Azoxystrobin Synthesis Catalyst Reduction

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Solution Overview

Problem

Current methods for producing azoxystrobin require high amounts of the expensive catalyst 1,4-diazabicyclo[2.2.2]octane (DABCO), leading to increased costs and environmental concerns due to catalyst discharge in aqueous process effluent.

Innovation Solution

A process using between 0.1 and 2 mol% of DABCO to react 2-cyanophenol with methyl (E)-2-[2-(6-chloropyrimidin-4-yloxy)phenyl]-3-methoxyacrylate or its derivatives, significantly reducing catalyst usage while maintaining high yields.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If high amounts of DABCO catalyst are used in the reaction, then the reaction yield is improved, but the manufacturing cost increases and environmental harm worsens due to catalyst discharge

Engineering Contradiction:
Improvereaction yieldVSAvoidcatalyst discharge in aqueous process effluent
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent applies parameter changes by optimizing the catalyst concentration from the conventional high amount (40 mol% as per WO 01/727191) to a significantly reduced range of 0.1-2 mol%. This parameter modification maintains high reaction yields while dramatically reducing the amount of DABCO catalyst discharged into aqueous effluent, thereby resolving the contradiction between productivity and environmental harm.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If high amounts of DABCO catalyst are used, then the reaction proceeds efficiently, but the manufacturing cost increases due to the expensive catalyst

Engineering Contradiction:
Improvereaction efficiencyVSAvoidmanufacturing cost
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The patent resolves this contradiction by changing the catalyst concentration parameter from high (40 mol%) to low (0.1-2 mol%). This parameter optimization maintains sufficient reaction efficiency while dramatically reducing the quantity of expensive DABCO catalyst required, thereby lowering manufacturing costs without sacrificing productivity.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If conventional catalyst amounts (40 mol% DABCO) are used, then the reaction yield is high, but the quantity of catalyst discharged in aqueous process effluent increases

Engineering Contradiction:
Improvereaction yieldVSAvoidquantity of catalyst discharged
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent addresses this contradiction by modifying the catalyst concentration parameter from 40 mol% to 0.1-2 mol%. This change maintains high reaction yields while minimizing the absolute quantity of DABCO catalyst that ends up in aqueous process effluent, thereby reducing substance loss and environmental contamination.

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 significantly reduces the cost of azoxystrobin production and minimizes environmental impact by using less DABCO, achieving yields comparable to or exceeding those with higher catalyst concentrations.

Implementation Method 1

reacting 2-cyanophenol with methyl (E)-2-[2-(6-chloropyrimidin-4-yloxy)phenyl]-3-methoxyacrylate in the presence of between 0.1 and 2 mol % of 1,4-diazabicyclo[2.2.2]octane

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentEP2308825B1Process for the preparation of an intermediate for azoxystrobin
Publication Date: 2014.05.21 SYNGENTA IP
  • EP2308825B1 patent drawing
  • EP2308825B1 patent drawing
  • EP2308825B1 patent drawing

AI summary

The present invention relates to a process for preparing a compound of formula (IV) where W is the methyl (E)-2-(3-methoxy)acrylate group, which comprises the steps of: (i) reacting the compound of formula (IV) where W is the methyl 2-(3,3-dimethoxy)propanoate group with a reagent that will protect the hydroxyl group of that compound from reaction during subsequent demethanolysis; (ii) eliminating methanol from the hydroxyl-protected compound formed in step (i); and (iii) removing the hydroxyl-protecting group formed in step (i) to form a compound of formula (IV) where W is the methyl (E)-2-(3-methoxy)acrylate group.