Multi-Block Copolymer Synthesis via Chain Shuttling

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Solution Overview

Problem

Current methods for producing block copolymers, particularly those involving propylene and 4-methyl-1-pentene, face limitations such as requiring sequential monomer addition, narrow molecular weight distribution, high process costs, and inability to produce polymers with optimal tacticity and crystallinity, leading to inefficient and inhomogeneous block distributions.

Innovation Solution

A composition comprising a first and second olefin polymerization catalyst, along with a chain shuttling agent, is used to produce multi-block copolymers with alternating blocks of atactic and isotactic polypropylene or poly-4-methyl-1-pentene, allowing for continuous solution polymerization and independent control of block sequencing and tacticity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If anionic or free-radical polymerization methods are used to prepare block copolymers, then block copolymer formation is achieved, but the process requires sequential monomer addition, batch processing, and produces extremely narrow molecular weight distribution with poor process economics

Engineering Contradiction:
Improveblock copolymer structure controlVSAvoidprocess efficiency
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The patent changes the fundamental polymerization parameters by using coordination polymerization catalysts (such as Ziegler-Natta catalysts) instead of anionic or free-radical initiators. This parameter change enables continuous processing, broader molecular weight distribution, and improved process economics while maintaining block copolymer structure control through catalyst-specific monomer addition sequences.

Inventive Principle:
Principle #35Parameter changes

2Manufacturing precision

If conventional coordination polymerization catalysts are used to suppress chain-transfer, then block-like structure is formed, but the process requires low temperatures and sequential monomer addition, resulting in high process operating costs

Engineering Contradiction:
Improveblock structure formationVSAvoidprocess operating cost
Core Design Contradiction:
Manufacturing precisionVSUse of energy by stationary object

Solution Approach 1:

The patent implements continuous polymerization processes using coordination catalysts, eliminating the need for sequential monomer addition and low-temperature batch processing. The continuous operation at elevated temperatures significantly reduces process operating costs while maintaining block structure formation through controlled monomer feeding rates and catalyst activity management.

Inventive Principle:
Principle #20Continuity of useful action

3Manufacturing precision

If sequential monomer addition is used in batch processing, then block copolymer synthesis is achieved, but the production rate is limited and inhomogeneous block distributions result

Engineering Contradiction:
Improveblock distribution uniformityVSAvoidproduction rate
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The patent transitions from batch to continuous polymerization processing, enabling uninterrupted monomer conversion to polymer. This continuous operation eliminates the inhomogeneous block distributions characteristic of sequential batch addition, while significantly increasing production rates through sustained catalytic activity and improved heat/mass transfer efficiency.

Inventive Principle:
Principle #20Continuity of useful action

4Device complexity

If a single catalyst system is used, then polymerization is simplified, but the ability to produce polymers with specific tacticity and crystallinity is limited

Engineering Contradiction:
Improvecatalyst system complexityVSAvoidtacticity control
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The patent employs multiple catalyst systems with different stereoselective characteristics to produce polymers with specific tacticity and crystallinity. By segmenting the catalytic function into distinct catalyst types (e.g., isotactic and syndiotactic catalysts), the process achieves precise control over polymer microstructure while maintaining manageable system complexity through modular catalyst design.

Inventive Principle:
Principle #1Segmentation

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This approach enables the production of high molecular weight, segmented copolymers with improved physical properties, including a narrow molecular weight distribution and enhanced tacticity, overcoming the inefficiencies of existing methods by allowing for high-yield, continuous production of polymers with specific block structures.

Implementation Method 1

a chain shuttling agent; wherein the chain shuttling agent causes polymer chain transfer between the catalyst sites

Methodology Applied
Scientific EffectChain shuttling:

Implementation Method 2

a first olefin polymerization catalyst, and a second olefin polymerization catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

homogeneous coordination polymerization catalysts can be used to prepare polymers having a substantially 'block-like' structure

Methodology Applied
Scientific EffectCoordination polymerization:

Data Source

PatentUS8981028B2Catalyst composition comprising shuttling agent for tactic/ atactic multi-block copolymer formation
Publication Date: 2015.03.17 DOW GLOBAL TECHNOLOGIES LLC
  • US8981028B2 patent drawing
  • US8981028B2 patent drawing
  • US8981028B2 patent drawing

AI summary

Copolymers, especially multi-block copolymer containing therein two or more segments or blocks differing in tacticity, are prepared by polymerizing propylene, 4-methyl-1-pentene, or another C4-8 α-olefin in the presence of a composition comprising the admixture or reaction product resulting from combining: (A) a first metal complex olefin polymerization catalyst, (B) a second metal complex olefin polymerization catalyst capable of preparing polymers differing in tacticity from the polymer prepared by catalyst (A) under equivalent polymerization conditions, and (C) a chain shuttling agent.