3,4′Diacetoxybenzophenone Synthesis via Segmented Catalysis

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Solution Overview

Problem

Current processes for producing 3,4′diacetoxybenzophenone are not efficient or economical, necessitating a more effective method for its synthesis.

Innovation Solution

A method involving the combination of m-hydroxybenzoic acid, phenol, a protonic acid, and a Lewis acid to form 3,4′dihydroxybenzophenone, followed by acetylation with an acetylating agent in the presence of an inorganic acid and activated carbon, while using specific temperature and pH controls to optimize yield and purity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional processes are used to produce 3,4′diacetoxybenzophenone, then production can proceed with existing methods, but efficiency and economy are insufficient

Engineering Contradiction:
Improveproduction efficiencyVSAvoidmanufacturing economy
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The production process is divided into distinct sequential stages: (a) condensation of m-hydroxybenzoic acid with phenol to form 3,4′dihydroxybenzophenone, (b) acetylation to form 3,4′diacetoxybenzophenone, and (c) purification. Each stage uses optimized conditions and specific catalysts to maximize efficiency and yield at that particular step, thereby improving overall productivity and economy.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The process employs specific parameter optimizations including temperature ranges (27-33°C for condensation), pressure conditions (at least 5 psig), pH control (4.5-6.0 during acetylation), and catalyst selection (protonic acid combined with Lewis acid). These parameter changes are carefully controlled to enhance reaction efficiency, yield, and economic feasibility while avoiding side reactions and minimizing waste.

Inventive Principle:
Principle #35Parameter changes

2Speed

If temperature and pressure are increased to accelerate reaction, then production speed increases, but energy consumption and safety risks increase

Engineering Contradiction:
Improvereaction rateVSAvoidenergy consumption
Core Design Contradiction:
SpeedVSUse of energy by moving object

Solution Approach 1:

The process uses moderate temperature (27-33°C) and pressure (at least 5 psig) conditions combined with efficient catalysis to achieve acceptable reaction rates without excessive energy input. The dual-catalyst system (protonic acid and Lewis acid) enables the reaction to proceed efficiently at these milder conditions, balancing speed with energy economy and safety.

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If multiple purification steps are added to increase product purity, then product quality improves, but process complexity and time increase

Engineering Contradiction:
Improveproduct purityVSAvoidprocess complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The purification process selectively removes catalysts and impurities through extraction with water followed by filtration. This targeted removal of specific contaminants (protonic acid, Lewis acid, and colored impurities) achieves high product purity without requiring multiple complex purification stages, thereby maintaining process simplicity while ensuring quality.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

Activated carbon is used during the acetylation step to adsorb colored impurities and other contaminants from the reaction mixture. This porous material provides effective purification through adsorption, simplifying the overall purification process while achieving high product purity and eliminating the need for more complex purification equipment.

Inventive Principle:
Principle #31Porous materials

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 method achieves a high yield of purified 3,4′diacetoxybenzophenone with improved efficiency and economy, suitable for applications in liquid crystal polyester polymers, with yields exceeding 80% and high purity.

Implementation Method 1

combining m-hydroxybenzoic acid, phenol, a protonic acid and a Lewis acid to form a mixture, heating an agitated mixture of step (a) to a temperature in a range of 27-33° C. and a pressure of at least 5 psig to form a reaction product of 3,4′dihydroxybenzophenone

Methodology Applied
Scientific EffectCondensation reaction: Chemical Bonding

Implementation Method 2

reacting 3,4′dihydroxybenzophenone with an acetylating agent in the presence of an inorganic acid and activated carbon to form 3,4′diacetoxybenzophenone

Methodology Applied
Scientific EffectAcetylation reaction: Chemical Bonding

Implementation Method 3

reacting 3,4′dihydroxybenzophenone with an acetylating agent in the presence of an inorganic acid and activated carbon

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS20100217046A1Process for producing 3,4' diacetoxybenzophenone
Publication Date: 2010.08.26 DUPONT SAFETY & CONSTRUCTION INC

AI summary

A process for producing 3,4′diacetoxybenzophenone by first synthesizing 3,4′dihydroxybenzophenone by reacting meta-hydroxybenzoic acid and phenol in the presence of a Lewis acid, and a protonic acid followed by reacting the 3,4′dihydroxybenzophenone with an acetylating agent in the presence of an inorganic acid and activated carbon.