Catalyst Recycling in Alkyl Methacrylate Transesterification

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Solution Overview

Problem

Existing continuous processes for preparing alkyl(meth)acrylates through transesterification are inefficient due to high catalyst consumption and costs, as well as issues with catalyst stability and reuse, leading to increased operational expenses and reduced product quality.

Innovation Solution

The process employs a homogeneous tetraalkyl titanate catalyst that can be repeatedly recycled, allowing for reduced auxiliary costs and maintaining product quality, using a liquid stream divider and pump to control catalyst recycling based on activity indicators such as alcohol and MMA conversion.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If a homogeneous tetraalkyl titanate catalyst is used in continuous transesterification, then the reaction efficiency and product quality are improved, but the catalyst consumption and operational costs increase due to inability to recycle

Engineering Contradiction:
Improvereaction efficiencyVSAvoidcatalyst consumption
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent implements a catalyst recovery system where the homogeneous tetraalkyl titanate catalyst is separated from the reaction mixture through a decanter after transesterification. The recovered catalyst is then recycled back to the reactor, eliminating continuous catalyst consumption while maintaining high reaction efficiency throughout the process

Inventive Principle:
Principle #34Discarding and recovering

Solution Approach 2:

The patent introduces a decanter as an intermediary separation device between the reactor and product processing units. This decanter enables phase separation of the homogeneous catalyst from the organic reaction mixture, allowing catalyst recovery and reuse without affecting product quality

Inventive Principle:
Principle #24Intermediary (Mediator)

2Loss of substance

If the catalyst is continuously recycled without separation, then catalyst consumption is reduced, but product purity deteriorates due to catalyst contamination

Engineering Contradiction:
Improvecatalyst consumptionVSAvoidproduct purity
Core Design Contradiction:
Loss of substanceVSManufacturing precision

Solution Approach 1:

The patent segments the continuous process into distinct functional units: reaction zone, separation zone (decanter), and recycling zone. This spatial segmentation ensures that catalyst separation occurs in a dedicated zone before product collection, preventing catalyst contamination while enabling continuous recycling

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent extracts the catalyst from the reaction mixture using a decanter that separates the homogeneous catalyst phase from the organic product phase. This extraction step removes the catalyst from the product stream, ensuring high product purity while allowing the extracted catalyst to be recycled

Inventive Principle:
Principle #2Taking out (Extraction)

3Productivity

If the catalyst is subjected to thermal stress during continuous operation, then the reaction rate is maintained, but catalyst stability and activity deteriorate over time

Engineering Contradiction:
Improvereaction rateVSAvoidcatalyst stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent implements periodic catalyst replacement in the continuous recycling system. After a certain operating period, the catalyst in the recycling loop is replaced with fresh catalyst, restoring full catalytic activity while maintaining continuous production. This periodic intervention counteracts the gradual deactivation caused by thermal stress

Inventive Principle:
Principle #19Periodic 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 approach significantly reduces auxiliary costs while maintaining high product quality and overall yields, with the catalyst retaining activity through thermal stress, enabling efficient and cost-effective production of alkyl(meth)acrylates.

Implementation Method 1

The mixture of starting materials (methyl(meth)acrylate and alcohol) is continuously fed to a stirred reactor together with a homogeneous tetraalkyl titanate transesterification catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

the conversion to the dialkylaminoalkyl(meth)acrylate is effected in the stirred reactor at a temperature of 90-120° C. while continuously removing the azeotropic methyl(meth)acrylate/methanol mixture

Methodology Applied
Scientific EffectDistillation: Distillation

Data Source

PatentUS8461375B2Method for the continuous production of alkyl(meth)acrylates with multiple catalyst recycling
Publication Date: 2013.06.11 EVONIK OPERATIONS GMBH
  • US8461375B2 patent drawing
  • US8461375B2 patent drawing
  • US8461375B2 patent drawing

AI summary

The invention relates to an improved method for the continuous production of alkyl(methyl)acrylates by transesterification of methyl(meth)acrylate with alcohols that are heavy in comparison with methanol. A special processing technique makes it possible to obtain new levels of product quality. Very high space-time-overall yields can also be obtained. The invention is characterized by the multiple use of a homogeneous catalyst which thereby reduces the costs of auxiliary agents significantly.