Ethylene Polymer Particle Composition for Flowable Stretch Molding

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Solution Overview

Problem

Current methods for producing ultrahigh molecular weight ethylenic polymer particles face challenges with poor flowability, leading to issues like fouling, coarse particle formation, and increased production costs, which affect the industrial productivity and physical properties of the final product.

Innovation Solution

The development of ethylenic polymer particles with specific surface areas, intrinsic viscosities, and bulk densities, along with the use of a compound with a molecular backbone and magnesium content, enhances flowability and inhibits fouling, allowing for improved stretch moldability and bindability.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Strength

If ultrahigh molecular weight ethylenic polymer is used, then impact resistance and strength are improved, but flowability deteriorates

Engineering Contradiction:
Improveimpact resistanceVSAvoidflowability
Core Design Contradiction:
StrengthVSEase of operation

Solution Approach 1:

The patent changes the molecular weight parameter of the ethylenic polymer to a specific range (intrinsic viscosity 6-30 dl/g) to optimize both strength and flowability. This parameter optimization allows the polymer to maintain high impact resistance while achieving sufficient flowability for molding operations.

Inventive Principle:
Principle #35Parameter changes

2Ease of manufacture

If solid phase stretch molding is used, then molding capability is improved, but coarse particle formation occurs

Engineering Contradiction:
Improvemolding capabilityVSAvoidparticle uniformity
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent optimizes the particle size parameters (median diameter 20-700 μm, specific surface area 0.5-5.0 m²/g) of the ethylenic polymer particles to prevent coarse particle formation during solid phase stretch molding. This ensures uniform feeding and molding while maintaining the molding capability.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If polymerization is conducted without fouling inhibition, then productivity is improved, but coarse particles and fouling increase

Engineering Contradiction:
Improveproduction efficiencyVSAvoidparticle size uniformity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent introduces a specific polymerization catalyst system (Ziegler-Natta catalyst with specific components and ratios) as an intermediary to control the polymerization process. This catalyst system enables high productivity while preventing fouling and coarse particle formation by controlling the polymerization kinetics and particle morphology.

Inventive Principle:
Principle #24Intermediary (Mediator)

4Ease of operation

If powder transfer is performed with coarse particles, then material handling is simplified, but feed uniformity deteriorates

Engineering Contradiction:
Improvematerial handlingVSAvoidfeed uniformity
Core Design Contradiction:
Ease of operationVSManufacturing precision

Solution Approach 1:

The patent optimizes the particle size distribution parameters (median diameter 20-700 μm, specific surface area 0.5-5.0 m²/g) to achieve a balance between material handling ease and feed uniformity. The controlled particle size distribution prevents coarse particle aggregation while maintaining free-flowing characteristics for uniform powder transfer and feeding.

Inventive Principle:
Principle #35Parameter changes

Data Source

PatentEP4474399A1Ethylene polymer particles, method for producing ethylene polymer particles, stretch molded body, method for producing stretch molded body, and use of same
Publication Date: 2024.12.11 MITSUI CHEMICALS INC
  • EP4474399A1 patent drawing
  • EP4474399A1 patent drawing
  • EP4474399A1 patent drawing

AI summary

One embodiment of the present invention is an ethylenic polymer particle, having a specific surface area of larger than 2.00 m2/g and 30.0 m2/g or smaller, as determined by a BET method from the adsorption/desorption isotherms measured by a nitrogen gas adsorption method, and a median diameter (D50) of 20 µm or larger and 700 pm or smaller as determined by laser diffraction/scattering.