Planetary Roller Extruder Bulk Polymerization Heat Management

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Solution Overview

Problem

Conventional bulk polymerization processes for producing adhesives face challenges with heat transfer at high conversion rates, leading to runaway reactions and increased processing costs due to fouling of heat transfer surfaces and the need for additional steps like de-volatilization to remove excess monomer.

Innovation Solution

A continuous bulk polymerization process using a recirculation tubular loop reactor system with a planetary roller extruder (PRE) and plug flow reactor, which maintains effective heat exchange and mixing through intermeshed spindles and controlled temperature, allowing for high conversion rates without fouling and reducing the need for additional processing steps.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional bulk polymerization processes are used at high conversion rates, then productivity is improved, but heat transfer efficiency deteriorates due to fouling of heat transfer surfaces

Engineering Contradiction:
Improveconversion rateVSAvoidheat transfer efficiency
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The reaction system is segmented into discrete droplets dispersed in a continuous phase, creating numerous small reaction zones rather than a single bulk reaction. This segmentation prevents fouling of heat transfer surfaces by distributing the exothermic reaction throughout the continuous phase, maintaining effective heat transfer even at high conversion rates

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A continuous phase acts as an intermediary medium between the reacting droplets and the heat transfer surfaces. This intermediary phase absorbs and transports heat away from the reaction sites, preventing direct contact between the reacting mixture and heat transfer surfaces, thereby eliminating fouling while maintaining thermal control

Inventive Principle:
Principle #24Intermediary (Mediator)

2Reliability

If conventional bulk polymerization is used at low conversion rates to maintain heat transfer efficiency, then heat transfer reliability is improved, but productivity deteriorates and additional processing steps are required

Engineering Contradiction:
Improveheat transfer efficiencyVSAvoidconversion rate
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

By segmenting the reaction into dispersed droplets, the system achieves both high conversion and effective heat transfer simultaneously. The segmentation allows the reaction to proceed to high conversion within each droplet while the continuous phase maintains efficient heat removal, eliminating the need to operate at low conversion rates

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The continuous phase continuously circulates through the reaction system, providing uninterrupted heat removal throughout the entire reaction process. This continuous action enables the system to maintain high conversion rates without the heat transfer efficiency deterioration that plagues conventional batch processes

Inventive Principle:
Principle #20Continuity of useful action

3Productivity

If high conversion rates are achieved in conventional processes, then productivity is improved, but additional processing steps are required to remove excess monomer

Engineering Contradiction:
Improveconversion rateVSAvoidnumber of processing steps
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The emulsion polymerization system inherently produces a stable dispersion of polymer particles in the continuous phase, with the surfactant system automatically preventing aggregation and controlling particle morphology. This self-stabilizing mechanism eliminates the need for additional processing steps to remove excess monomer or stabilize the product

Inventive Principle:
Principle #25Self-service

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 efficient polymerization of acrylic pressure-sensitive adhesives with high conversion rates, controlled heat management, and reduced processing costs by maintaining temperature below 240°C and achieving conversions of up to 99.5% with minimal residual monomer, resulting in polymers with desired molecular weights and polydispersity.

Implementation Method 1

maintains effective heat exchange and mixing through intermeshed spindles and controlled temperature

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 2

the free radical polymerization of the acrylate monomer, the di-vinyl monomer, and the hydroxyl functional acrylic monomer

Methodology Applied
Scientific EffectExothermic reaction: Exothermic Reaction

Implementation Method 3

maintains effective heat exchange and mixing through intermeshed spindles

Methodology Applied
Scientific EffectMixing: Stirring

Implementation Method 4

planetary roller extruder (PRE) and plug flow reactor

Methodology Applied
Scientific EffectCompression: Compression

Data Source

PatentUS9598518B2Continuous bulk polymerization of vinyl monomers
Publication Date: 2017.03.21 INTERTAPE POLYMER CORP
  • US9598518B2 patent drawing
  • US9598518B2 patent drawing
  • US9598518B2 patent drawing

AI summary

A method for continuous bulk polymerization is disclosed that includes providing a planetary roller extruder having a plurality of planetary roller zones, introducing an acrylate monomer, a di-vinyl monomer, and a hydroxyl functional acrylic monomer into the planetary roller extruder, introducing an initiator into the planetary roller extruder for initiation of a free-radical polymerization of the acrylate monomer, the di-vinyl monomer, and the hydroxyl functional acrylic monomer to form an acrylic polymer, maintaining the temperature of the free-radical polymerization in the planetary roller extruder below 240° C., and discharging a portion of the acrylic polymer from the planetary roller extruder, and returning the portion of the acrylic polymer to one or more of the plurality of planetary roller zones.