Fluoroalkyl Iodide Telomerization Selectivity via Segmented Reactors

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current methods for producing fluoroalkyl iodides through telomerization suffer from low selectivity and efficiency due to the production of by-products and consecutive reactions, which result in a mixture containing undesired fluoroalkyl iodides with more carbon atoms than intended.

Innovation Solution

A method involving two copper catalyst-containing reactors is used, where the first reactor produces a mixture of fluoroalkyl iodides with a specific degree of polymerization, and the second reactor further reacts the desired fluoroalkyl iodides with tetrafluoroethylene to enhance selectivity and reduce by-product formation, allowing for the independent adjustment of reaction times and product distribution.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If telomerization is conducted by consecutive reactions in a single reactor, then the production process is simple, but the selectivity of the desired fluoroalkyl iodide is low due to consecutive reactions producing higher polymerization products

Engineering Contradiction:
Improvereaction process complexityVSAvoidselectivity of desired fluoroalkyl iodide
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The single reactor system is segmented into two separate reactors. The first reactor performs the initial telomerization reaction to produce fluoroalkyl iodide with n=1 or 2, which is then separated and transferred to the second reactor for further reaction to produce the desired higher polymerization product. This segmentation prevents consecutive reactions from producing excessive higher polymerization products in a single reactor, thereby improving selectivity while maintaining reasonable process complexity.

Inventive Principle:
Principle #1Segmentation

2Productivity

If peroxide catalyst is used to promote the reaction, then the reaction rate is improved, but by-products represented by Rf-(CF2CF2)n-H are produced requiring additional removal steps

Engineering Contradiction:
Improvereaction rateVSAvoidby-product formation
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The catalyst type is changed from peroxide to copper catalyst. This parameter change in the catalytic system fundamentally alters the reaction pathway to eliminate by-product formation while maintaining acceptable reaction rates. The copper catalyst enables the telomerization reaction to proceed without producing the harmful by-products Rf-(CF2CF2)n-H that characterize peroxide-catalyzed reactions, thereby improving productivity by eliminating the need for by-product removal steps.

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If the reaction of 1-iodoperfluoroethane with tetrafluoroethylene is allowed to progress, then the desired fluoroalkyl iodide is produced, but the reaction rate is slow making it the rate-determining step

Engineering Contradiction:
Improveproduction of desired fluoroalkyl iodideVSAvoidreaction rate
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The reaction process is segmented into two stages across two reactors. The first reactor is dedicated to the slow rate-determining step of 1-iodoperfluoroethane reacting with tetrafluoroethylene to form intermediates with n=1 or 2. These intermediates are then separated and transferred to the second reactor where the faster reaction occurs to produce the desired higher polymerization products. This segmentation allows optimization of each stage independently, managing the slow initial reaction without compromising overall productivity.

Inventive Principle:
Principle #1Segmentation

4Manufacturing precision

If multiple reactors are used to improve selectivity, then the desired fluoroalkyl iodide is produced with high selectivity, but the device complexity increases

Engineering Contradiction:
Improveselectivity of desired fluoroalkyl iodideVSAvoidnumber of reactors and separation steps
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The system uses exactly two reactors with a separation unit, representing an optimized segmentation that balances complexity and selectivity. The first reactor produces intermediates that are separated and transferred to the second reactor for final product formation. This limited segmentation achieves high selectivity for the desired fluoroalkyl iodide with n≥2 without creating excessive device complexity, as opposed to using more reactors or more complex separation systems.

Inventive Principle:
Principle #1Segmentation

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 increases the selectivity of the desired fluoroalkyl iodides, such as 1-iodoperfluorohexane, by reducing the proportion of higher polymerization products and eliminating the need for by-product removal, thereby improving production efficiency.

Implementation Method 1

reacting a fluoroalkyl iodide represented by formula (II) with tetrafluoroethylene in the presence of a copper catalyst in a first reactor to obtain a first reaction mixture

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentEP2840075B1Method for producing mixture of fluoroalkyl iodides
Publication Date: 2017.11.15 DAIKIN INDUSTRIES LTD

AI summary

The present invention provides a novel method for producing a mixture of fluoroalkyl iodides with high production efficiency, the method enabling the production of a desired fluoroalkyl iodide with high selectivity. Specifically, the present invention provides a method for producing a mixture of fluoroalkyl iodides represented by formula (I):         Rf(CF2CF2)nI     (I) (wherein Rf represents a fluoroalkyl group having 1 to 10 carbon atoms, and n is an integer indicating a degree of polymerization), the degree of polymerization n being m or more (m is an integer of 2 or more) by telomerization in metal catalyst-containing reactors, the method including: (1) step 1 of reacting a fluoroalkyl iodide represented by formula (II):         RfI     (II) (wherein Rf is a fluoroalkyl group having 1 to 10 carbon atoms) with tetrafluoroethylene in the presence of a metal catalyst in a first reactor to obtain a first reaction mixture containing a mixture of fluoroalkyl iodides represented by formula (I) wherein the degree of polymerization n is 1 or more; (2) step 2 of separating the first reaction mixture withdrawn from the first reactor into a first fraction containing a fluoroalkyl iodide or a mixture of fluoroalkyl iodides represented by formula (I) wherein the degree of polymerization n is (m-2) or less, a fluoroalkyl iodide represented by formula (II), and tetrafluoroethylene, a second fraction containing a fluoroalkyl iodide represented by formula (I) wherein the degree of polymerization n is (m-1), and a third fraction containing a mixture of fluoroalkyl iodides represented by formula (I) wherein the degree of polymerization n is m or more; and (3) step 3 of transferring the second fraction into a second reactor in which a metal catalyst is present and reacting the second fraction with tetrafluoroethylene in the second reactor to obtain a second reaction mixture containing a mixture of fluoroalkyl iodides represented by formula (I) wherein the degree of polymerization n is m or more.