Perfluoro(2-methylene-4-methyl-1,3-dioxolane) Production via Aqueous Decarboxylation

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Solution Overview

Problem

Current methods for producing perfluoro(2-methylene-4-methyl-1,3-dioxolane face challenges such as high temperature requirements, generation of toxic by-products, difficulty in scaling up industrial production, and issues with separating the target product from by-products like 2-hydro-perfluoro(2,4-dimethyl-1,3-dioxolane).

Innovation Solution

A method involving the reaction of perfluoro(2,4-dimethyl-2-fluoroformyl-1,3-dioxolane) with a basic aqueous solution containing alkali or alkaline earth metal ions, followed by liquid separation and water content reduction treatments, to facilitate a decarboxylation reaction in a liquid phase system, thereby producing perfluoro(2-methylene-4-methyl-1,3-dioxolane with high yield and minimal by-product formation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If a reaction at high temperature of 295°C is performed using perfluoro(2,4-dimethyl-2-fluoroformyl-1,3-dioxolane) on a sodium carbonate solid catalyst, then the decarboxylation reaction proceeds, but highly toxic fluorophosgenes are generated as by-products and the method is difficult to perform on an industrial scale

Engineering Contradiction:
Improvedecarboxylation reaction efficiencyVSAvoidtoxic fluorophosgene by-products
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent changes the temperature parameter from high temperature (295°C) to moderate temperature (130°C or lower), and changes the catalyst phase from solid to aqueous solution, thereby eliminating toxic fluorophosgene by-products while maintaining reaction efficiency

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces an aqueous solution of alkali metal carbonate or alkaline earth metal carbonate as an intermediary medium to facilitate the decarboxylation reaction at lower temperatures without generating toxic by-products, replacing the direct high-temperature solid-catalyst method

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If a decarboxylation reaction is performed at high temperature of 250°C to 280°C in a solid phase system using 2-methoxycarbonyl-2-trifluoromethyl-4-methyl-1,3-dioxolane fluorinated with fluorine gas, then the target compound is produced, but the method is difficult to perform on an industrial scale

Engineering Contradiction:
Improvetarget compound productionVSAvoidindustrial scalability
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The patent changes the reaction temperature from high temperature (250-280°C) to moderate temperature (130°C or lower), and changes the reaction phase from solid to liquid (aqueous solution), thereby improving industrial scalability while maintaining production efficiency

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent replaces the solid phase reaction system with a liquid phase (aqueous solution) system, making the process more suitable for industrial manufacturing by improving heat and mass transfer efficiency

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Temperature

If a decarboxylation reaction is performed at low temperature of 130°C in a liquid phase system using potassium perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylate and potassium fluoride, then the reaction temperature is reduced, but the target product is obtained as a mixture with 2-hydro-perfluoro(2,4-dimethyl-1,3-dioxolane) by-product that is very difficult to separate by distillation

Engineering Contradiction:
Improvereaction temperatureVSAvoidproduct separation difficulty
Core Design Contradiction:
TemperatureVSManufacturing precision

Solution Approach 1:

The patent optimizes the temperature parameter to be 130°C or lower (preferably 100-120°C) and changes the catalyst to alkali metal carbonate or alkaline earth metal carbonate in aqueous solution, thereby reducing the formation of hard-to-separate by-products while maintaining low temperature operation

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent converts the potential harm of low temperature reaction (by-product formation) into a benefit by selecting specific catalysts (alkali metal carbonate or alkaline earth metal carbonate) that promote selective decarboxylation, minimizing by-product formation and simplifying separation

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

4Productivity

If water content reduction treatments are performed on the liquid containing perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkali metal salts or perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkaline earth metal salts, then the decarboxylation reaction can be performed in a liquid phase system with high yield, but additional processing steps are required

Engineering Contradiction:
Improvedecarboxylation reaction yieldVSAvoidnumber of processing steps
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent performs water content reduction treatments (evaporation or adsorption) on the aqueous solution before decarboxylation to ensure high reaction yield, maintaining continuous improvement of product quality through sequential processing steps

Inventive Principle:
Principle #20Continuity of useful action

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 allows for industrial-scale production of perfluoro(2-methylene-4-methyl-1,3-dioxolane with high yield and reduced by-product formation, specifically minimizing the production of 2-hydro-perfluoro(2,4-dimethyl-1,3-dioxolane, making the process more feasible and efficient.

Implementation Method 1

reacting at least one of perfluoro(2,4-dimethyl-2-fluoroformyl-1,3-dioxolane) and a hydrolysis product thereof with a basic aqueous solution

Methodology Applied
Scientific EffectHydrolysis: Hydrolysis

Implementation Method 2

reacting with a basic aqueous solution containing one or more cations selected from the group consisting of alkali metal ions and alkaline earth metal ions

Methodology Applied
Scientific EffectNeutralization: Redox Reactions

Implementation Method 3

separating a liquid containing produced perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkali metal salts or perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkaline earth metal salts by a liquid separation operation

Methodology Applied
Scientific EffectLiquid separation: Liquid-Liquid Extraction

Implementation Method 4

performing one or more water content reduction treatments selected from the group consisting of water evaporation and water adsorption

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 5

performing one or more water content reduction treatments selected from the group consisting of water evaporation and water adsorption

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 6

causing a decarboxylation reaction in a liquid phase system with the obtained perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkali metal salts or perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkaline earth metal salts

Methodology Applied
Scientific EffectDecarboxylation: Decomposition (biological)

Implementation Method 7

thermally decomposed

Methodology Applied
Scientific EffectThermal decomposition: Thermolysis

Data Source

PatentEP3878845B1Perfluoro(2-methylene-4-methyl-1,3-dioxolane) production method
Publication Date: 2023.06.21 TOSOH CORP
  • EP3878845B1 patent drawing
  • EP3878845B1 patent drawing
  • EP3878845B1 patent drawing

AI summary

Provided is a method of producing perfluoro(2-methylene-4-methyl-1,3-dioxolane), the method including at least following processes (1) to (3): (1) reacting at least one of perfluoro(2,4-dimethyl-2-fluoroformyl-1,3-dioxolane) and a hydrolysis product thereof with a basic aqueous solution containing one or more cations selected from the group consisting of alkali metal ions and alkaline earth metal ions and then separating a liquid containing produced perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkali metal salts or perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkaline earth metal salts by a liquid separation operation; (2) performing one or more water content reduction treatments selected from the group consisting of water evaporation and water adsorption on the liquid containing the obtained perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkali metal salts or perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkaline earth metal salts to obtain perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkali metal salts or perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkaline earth metal salts in a solution state or a solid state; and (3) causing a decarboxylation reaction in a liquid phase system with the obtained perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkali metal salts or perfluoro(2,4-dimethyl-1,3-dioxolane-2-yl)carboxylic acid alkaline earth metal salts in a solution state or a solid state to produce perfluoro(2-methylene-4-methyl-1,3-dioxolane).