High Assay Decabromodiphenylethane Bromination Process

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Solution Overview

Problem

Current processes for producing decabromodiphenylethane result in inconsistent bromine content, often below 99.0 GC area percent, due to variations in reaction conditions and the presence of lower brominated impurities, which fails to meet stringent regulatory requirements and user demands for high-purity perbrominated flame retardants.

Innovation Solution

A commercially feasible process involving batch bromination of diphenylethane or partially brominated diphenylethane in a reaction mixture with excess liquid bromine and an aluminum-based Lewis acid catalyst, conducted at temperatures of at least 60°C for most of the reaction time, with a minimum feed time of two hours and sufficient pressure to maintain bromine in the liquid state, and using a high concentration of aluminum-based catalyst to achieve high assay decabromodiphenylethane production.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If standard batch bromination processes are used, then production is commercially feasible, but the bromine content varies and often falls below 99.0 GC area percent

Engineering Contradiction:
Improvebromine content consistencyVSAvoidregulatory compliance
Core Design Contradiction:
Manufacturing precisionVSReliability

Solution Approach 1:

The patent applies parameter changes by optimizing reaction temperature (maintaining 60-80°C), bromine-to-diphenylethane molar ratio (excess bromine), catalyst concentration (0.5-5% aluminum-based catalyst), and feed rate control (minimum 2 hours) to achieve consistent high-purity products meeting regulatory standards

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements feedback control through GC analysis of product batches to monitor bromine content, allowing adjustment of process parameters to maintain consistent 99.0%+ purity and ensure regulatory compliance

Inventive Principle:
Principle #23Feedback

2Ease of manufacture

If lower brominated impurities are present to meet production efficiency, then manufacturing is easier, but purity decreases below user requirements

Engineering Contradiction:
Improveproduction efficiencyVSAvoidpurity of decabromodiphenylethane
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent applies preliminary action by conducting the bromination reaction under optimized conditions from the start (excess bromine, controlled temperature, adequate reaction time) to prevent formation of lower brominated impurities, eliminating the need for subsequent purification steps

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent ensures continuous useful action by maintaining reaction conditions (temperature 60-80°C, excess bromine presence, continuous stirring) throughout the minimum 2-hour feed period to ensure complete bromination and prevent impurity formation

Inventive Principle:
Principle #20Continuity of useful action

3Productivity

If reaction time is reduced to increase productivity, then output increases, but assay consistency decreases

Engineering Contradiction:
Improveproduction outputVSAvoidassay consistency
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent applies dynamics by optimizing the balance between feed rate and reaction time, using a minimum 2-hour feed period with controlled addition rates to ensure complete reaction while maintaining productivity through efficient process design

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 consistently produces decabromodiphenylethane with at least 99.0 GC area percent, ensuring high purity and reducing the presence of nonabromodiphenylethane, thereby meeting regulatory standards and user expectations for high assay products.

Implementation Method 1

a reaction mixture with excess liquid bromine and an aluminum-based Lewis acid catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

conducted at temperatures of at least 60°C for most of the reaction time

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 3

with sufficient pressure to maintain bromine in the liquid state

Methodology Applied
Scientific EffectPressure Increase: Pressure Increase

Data Source

PatentEP2137118B1Preparation and provision of high assay decabromodiphenylethane
Publication Date: 2013.12.25 ALBEMARLE CORP

AI summary

High assay reaction-derived decabromodiphenylethane product is produced and provided. The process comprises feeding diphenylethane, a partially brominated diphenylethane, or both subsurface into the liquid phase of a reaction mixture formed from components comprising excess liquid bromine and aluminum-based Lewis acid bromination catalyst. The temperature of the reaction mixture, the catalyst concentration in the excess bromine in the reaction mixture, and the feed time are coordinated in the processes to produce high assay reaction-derived decabromodiphenylethane product. Ways of effecting such coordination are described.