Extractive Distillation for 245cb Purification

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Solution Overview

Problem

Current processes for producing 2,3,3-tetrafluoro-1-propene face challenges in purifying 1,1,1,2,2-pentafluoropropane due to the presence of impurities with similar boiling points, leading to inefficient separation and product contamination.

Innovation Solution

A process involving selective operational conditions and the use of organic extractants like ethylamine or isopropylamine for extractive distillation to separate and recycle 1,1,1,2,2-pentafluoropropane from mixtures containing trans-1,3,3-tetrafluoro-1-propene and other impurities, allowing for the recovery of high-purity 2,3,3-tetrafluoro-1-propene.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If distillation is used to purify the reaction mixture, then separation of compounds is achieved, but separation efficiency is poor when compounds have similar boiling points or form azeotropic compositions

Engineering Contradiction:
Improvepurification efficiencyVSAvoidseparation effectiveness
Core Design Contradiction:
Manufacturing precisionVSReliability

Solution Approach 1:

The patent introduces an extractive distillation agent as an intermediary substance to facilitate the separation of compounds with similar boiling points. The agent selectively interacts with one component of the mixture, creating a temporary complex that changes the relative volatility between components, thereby enabling effective separation through distillation where it would otherwise fail due to azeotropic or near-azeotropic compositions.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent modifies the physical-chemical parameters of the mixture by introducing an extractive distillation agent that changes the volatility relationships between components. This parameter change allows the separation process to overcome the limitation of similar boiling points and azeotropic behavior, transforming an intractable separation problem into a solvable one.

Inventive Principle:
Principle #35Parameter changes

2Manufacturing precision

If extractive distillation processes are used to purify compounds with similar boiling points, then separation efficiency improves, but process complexity increases

Engineering Contradiction:
Improveseparation efficiencyVSAvoidprocess complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The extractive distillation agent serves as a mediator that simplifies the overall separation challenge into more manageable steps. By introducing this intermediary substance, the complex task of separating compounds with similar boiling points is broken down into selective complexation followed by straightforward distillation, reducing the inherent process complexity.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent employs a strategy where the extractive distillation agent is temporarily introduced to facilitate separation, then recovered and recycled. This approach allows the system to benefit from the enhanced separation capability while minimizing the permanent addition of process complexity, as the agent can be removed and reused.

Inventive Principle:
Principle #34Discarding and recovering

3Manufacturing precision

If impurities accumulate in the reactor, then reaction selectivity decreases, but continuous removal of impurities increases process complexity

Engineering Contradiction:
Improvereaction selectivityVSAvoidprocess complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent applies preliminary action by performing extractive distillation on the reaction mixture to remove impurities before they can accumulate and affect reaction selectivity. By proactively eliminating unwanted compounds from the system, the process maintains high selectivity without requiring continuous complex intervention during the reaction itself.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent extracts impurities from the reaction mixture using extractive distillation, removing them from the system before they can interfere with the main reaction. This extraction approach selectively isolates unwanted compounds while leaving the desired products intact, maintaining reaction selectivity without adding continuous complexity to the reaction process.

Inventive Principle:
Principle #2Taking out (Extraction)

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 effectively purifies 1,1,1,2,2-pentafluoropropane and promotes the production of 2,3,3-tetrafluoro-1-propene by efficiently separating and recycling the desired compounds, even in azeotropic or quasi-azeotropic compositions, thereby improving overall process efficiency.

Implementation Method 1

b) extractive distillation of said second composition to form: i) a third composition comprising said organic extraction agent, trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally said at least one of the compounds selected from the group consisting of 1,1-difluoroethane (152a), 1,1,1,2-tetrafluoroethane (134a), cis-1,3,3,3-tetrafluoro-1-propene (1234ze-Z), trans-1,2,3,3,3-pentafluoropropene (1225ye-E), cis-1,2,3,3,3-pentafluoropropene (1225ye-Z) and 3,3,3-trifluoropropene (1243zf)

Methodology Applied
Scientific EffectExtractive distillation: Distillation

Data Source

PatentEP3394018B1Method for producing 2,3,3,3-tetrafluoropropene and recycling 1,1,1,2,2-pentafluoropropane free of impurities
Publication Date: 2023.06.21 ARKEMA FRANCE SA
  • EP3394018B1 patent drawingFigure 1a
  • EP3394018B1 patent drawingFigure 1b
  • EP3394018B1 patent drawingFigure 1c

AI summary

The invention relates to a method for purifying 1,1,1,2,2-pentafluoropropane (245cb) using a first composition comprising 1,1,1,2,2-pentafluoropropane and at least one of the compounds selected from the group consisting of 1,1-difluoroethane (152a), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), cis-1,3,3,3-tetrafluoro-1-propene (1234ze-Z), trans-1,2,3,3,3-pentafluoropropene (1225ye-E), cis-1,2,3,3,3-10 pentafluoropropene (1225ye-Z) and 3,3,3-trifluoropropene (1243zf), said method comprising the steps of: a) bringing said first composition into contact with at least one organic extraction agent in order to form a second composition; b) extractive distillation of said second composition in order to form i) a third composition comprising said organic extraction agent and said at least one of the compounds selected from the group consisting of 1,1-difluoroethane (152a), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), cis-1,3,3,3-tetrafluoro-1-propene (1234ze-Z), trans-1,2,3,3,3- pentafluoropropene (1225ye-E), cis-1,2,3,3,3-pentafluoropropene (1225ye-Z) and 3,3,3- trifluoropropene(1243zf); and ii) a stream comprising the 1,1,1,2,2-pentafluoropropane; and c) recovery and separation of said third composition. The invention also relates to a method for producing 1234yf including the method for purifying 1,1,2,2-pentafluoropropane.