MIBK Solvent System for Methyl Pyridine Carboxylate Synthesis

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Solution Overview

Problem

Conventional methods for producing methyl 4-amino-3-chloro-6-(4-chloro-2-fluoro-3-methoxyphenyl)pyridine-2-carboxylate face challenges in yield and process complexity due to the use of multiple solvents and solvent exchanges, leading to losses of intermediate products.

Innovation Solution

The method involves using methyl isobutyl ketone (MIBK) as a solvent for extraction, Suzuki coupling, and deacetylation reactions, minimizing solvent exchanges and reducing the number of solvents required, thereby increasing yield and simplifying the production process.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If multiple solvents and solvent exchanges are used in conventional production methods, then the production process can proceed through different reaction stages, but the yield decreases and process complexity increases due to losses of intermediate products

Engineering Contradiction:
ImproveyieldVSAvoidprocess complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

MIBK serves multiple functions throughout the production process: it acts as the extraction solvent for isolating PBA from the aqueous reaction mixture, as the reaction solvent for the Suzuki coupling between PBA and methyl 4-(acetylamino)-3,6-dichloropyridine-2-carboxylate, and as the reaction solvent for the deacetylation step. This multi-functionality eliminates the need for solvent exchanges between stages, preventing intermediate product losses and simplifying the overall process while maintaining high yield

Inventive Principle:
Principle #6Universality (Multi-functionality)

Solution Approach 2:

The use of MIBK enables continuous operation without interruption for solvent removal and replacement. The intermediate products remain dissolved in MIBK throughout the extraction, coupling, and deacetylation steps, eliminating discontinuities associated with solvent exchanges and ensuring uninterrupted productive action throughout the synthesis sequence

Inventive Principle:
Principle #20Continuity of useful action

2Ease of manufacture

If multiple solvents are used for extraction, reaction, and deacetylation, then each reaction stage can be optimized, but the number of solvents and process steps increases

Engineering Contradiction:
Improveease of manufactureVSAvoidnumber of solvents
Core Design Contradiction:
Ease of manufactureVSQuantity of substance

Solution Approach 1:

MIBK is used as a universal solvent for all three major process stages: extraction of PBA from aqueous phase, Suzuki coupling reaction, and deacetylation reaction. This eliminates the need to use and switch between multiple different solvents (such as ethyl acetate for extraction, then acetonitrile or toluene for reaction, then another solvent for deacetylation), thereby reducing the quantity of substances handled and simplifying the manufacturing process

Inventive Principle:
Principle #6Universality (Multi-functionality)

Solution Approach 2:

The patent merges the functions of multiple separate solvent systems into a single continuous MIBK system. Instead of having separate extraction, reaction, and workup steps with different solvents, all operations are conducted in MIBK, combining multiple process functions into a unified solvent system that reduces the number of solvents required and simplifies the overall manufacturing procedure

Inventive Principle:
Principle #5Merging (Combining)

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 results in a higher yield of methyl 4-amino-3-chloro-6-(4-chloro-2-fluoro-3-methoxyphenyl)pyridine-2-carboxylate with reduced complexity and cost, as MIBK facilitates better partitioning of intermediates and eliminates the need for additional concentration or isolation steps.

Implementation Method 1

adding methyl isobutyl ketone to an aqueous solution comprising 4-chloro-2-fluoro-3-methoxyphenylboronic acid to form an organic phase comprising the 4-chloro-2-fluoro-3-methoxyphenylboronic acid and an aqueous phase. The organic phase and the aqueous phase are separated.

Methodology Applied
Scientific EffectLiquid-liquid extraction: Liquid-Liquid Extraction

Implementation Method 2

The 4-chloro-2-fluoro-3-methoxyphenylboronic acid is reacted with methyl 4-(acetylamino)-3,6-dichloropyridine-2-carboxylate in methyl isobutyl ketone to produce methyl 4-(acetylamino)-3-chloro-6-(4-chloro-2-fluoro-3-methoxyphenyl)pyridine-2-carboxylate

Methodology Applied
Scientific EffectSuzuki coupling reaction: Chemical Bonding

Implementation Method 3

which is deacetylated in the methyl isobutyl ketone to produce methyl 4-amino-3-chloro-6-(4-chloro-2-fluoro-3-methoxyphenyl)pyridine-2-carboxylate

Methodology Applied
Scientific EffectDeacetylation reaction: Chemical Bonding

Data Source

PatentEP2797890B1Methods of producing methyl 4-amino-3-chloro-6-(4-chloro-2-fluoro-3-methoxyphenyl)pyridine-2-carboxylate
Publication Date: 2016.10.05 DOW AGROSCIENCES LLC
  • EP2797890B1 patent drawing
  • EP2797890B1 patent drawing
  • EP2797890B1 patent drawing

AI summary

Methods of producing methyl 4-amino-3-chloro-6-(4-chloro-2-fluoro-3-methoxyphenyl)pyridine-2-carboxylate. One method comprises adding methyl isobutyl ketone to an aqueous solution comprising 4-chloro-2-fluoro-3-methoxyphenyl boronic acid to form an organic phase comprising the 4-chloro-2-fluoro-3-methoxyphenylboronic acid and an aqueous phase. The organic phase and the aqueous phase are separated. The 4-chloro-2-fluoro-3-methoxyphenylboronic acid is reacted with methyl 4-(acetylamino)-3,6-dichloropyridine-2-carboxylate in methyl isobutyl ketone to produce methyl 4-(acetylamino)-3-chloro-6-(4-chloro-2-fluoro-3-methoxyphenyl)pyridine-2-carboxylate, which is deacetylated to produce methyl 4-amino-3-chloro-6-(4-chloro-2-fluoro-3-methoxyphenyl)pyridine-2-carboxylate.