Poly(Pentabromobenzyl Acrylate) Composition for Molecular Weight Control

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Solution Overview

Problem

Current methods for polymerizing pentabromobenzyl acrylate to produce poly(pentabromobenzyl acrylate) as a flame retardant face challenges in achieving high yields and controlling molecular weight, particularly in solution polymerization processes that require careful solvent selection and often result in polymers with high polydispersity and high glass transition temperatures.

Innovation Solution

The process involves polymerizing pentabromobenzyl acrylate in a mixture of water-miscible aprotic solvents and water, using a water-soluble free radical initiator and optionally a chain length regulator, which allows for faster reaction completion and control over molecular weight, resulting in polymers with narrow molecular weight distribution and lower glass transition temperatures.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If solution polymerization is performed in traditional aprotic solvents, then polymerization can proceed, but reaction yield is limited to not more than 80% and molecular weight control is difficult

Engineering Contradiction:
Improvereaction yieldVSAvoidmolecular weight control
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent changes the solvent system from traditional aprotic solvents to an aqueous system containing water-miscible aprotic solvents. This parameter change enables reaction yields exceeding 80% and allows effective molecular weight control through the use of chain length regulators in the aqueous medium, resolving both the productivity and manufacturing precision issues.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces water-miscible aprotic solvents as intermediaries that bridge the compatibility between water-based systems and organic monomer polymerization. These solvents enable the monomer to polymerize effectively in an aqueous environment while allowing control over polymerization kinetics and molecular weight through water-soluble chain length regulators.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If polymerization is performed in anhydrous aprotic solvents, then reaction can proceed, but reaction time is extended and molecular weight distribution is broad

Engineering Contradiction:
Improvereaction speedVSAvoidmolecular weight distribution
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent changes from anhydrous conditions to aqueous conditions by introducing water into the aprotic solvent system. This parameter change accelerates the polymerization reaction and, when combined with water-soluble chain length regulators, produces polymers with narrow molecular weight distributions, simultaneously improving both productivity and manufacturing precision.

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If chain length regulators are used to control molecular weight, then molecular weight can be adjusted, but polydispersity increases in traditional solvent systems

Engineering Contradiction:
Improvemolecular weight controlVSAvoidpolydispersity
Core Design Contradiction:
Manufacturing precisionVSStability of the object's composition

Solution Approach 1:

The patent uses water-miscible aprotic solvents as intermediaries that enable chain length regulators to function more effectively. In this aqueous-compatible solvent system, chain length regulators achieve molecular weight control while maintaining narrow polydispersity indices (2-10), unlike traditional aprotic solvents where the same regulators increase polydispersity.

Inventive Principle:
Principle #24Intermediary (Mediator)

4Productivity

If bulk polymerization is performed at high temperature, then polymerization completes quickly, but polymer exhibits high glass transition temperature and reduced processability

Engineering Contradiction:
Improvepolymerization speedVSAvoidglass transition temperature
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The patent changes the solvent environment from bulk to aqueous solution, which fundamentally alters the polymerization kinetics and polymer properties. The aqueous environment with water-miscible aprotic solvents enables fast polymerization while producing polymers with lower glass transition temperatures (20-150°C), improving processability without sacrificing productivity.

Inventive Principle:
Principle #35Parameter changes

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 yields poly(pentabromobenzyl acrylate) with controlled molecular weight and thermal stability, effectively reducing flammability in materials such as polypropylene and styrene-containing polymers, while also reducing the amount of bromine and synergist required for flame retardancy, meeting stringent UL 94 ratings.

Implementation Method 1

polymerizing a monomer of the formula: [PBBMA] in a mixture of water-miscible aprotic solvent and water, in the presence of a free radical initiator

Methodology Applied
Scientific EffectFree radical polymerization: Chemical Bonding

Data Source

PatentUS9493584B2Poly (pentabromobenzyl acrylate) having specific properties
Publication Date: 2016.11.15 BROMINE COMPOUNDS
  • US9493584B2 patent drawing
  • US9493584B2 patent drawing
  • US9493584B2 patent drawing

AI summary

Poly (pentabromobenzyl acrylate) having weight average molecular weight (Mw) in the range from 4,000 to 120,000 and polydispersity index of less than 10 as determined by high temperature gel permeation chromatography, wherein the glass transition temperature of the poly (pentabromobenzyl acrylate) is not more than 150 C.°, the poly (pentabromobenzyl acrylate) includes chains which are terminated by an end group derived from a chain length regulator, wherein the end group is a thiol group —SR1, and wherein R1, is a linear or branched alkyl group composed of not less than 8 carbon atom.