.

Twin-Stage High-Volume Powder Side-Stuffing

Dense mineral flame-retardant powders (ATH/MCA) are de-aerated and rammed into the molten TPU pool via twin-screw co-rotating side feeders at up to 60% loading ratios.

Low-Shear Distributive Blending & Vacuum De-Watering

Specially profiled distributive mixing gears disperse powder aggregates into the matrix, while dual high-vacuum ports (0.05 kPa) strip mineral hydration moisture and trapped air.

Die-Face Water-Ring Pelletizing & Classification

The filled melt is extruded through wear-resistant carbide die plates, sliced by high-speed rotary cutters into water rings, centrifugally spin-dried, and classified by vibrating screens.

Configuration data

Model and Technical Parameters

Supplied HF-TPU75-HFFR configuration references, pending original calibration and acceptance documents. Material, finished-part and project outcomes are separate from equipment ratings. This is pellet/additive compounding rather than a primary liquid reactive-polymerization route. UL 94 V-0 at 0.8 mm and oxygen index concern the tested compound/specimen; they do not establish cable qualification or machine certification. Feeder accuracy and final dispersion are different measures.

Technical ParameterHF-TPU75-HFFR
ComponentsSolid Feeding (TPU Pellets + 2 Powder Streams + Liquid Additive)
Output Range (g/s)300.0 to 800.0 kg/h (Continuous compound output)
Mixing Ratio Range40% to 60% Mineral Filler by weight
Ratio Accuracy±0.3% (Gravimetric loss-in-weight feeders)
Power Supply380V, 3-Phase, 50Hz (Custom 440V/480V 60Hz optional)
Working Pressure8.0 to 14.0 MPa (Extruder die discharge and pelletizer head)
Tank Capacity (L)Day hoppers: 1 x 500 L (Pellet), 2 x 300 L (Powder de-aerated)
Weight16,200 kg (Extruder, side feeders, and water-ring pelletizer)
Dimensions (L×W×H)20,500 mm x 3,600 mm x 3,100 mm
Flame Retardancy ClassificationUL94 V-0 (At 0.8 mm specimen thickness); Standard vertical burning test; supplied reference pending original configuration or test records
Tensile Elongation at Break≥ 400% (ASTM D412 test on compounded cable core); Compound tensile test coupon; supplied reference pending original configuration or test records
Side Feeder Processing CapacityUp to 500 kg/h (De-aerated powder compaction); Dual-stage co-rotating stuffer; supplied reference pending original configuration or test records
Limiting Oxygen Index (LOI)≥ 35% (ASTM D2863 oxygen index test); Finished HFFR TPU pellets; supplied reference pending original configuration or test records
Equipment configuration

Key Equipment Features

Pellet feed, staged powder side feeds, liquid additives, compounding extruder and pelletizing stages; cable extrusion, final formulation and finished-cable qualification are separate.

UL94 V-0 at 0.8 mm Compliance

Supplied configuration reference: Optimized filler dispersion achieves self-extinguishing flame resistance compliant with UL94 V-0 and zero dripping. Actual capability requires material and tooling validation.

Dual-Stage Side-Feeding (Up to 60%)

Supplied configuration reference: High-capacity side stuffers ram bulky flame-retardant powders without hopper bridging or back-venting. Actual capability requires material and tooling validation.

Retained Elongation at Break > 400%

Supplied configuration reference: Low-shear distributive mixing prevents polymer chain degradation, preserving high cable flexibility. Actual capability requires material and tooling validation.

Water-Ring Die-Face Cutting

Supplied configuration reference: Eliminates frequent strand-break shutdowns common to water-cooled strand pelletizers on highly filled compounds. Actual capability requires material and tooling validation.

Planning questions

Frequently Asked Questions

How does the line feed 60% mineral powder without hopper bridging?
Co-rotating twin-screw side stuffers force de-aerated powder directly into the molten polymer pool. Confirm the applicable material, tooling, test method and original records for the specified configuration.
Why is low-shear distributive mixing critical for retaining 400% elongation?
Excessive shear thermal degradation breaks TPU polymer backbones; gentle distributive blocks disperse powder without chain scission. Confirm the applicable material, tooling, test method and original records for the specified configuration.
What prevents cable surface roughness and pinholes during jacket extrusion?
Fine powder dispersion and multi-stage 0.05 kPa vacuum de-volatilization eliminate agglomerates and moisture pockets. Confirm the applicable material, tooling, test method and original records for the specified configuration.
Why is water-ring cutting superior to water-bath strand cutting for HFFR TPU?
High mineral loads make molten strands brittle; die-face water-ring cutting eliminates strand breakage shutdowns. Confirm the applicable material, tooling, test method and original records for the specified configuration.