TPU Production Systems
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TPU Reactive Extrusion Line | Blown-Film Grades

TPU feed preparation, reactive extrusion and melt stabilization for downstream thin-film processing and grade development.

Ultra-High Molecular Weight Extrusion & Calendering Granulation

High Melt-Strength Reactive Synthesis for Technical TPU Films

TPU feed preparation, reactive extrusion and melt stabilization for downstream thin-film processing and grade development.

TPU feed preparation, reactive extrusion and melt stabilization for downstream thin-film processing and grade development.

Conditioned liquid feed streams, extruder, melt pump, venting and pelletizing/drying stages. Blown-film tower, formulation and final application qualification are separate interfaces.

The document reports 74.5 h uninterrupted operation inside a stated 72 h assessment; reconcile observation duration and aggregation. Melt pressure variation is not a guarantee of downstream bubble stability. MVTR varies with film thickness and method. Medical-use suitability is not established by the equipment brief.

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

High Melt-Strength Reactive Synthesis for Technical TPU Films

Material Flow and Working Principle

Four-Stream Dehydrated Chemical Metering

High-purity PTMEG polyol, pure MDI, BDO extender, and trifunctional branching curatives are conditioned under nitrogen at 80°C and metered into the throat with mass-flow precision within ±0.15%.

High-Molecular-Weight Twin-Screw Reaction

The formulation advances through an extended L/D = 58 extruder barrel, undergoing controlled chain extension and long-chain branching across 14 zones to achieve number-average molecular weights above 120,000.

High-Torque Melt Pump Pressure Decoupling

An oil-jacketed melt gear pump pulls polymer from screw tips, decoupling extrusion variance and keeping discharge pressure fluctuations below 0.05 MPa into a 325-mesh hydraulic screen changer.

Die-Face Underwater Cutting & Clean Water Slurry

The viscous melt is extruded through multi-orifice die plates into a flooded cutting chamber, where high-speed multi-knife cutters slice uniform spherical pellets in tempered 50°C water.

Centrifugal Spin Dewatering & Dehumidified Storage

The pellet slurry transfers to a high-speed spin dryer dropping moisture below 0.02% (200 ppm), discharging into sealed aluminum-lined storage bags to protect high-melt-strength integrity.

Configuration data

Model and Technical Parameters

Supplied HF-TPU85-FLM configuration references, pending original calibration and acceptance documents. Material, finished-part and project outcomes are separate from equipment ratings. The document reports 74.5 h uninterrupted operation inside a stated 72 h assessment; reconcile observation duration and aggregation. Melt pressure variation is not a guarantee of downstream bubble stability. MVTR varies with film thickness and method. Medical-use suitability is not established by the equipment brief.

Technical ParameterHF-TPU85-FLM
Components4 Liquid Streams (PTMEG Polyol, Pure MDI, BDO, Branching Agent)
Output Range (g/s)250.0 to 750.0 kg/h (Continuous compound throughput)
Mixing Ratio Range100:32:8:0.5 to 100:60:18:1.5 (By weight)
Ratio Accuracy±0.15% (Continuous closed-loop Coriolis feedback)
Power Supply380V, 3-Phase, 50Hz (Custom 440V/480V 60Hz optional)
Working Pressure12.0 to 18.0 MPa (Extruder die discharge and pelletizer head)
Tank Capacity (L)Day tanks: 2 x 1,000 L (Stainless steel with thermal jackets)
Weight17,800 kg (Combined extruder, gear pump, and pelletizer)
Dimensions (L×W×H)24,500 mm x 3,600 mm x 3,200 mm
Minimum Blown Film ThicknessDown to 0.015 mm (15 µm continuous bubble); Downstream blown-film tower; supplied reference pending original configuration or test records
Melt Pump Pressure Fluctuation< ±0.03 MPa (At 15.0 MPa delivery pressure); Oil-jacketed melt gear pump; supplied reference pending original configuration or test records
Moisture Vapor Transmission (MVTR)≥ 8,000 g/(m²·24h) (25 µm film thickness); ASTM E96 Inverted Cup method; supplied reference pending original configuration or test records
Number-Average Molecular WeightMn ≥ 120,000 (GPC measurement in THF); Cured polymer pellet sample; supplied reference pending original configuration or test records
Equipment configuration

Key Equipment Features

Conditioned liquid feed streams, extruder, melt pump, venting and pelletizing/drying stages. Blown-film tower, formulation and final application qualification are separate interfaces.

0.015 mm Ultra-Thin Blown Film

Supplied configuration reference: High melt strength eliminates bubble sagging, enabling stable continuous blowing down to 15 microns. Actual capability requires material and tooling validation.

< 0.05 MPa Pressure Ripple

Supplied configuration reference: Jacketed melt gear pump decouples screw surges, locking die pressure fluctuations under 0.05 MPa. Actual capability requires material and tooling validation.

72-Hour Continuous Run

Supplied configuration reference: Molecular uniformity prevents die lip drool and fish-eye buildup, supporting 72-hour non-stop film production. Actual capability requires material and tooling validation.

≥ 8,000 g/(m²·24h) Breathability

Supplied configuration reference: Polyether matrix structure delivers extreme moisture vapor permeability for technical outdoor apparel. Actual capability requires material and tooling validation.

Planning questions

Frequently Asked Questions

How does this line prevent bubble sagging during 0.015 mm thin blown-film runs?
Controlled long-chain branching elevates melt strength and extensional viscosity, stabilizing the bubble neck. Confirm the applicable material, tooling, test method and original records for the specified configuration.
Why is a melt gear pump essential for high-molecular-weight reactive extrusion?
It dampens screw pressure surges, holding discharge pressure fluctuations below 0.05 MPa into the die. Confirm the applicable material, tooling, test method and original records for the specified configuration.
What enables the material to achieve MVTR > 8,000 g/(m²·24h)?
TPU feed preparation, reactive extrusion and melt stabilization for downstream thin-film processing and grade development. Conditioned liquid feed streams, extruder, melt pump, venting and pelletizing/drying stages. Blown-film tower, formulation and final application qualification are separate interfaces. The document reports 74.5 h uninterrupted operation inside a stated 72 h assessment; reconcile observation duration and aggregation. Melt pressure variation is not a guarantee of downstream bubble stability. MVTR varies with film thickness and method. Medical-use suitability is not established by the equipment brief.
Can this resin be processed on conventional LDPE or EVA blown-film towers?
Yes, wide processing windows allow processing on standard film towers fitted with low-shear barrier screws. Confirm the applicable material, tooling, test method and original records for the specified configuration.