Aliphatic TPU Two-Step Production Solution Banner background

Aliphatic TPU Two-Step Production Solution

A two-stage aliphatic TPU process with prepolymer preparation, reactive extrusion, melt conditioning and pelletizing for film-grade development.

Process configuration

Extreme Purity & Non-Yellowing Optical Precision for PPF Resins

A two-stage aliphatic TPU process with prepolymer preparation, reactive extrusion, melt conditioning and pelletizing for film-grade development.

Equipment and process scope

Selected prepolymer reactor, liquid feed circuits, twin-screw extruder, melt pump, pelletizer and drying interfaces. Film conversion and optical testing are separate downstream processes.

Validation and production planning

CSTR and tubular reactor are different architectures and must be reconciled from the supplied description. Polymerization is not permanent thermoset crosslinking. Optical defect counts are film-conversion results, and ASTM E313 describes color-index calculations rather than the complete weathering exposure. Yellowing method, film thickness and sampling need original records.

Selected prepolymer reactor, liquid feed circuits, twin-screw extruder, melt pump, pelletizer and drying interfaces. Film conversion and optical testing are separate downstream processes. CSTR and tubular reactor are different architectures and must be reconciled from the supplied description. Polymerization is not permanent thermoset crosslinking. Optical defect counts are film-conversion results, and ASTM E313 describes color-index calculations rather than the complete weathering exposure. Yellowing method, film thickness and sampling need original records.Generated concept illustration for process discussion; not a photograph of the specified machine, a customer facility or a delivered project.

Process configuration

Turnkey Two-Step Aliphatic TPU Synthesis Workflow

Configuration sequence from the supplied brief. Material, tool, pressure/temperature basis and complete line balance require verification. CSTR and tubular reactor are different architectures and must be reconciled from the supplied description. Polymerization is not permanent thermoset crosslinking. Optical defect counts are film-conversion results, and ASTM E313 describes color-index calculations rather than the complete weathering exposure. Yellowing method, film thickness and sampling need original records.

01

Continuous Tubular CSTR Pre-Reaction (Step 1)

Supplied process reference: Dehydrated PCL polyol and pure liquid H12MDI are metered into a jacketed tubular CSTR reactor at 90°C under nitrogen, forming a uniform prepolymer.

PRE-REACTION TEMP 90°C ± 0.5°C; VISCOSITY 1,200 MPA·S; CONFIRM FOR SELECTED MATERIAL AND TOOLING
02

High-Torque Mirror Screw Extension (Step 2)

Supplied process reference: Prepolymer enters Zone 1 of the L/D = 60 mirror extruder; micro-nozzles inject BDO extender and bismuth catalysts to complete linear chain growth.

BARREL L/D = 60; ROUGHNESS RA ≤ 0.05 µM; CONFIRM FOR SELECTED MATERIAL AND TOOLING
03

Three-Stage Deep-Vacuum De-Volatilization

Supplied process reference: The reacting melt traverses three vacuum vents operating down to 0.02 kPa, extracting unreacted monomers and micro-moisture to achieve optical clarity.

DE-VOLATILIZATION VACUUM ≤ 0.02 KPA; 3 PORTS; CONFIRM FOR SELECTED MATERIAL AND TOOLING
Process configuration

Reference Solution Engineering Envelope

Supplied configuration and validation references; material/component results are separate from equipment ratings.

ParameterValue / UnitApplicable Configuration / Conditions
Continuous Production Output150.0 to 500.0 kg/hourHigh-torque co-rotating twin-screw extruder with CSTR; supplied configuration or material target, pending the applicable original records
Extruder Screw ArchitectureØ 65 mm, L/D = 60Modular PVD mirror-finish screw elements (Ra ≤ 0.05 µm); supplied configuration or material target, pending the applicable original records
Optical Gel Defect ThresholdLess than 2 parts/m²Verified via automated optical inspection on 150 µm film; supplied configuration or material target, pending the applicable original records
Accelerated UV Yellowing IndexΔ YI < 0.8 (CIE Lab)1,000 hours QUV-A exposure under ASTM E313; supplied configuration or material target, pending the applicable original records
Chemical Dosing PrecisionRatio tolerance within ±0.1%Four-stream Coriolis mass-flow closed-loop skid; supplied configuration or material target, pending the applicable original records
De-Volatilization Vacuum LevelAbsolute pressure ≤ 0.02 kPaThree-stage multi-port vacuum extraction skid with cold traps; supplied configuration or material target, pending the applicable original records
CSTR and tubular reactor are different architectures and must be reconciled from the supplied description. Polymerization is not permanent thermoset crosslinking. Optical defect counts are film-conversion results, and ASTM E313 describes color-index calculations rather than the complete weathering exposure. Yellowing method, film thickness and sampling need original records.

Core Equipment for This Solution

Selected prepolymer reactor, liquid feed circuits, twin-screw extruder, melt pump, pelletizer and drying interfaces. Film conversion and optical testing are separate downstream processes.

Core Advantages of Haifeng Optical TPU Systems

Configured equipment functions and interfaces for the selected material and tooling.

reported Fish-Eyes < 2 parts/m²

Supplied configuration function: Two-step CSTR prepolymerization eliminates unreacted monomer pockets, ensuring pristine optical film clarity. Project-dependent performance requires validation.

Non-Yellowing Δ YI < 0.8 Stability

Supplied configuration function: Aliphatic H12MDI/PCL molecular architecture and PVD-coated barrels eliminate metallic ion yellowing catalysts. Project-dependent performance requires validation.

Deep 0.02 kPa Vacuum Extraction

Supplied configuration function: Three-stage de-volatilization strips residual monomers and moisture, eliminating film bubble haziness. Project-dependent performance requires validation.

Ultra-Pure Deionized Pelletizing

Supplied configuration function: Cleanroom tempered deionized water cutting prevents surface salt marks and dust contamination on pellets. Project-dependent performance requires validation.

Related review draft

Related Project Draft

An anonymous project brief from the supplied document. Original attribution, dates, acceptance and outcome records require verification before public use.

Review Project
Planning questions

Frequently Asked Questions

How does two-step CSTR prepolymerization prevent film fish-eye gels? +
It ensures complete stoichiometric pre-reaction of H12MDI before chain extension, preventing micro-gel seeds. Confirm the applicable formulation, geometry and original test records. CSTR and tubular reactor are different architectures and must be reconciled from the supplied description. Polymerization is not permanent thermoset crosslinking. Optical defect counts are film-conversion results, and ASTM E313 describes color-index calculations rather than the complete weathering exposure. Yellowing method, film thickness and sampling need original records.
Why is PVD mirror coating necessary on screw elements and barrels? +
It eliminates microscopic crevices (Ra ≤ 0.05 µm) where resin could hang up and scorch into black specks. Confirm the applicable formulation, geometry and original test records. CSTR and tubular reactor are different architectures and must be reconciled from the supplied description. Polymerization is not permanent thermoset crosslinking. Optical defect counts are film-conversion results, and ASTM E313 describes color-index calculations rather than the complete weathering exposure. Yellowing method, film thickness and sampling need original records.
What prevents the high-purity water pelletizer from picking up dust? +
The water circulation is closed, filtered through 0.1 µm sub-micron filters, and maintained under HEPA cleanroom hoods. Confirm the applicable formulation, geometry and original test records. CSTR and tubular reactor are different architectures and must be reconciled from the supplied description. Polymerization is not permanent thermoset crosslinking. Optical defect counts are film-conversion results, and ASTM E313 describes color-index calculations rather than the complete weathering exposure. Yellowing method, film thickness and sampling need original records.
Can this line produce polycaprolactone (PCL) and polycarbonate (PCDL) blends? +
Yes, independent multi-stream feed pumps process both PCL and PCDL polyols to tailor film softness and hydrolysis. Confirm the applicable formulation, geometry and original test records. CSTR and tubular reactor are different architectures and must be reconciled from the supplied description. Polymerization is not permanent thermoset crosslinking. Optical defect counts are film-conversion results, and ASTM E313 describes color-index calculations rather than the complete weathering exposure. Yellowing method, film thickness and sampling need original records.

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