Continuous Polymer Synthesis with Inverse Initiator Flow Control

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Solution Overview

Problem

Conventional polymer synthesis processes face inefficiencies due to batch reactor limitations, where reactants and products cannot be continuously fed and discharged, and struggle to produce polymers with specific molecular weights, which is crucial for controlling polymer properties.

Innovation Solution

A molecular weight-adjustable polymer synthesis process that continuously feeds gaseous monomers, surfactants, and initiators, with the initiator flow rate inversely proportional to the polymer's molecular weight, allowing for simultaneous and continuous reaction and product discharge, and uses liquid-gas separation and centrifugation for purification.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If a batch reactor is used for polymer synthesis, then monomer conversion rate is excellent, but production efficiency is low because reactants cannot be continuously fed and products cannot be continuously discharged

Engineering Contradiction:
Improveproduction efficiencyVSAvoidreaction time
Core Design Contradiction:
ProductivityVSLoss of time

Solution Approach 1:

The patent applies continuous flow reactor technology to replace batch reactors, enabling continuous feeding of monomers and initiators and continuous discharge of polymer products. This continuous operation eliminates idle time between batches and maintains constant reaction conditions, thereby significantly improving production efficiency while reducing overall reaction time

Inventive Principle:
Principle #20Continuity of useful action

Solution Approach 2:

The patent uses adjustable flow rates for feeding monomers and initiators in the continuous reactor system. By dynamically controlling the flow rates, the system can optimize reaction conditions and productivity while maintaining excellent monomer conversion rates, resolving the contradiction between production efficiency and reaction time

Inventive Principle:
Principle #15Dynamics

2Manufacturing precision

If conventional polymer synthesis is performed, then polymer is produced, but molecular weight control is difficult due to chain reaction characteristics

Engineering Contradiction:
Improvemolecular weight controlVSAvoidprocess complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent employs parameter control in continuous flow reactors, specifically controlling the flow rates of monomers and initiators, temperature, and pressure to precisely regulate polymer molecular weight. The continuous flow system allows for stable and reproducible parameter control, achieving desired molecular weight precision without excessive process complexity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements online monitoring and feedback control of reaction parameters in the continuous flow system. By continuously monitoring molecular weight and adjusting feed rates accordingly, the system achieves precise molecular weight control while maintaining manageable process complexity through automated feedback mechanisms

Inventive Principle:
Principle #23Feedback

Data Source

PatentUS20230100403A1Process for polymerizing molecular-weight controlled polymer
Publication Date: 2023.03.30 KOREA RES INST OF CHEM TECH
  • US20230100403A1 patent drawing
  • US20230100403A1 patent drawing
  • US20230100403A1 patent drawing

AI summary

According to an embodiment of the present invention, provided is a process for polymerizing molecular weight—adjustable polymer, comprising: a reactant supply step of supplying a gaseous monomer, a surfactant, and an initiator; a polymerization reaction step of performing a polymerization reaction in which the monomer, the surfactant, and the initiator participate; and a product discharging step of discharging the polymer compound produced by the polymerization reaction, wherein the flow rate of the supplied initiator is inversely proportional to the molecular weight of the polymer compound, and the molecular weight of the polymer compound produced by the polymerization reaction is adjusted by controlling the flow rate of the initiator.