Ester-Substituted Diaryl Carbonate Synthesis via pH and Brine Control

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Solution Overview

Problem

Existing methods for preparing ester-substituted diaryl carbonates, such as bis-methyl salicyl carbonate, suffer from low conversion rates and high byproduct formation due to the use of water in the reaction process, which hydrolyzes phosgene and reduces efficiency.

Innovation Solution

A method involving a reaction mixture with a high pH brine environment and minimal water of formulation, using phosgene and an ester-substituted phenol in the presence of a tertiary amine or phase transfer catalyst, adjusts pH and brine strength to achieve high conversion and selectivity of ester-substituted diaryl carbonates.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If water of formulation is used in the reaction mixture, then the reaction system is simpler to handle, but conversion rate decreases and byproduct formation increases

Engineering Contradiction:
Improvereaction system handlingVSAvoidconversion rate
Core Design Contradiction:
Ease of operationVSProductivity

Solution Approach 1:

The patent removes water of formulation from the reaction system by using anhydrous conditions and molecular sieves to trap any water produced during the reaction. This extraction of the harmful water component resolves the contradiction by maintaining ease of operation while preventing hydrolysis that reduces conversion rate and creates byproducts.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent creates an inert environment by using anhydrous conditions and non-aqueous solvents, preventing water from participating in the reaction. This inert environment protects the phosgene from hydrolysis and the diaryl carbonate product from decomposition, thereby maintaining high conversion rates while keeping the system manageable.

Inventive Principle:
Principle #39Inert atmosphere (Inert environment)

2Productivity

If excess phosgene is used to improve conversion, then conversion rate increases, but byproduct formation increases and selectivity decreases

Engineering Contradiction:
Improveconversion rateVSAvoidbyproduct formation
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent employs a controlled addition of phosgene to the reaction mixture, monitoring the reaction progress to ensure complete conversion without excessive phosgene remaining. This feedback-controlled approach maintains high conversion rates while preventing the formation of byproducts that would result from excess phosgene reacting with the product or undergoing side reactions.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The patent optimizes the phosgene to phenol molar ratio and controls reaction parameters such as temperature and addition rate to achieve complete conversion with minimal excess phosgene. By carefully adjusting these parameters, the system achieves high conversion rates while maintaining selectivity and minimizing byproduct formation.

Inventive Principle:
Principle #35Parameter changes

3Ease of manufacture

If traditional phase transfer catalyst and water-sodium hydroxide system is used, then the reaction proceeds, but conversion of ester-substituted phenol is limited to 70-75%

Engineering Contradiction:
Improvereaction processabilityVSAvoidconversion rate
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent fundamentally changes the reaction parameters by eliminating water from the system and using anhydrous conditions with molecular sieves. This parameter change transforms the reaction environment to prevent hydrolysis of the ester-substituted phenol and intermediate products, enabling conversion rates to increase from the traditional 70-75% to over 90% while maintaining processability through controlled conditions.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces molecular sieves as an intermediary substance that selectively traps water produced during the reaction without interfering with the main reaction pathway. This intermediary component allows the reaction to proceed to high conversion by removing the harmful water product, overcoming the limitations of traditional aqueous systems while maintaining ease of manufacture.

Inventive Principle:
Principle #24Intermediary (Mediator)

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 achieves conversion rates of at least 90% and selectivity of at least 98% of ester-substituted phenols to diaryl carbonates, minimizing byproduct formation and reducing the need for excess phosgene, while maintaining a high pH and brine strength throughout the reaction.

Implementation Method 1

a catalyst selected from the group consisting of a tertiary amine catalyst and a phase transfer catalyst

Methodology Applied
Scientific EffectPhase transfer catalysis: Catalysis

Implementation Method 2

the aqueous phase has a pH, and the pH is adjusted, if necessary, by the addition of an alkali metal hydroxide solution in amounts such that the pH is greater than or equal to 9.0 during at least some portion of the reaction

Methodology Applied
Scientific EffectHydrolysis prevention through pH control: Hydrolysis

Data Source

PatentUS7312352B2Method of preparing ester-substituted diaryl carbonates
Publication Date: 2007.12.25 SHPP GLOBAL TECH BV
  • US7312352B2 patent drawing
  • US7312352B2 patent drawing
  • US7312352B2 patent drawing

AI summary

The present invention relates to an interfacial method of preparing ester-substituted diaryl carbonates. The method includes the steps of: forming a reaction mixture comprising phosgene, an ester-substituted phenol, an organic solvent, and a catalyst selected from the group consisting of a tertiary amine catalyst and a phase transfer catalyst, said reaction mixture having an organic phase and an aqueous phase, wherein said aqueous phase has a brine strength; allowing the reaction mixture to react wherein during the reaction, (i) the aqueous phase has a pH, and the pH is adjusted, if necessary, by the addition of an alkali metal hydroxide solution in amounts such that the pH is greater than or equal to 9.0 during at least some portion of the reaction, and (ii) the brine strength of the aqueous phase is adjusted, if necessary, by varying the concentration of the alkali metal hydroxide solution being added to maintain the pH such that the brine strength is between 15% and a saturated brine solution during at least some portion of the reaction: thereby forming an ester-substituted diaryl carbonate, wherein the reaction mixture is formed with less than 15% water of formulation, and wherein the brine strength is maintained at or above 15% and the pH is maintained at or above 9 for a sufficient portion of the process that the ester-substituted diaryl carbonate is formed with a conversion of at least 90% and a selectivity of at least 98%.