Emulsion Polymerization of 1,1-Disubstituted Alkenes

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Solution Overview

Problem

The polymerization of 1,1-disubstituted alkene compounds using anionic polymerization is challenging due to difficulties in controlling the structure and properties of the resulting polymers, particularly in bulk polymerization, where high viscosity and temperature spikes occur, and emulsion polymerization is hindered by reactivity with water and surfactants, leading to issues like particle aggregation and undesirable by-products.

Innovation Solution

An emulsion polymerization process is developed involving agitation of a mixture with a carrier liquid and surfactant to form micelles, followed by anionic polymerization initiated with an activator, allowing for controlled polymerization of 1,1-disubstituted alkene monomers to achieve specific molecular weights and sequence distributions, and the use of an acid-containing compound to stabilize the emulsion and control reaction rates.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If bulk polymerization is used to polymerize 1,1-disubstituted alkene compounds, then high molecular weight polymer is produced, but the polymer exhibits high viscosity and difficult handling

Engineering Contradiction:
Improvemolecular weightVSAvoidhandling difficulty
Core Design Contradiction:
Quantity of substanceVSEase of operation

Solution Approach 1:

The patent applies segmentation by dividing the bulk polymerization process into multiple controlled stages with sequential monomer additions. This allows the polymerization to proceed in manageable increments, controlling viscosity at each stage while building up molecular weight over time, thereby maintaining ease of handling throughout the process.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent employs dynamic control of polymerization conditions by adjusting temperature, addition rates, and catalyst concentrations during the process. This dynamic approach allows optimization of molecular weight growth while controlling viscosity increases, ensuring the polymer remains handleable throughout production.

Inventive Principle:
Principle #15Dynamics

2Productivity

If bulk polymerization is used to achieve high conversion, then polymer yield increases, but temperature spikes occur during the process

Engineering Contradiction:
Improvepolymer yieldVSAvoidtemperature control
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The patent implements periodic action through staged monomer addition and controlled reaction intervals. By adding monomers in stages and allowing controlled reaction periods between additions, the exothermic heat generation is distributed over time rather than occurring all at once, preventing temperature spikes while maintaining high overall yield.

Inventive Principle:
Principle #19Periodic action

Solution Approach 2:

The patent maintains continuous useful action through optimized reaction conditions and staged additions that keep the polymerization proceeding efficiently without interruption. This continuous controlled process achieves high conversion and yield while managing heat generation through sustained, controlled reaction rather than intermittent high-intensity reactions.

Inventive Principle:
Principle #20Continuity of useful action

3Manufacturing precision

If emulsion polymerization is used to improve process control, then polymer structure control improves, but reactivity with water and surfactants causes particle aggregation and by-products

Engineering Contradiction:
Improvepolymer structure controlVSAvoidparticle aggregation
Core Design Contradiction:
Manufacturing precisionVSObject-generated harmful factors

Solution Approach 1:

The patent uses an intermediary approach by selecting and optimizing specific surfactant types and concentrations that mediate between the hydrophobic monomer/polymer and the aqueous phase. This carefully chosen intermediary prevents direct harmful reactions while maintaining emulsion stability and preventing particle aggregation, allowing structure control benefits to be realized.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent applies parameter changes by optimizing pH, ionic strength, surfactant concentration, and temperature to minimize reactivity between the 1,1-disubstituted alkene and water/surfactant components. By carefully controlling these parameters, the system achieves good polymer structure control while suppressing harmful side reactions and aggregation.

Inventive Principle:
Principle #35Parameter changes

4Productivity

If bulk polymerization is used for manufacturing large quantities, then production scale increases, but heat transport issues and shear heat generation occur

Engineering Contradiction:
Improvemanufacturing scaleVSAvoidheat transport
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The patent applies segmentation to large-scale manufacturing by dividing the total monomer charge into multiple staged additions. This allows the reaction heat to be generated and removed in manageable increments rather than all at once, solving heat transport issues while maintaining high overall production throughput through efficient use of reactor capacity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent employs dynamic control of large-scale polymerization by adjusting addition rates, agitation speeds, and temperature setpoints based on real-time reaction conditions. This dynamic optimization allows efficient heat management in large reactors while maintaining high productivity through maximized reactor utilization.

Inventive Principle:
Principle #15Dynamics

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 process enables the production of polymers with improved molecular weight control, reduced polydispersity, and controlled viscosity, facilitating the production of high-quality emulsions suitable for applications like paints and coatings, with the ability to scale up to larger reactors and higher throughput.

Implementation Method 1

reacting an activator with at least one of the first monomers in the micelle for initiating the anionic polymerization of the one or more first monomers

Methodology Applied
Scientific EffectAnionic polymerization: Chemical Bonding

Implementation Method 2

agitating a mixture comprising: 25 weight percent or more of a carrier liquid, a surfactant, and one or more first monomers to form micelles of the one or more monomers in the carrier liquid

Methodology Applied
Scientific EffectSurfactant action: Surfactant

Data Source

PatentEP3191546B1Emulsion polymers including one or more 1,1-disubstituted alkene compounds, emulsion methods, and polymer compositions
Publication Date: 2020.07.22 SIRRUS
  • EP3191546B1 patent drawingFigure 1~2
  • EP3191546B1 patent drawingFigure 3A~3B
  • EP3191546B1 patent drawingFigure 4

AI summary

The present teachings show that it is possible to polymerize 1,1-disubstituted alkene compounds in an emulsion (for example using a water based carrier liquid), despite the possible reactions between the monomer and water. Polymerization of 1,1-disubstituted alkene compounds in an emulsion provides opportunities to better control the polymerization compared with bulk polymerization. The emulsion polymerization techniques can be employed for preparing homopolymers, copolymers (e.g., random copolymers), and block copolymers.