Mono Vinyl Ether Production via Transesterification Separation

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Solution Overview

Problem

Existing methods for producing vinyl ethers, such as the Reppe process, face challenges with high viscosity and gel formation at high conversions, leading to inefficient separation and residual products, requiring termination at lower conversions and complex distillation processes.

Innovation Solution

A process involving the reaction of a mono hydroxy compound with acetylene in the presence of a catalyst, followed by addition of an ester for transesterification, allowing for easy separation and purification of the mono vinyl ether through distillation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of time

If the reaction is terminated at lower conversions of the alcohol, then the viscosity increases significantly and gel formation occurs, but the residence time is reduced and polymer formation is minimized

Engineering Contradiction:
Improveresidence timeVSAvoidviscosity increase and gel formation
Core Design Contradiction:
Loss of timeVSObject-generated harmful factors

Solution Approach 1:

The harmful by-products (polymer and residual products) are removed by extraction using a suitable solvent, separating them from the desired vinyl ether product. This allows the reaction to be terminated at lower conversions without the harmful effects accumulating in the final product

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The conversion level is optimized to a specific range (70-90%) where the balance between residence time and harmful by-product formation is achieved. This parameter change prevents excessive viscosity increase and gel formation while maintaining economical production time

Inventive Principle:
Principle #35Parameter changes

2Productivity

If the reaction is terminated at lower conversions of the alcohol, then the residence time is reduced, but the separation of vinyl ether from unconverted alcohol becomes more difficult

Engineering Contradiction:
Improveproduction efficiencyVSAvoidseparation difficulty
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

A separating agent is introduced as an intermediary substance to facilitate the separation of vinyl ether from the reaction mixture. This agent enables efficient separation even when the conversion is at optimized levels (70-90%), solving the contradiction between productivity and ease of manufacture

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The separating agent extracts the vinyl ether from the reaction mixture, allowing for easy separation from unconverted alcohol. This extraction process makes the separation step straightforward despite the optimized conversion level

Inventive Principle:
Principle #2Taking out (Extraction)

3Ease of manufacture

If a two-step distillation process is used, then the vinyl ether can be separated from the mixture, but the process complexity increases due to azeotrope formation

Engineering Contradiction:
Improveseparation capabilityVSAvoiddistillation process complexity
Core Design Contradiction:
Ease of manufactureVSDevice complexity

Solution Approach 1:

A separating agent is used as an intermediary to simplify the separation process. This agent enables separation without requiring complex two-step distillation, reducing device complexity while maintaining separation capability

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The complex mechanical distillation system is replaced with a chemical separation method using a separating agent. This substitution eliminates the need for multiple distillation columns and azeotrope handling, significantly reducing process complexity

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

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 enables efficient and economic production of mono vinyl ethers with high yields, avoiding complex distillation procedures and achieving low unconverted alcohol levels.

Implementation Method 1

reacting a mono hydroxy compound of formula II R-OH wherein R has the above meaning with acetylene in presence of a catalyst to get a product mixture comprising the mono vinyl ether

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

reacting the remaining mono hydroxy compound R -OH with the ester in the presence of the catalyst to get a transesterification product comprising at least one ester group of formula IV R-O 2 C- and an alcohol of formula V X-OH

Methodology Applied
Scientific EffectTransesterification: Chemical Bonding

Implementation Method 3

isolating the mono vinyl ether from the product mixture obtained after process step b), optionally followed by purification of the mono vinyl ether by distillation

Methodology Applied
Scientific EffectDistillation: Distillation

Data Source

PatentEP3844138B1Process to produce a mono vinyl ether
Publication Date: 2023.03.01 BASF SE

AI summary

A process to produce a mono vinylether of formula (I) R-O-CH=CH2 wherein R represents an organic group with at least three carbon atoms comprising a) reacting a mono hydroxy compound of formula (II) R-OH wherein R has the above meaning with acetylene in presence of a catalyst to get a product mixture comprising the mono vinyl ether, unconverted mono hydroxy compound and the catalyst b) adding an ester comprising at least one ester group of formula (III) X-O2 C- wherein X is a hydrocarbon group comprising less carbon atoms than R to the product mixture obtained in process step a) and reacting the remaining mono hydroxy compound R-OH with the ester in the presence of the catalyst to get a transesterification product comprising at least one ester group of formula (IV) R-O2C- and an alcohol of formula (V) X-OH wherein R and X have the above meaning and c) isolating the mono vinyl ether from the product mixture obtained after process step b), optionally followed by purification of the mono vinyl ether by distillation.