Azeotropic Distillation Separates HF from Fluoroolefins

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Solution Overview

Problem

The separation of hydrogen fluoride (HF) from fluoroolefins, such as 2,3,3,3-tetrafluoropropene (HFC-1234yf), is challenging due to the inefficiencies of existing methods like distillation and decantation, which often require large amounts of scrubbing solutions and result in excessive waste and wet products.

Innovation Solution

A process involving azeotropic distillation, where a mixture of HF and HFC-1234yf is fed to a distillation column, forming an azeotrope that condenses into two liquid phases, allowing for the recycling of enriched phases back into the column to separate and purify HF and HFC-1234yf, with optional use of an entrainer to enhance phase separation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If aqueous scrubbing is used to separate HF from fluoroolefins, then separation effectiveness is improved, but large amounts of scrubbing solutions are required and excessive waste is produced

Engineering Contradiction:
Improveseparation effectivenessVSAvoidscrubbing solution consumption and waste production
Core Design Contradiction:
ReliabilityVSLoss of substance

Solution Approach 1:

The invention utilizes phase transition of the azeotrope mixture into two liquid phases upon condensation. The distillate containing HF and fluoroolefin azeotrope is condensed to form an HF-rich liquid phase and a fluoroolefin-rich liquid phase, enabling separation without aqueous scrubbing solutions.

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The invention employs an azeotrope-forming compound as an intermediary substance. This compound forms a heterogeneous azeotrope with HF that separates into two liquid phases upon condensation, acting as a mediator to facilitate separation without requiring large amounts of scrubbing solutions.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Reliability

If conventional distillation is used to separate HF from fluoroolefins, then separation is attempted, but the method is very often ineffective

Engineering Contradiction:
Improveseparation effectivenessVSAvoidseparation efficiency
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The invention exploits the phase transition behavior of the azeotrope mixture. When the distillate is condensed, it automatically separates into two liquid phases with different compositions, enabling effective separation that conventional distillation cannot achieve alone.

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The invention changes the physical parameters of the system by condensing the vapor phase into liquid phase, which triggers phase separation. This parameter change from vapor to liquid state enables the separation mechanism that makes conventional distillation ineffective.

Inventive Principle:
Principle #35Parameter changes

3Reliability

If decantation is used to separate HF from fluoroolefins, then separation is attempted, but it requires large amounts of scrubbing solutions and produces wet product

Engineering Contradiction:
Improveseparation effectivenessVSAvoidscrubbing solution consumption
Core Design Contradiction:
ReliabilityVSLoss of substance

Solution Approach 1:

The invention uses phase transition to create two immiscible liquid phases upon condensation. The HF-rich phase and fluoroolefin-rich phase separate naturally, allowing decantation without requiring large amounts of scrubbing solutions and producing drier products.

Inventive Principle:
Principle #36Phase transitions

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 recovers HF and HFC-1234yf with reduced waste and energy consumption, improving the efficiency of separation and purification by leveraging the unique phase behavior of azeotropic mixtures.

Implementation Method 1

condensing the first distillate to form 2 liquid phases

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 2

condensing the first distillate to form 2 liquid phases, being i) an HF-rich phase and ii) an HFC-1234yf-rich phase

Methodology Applied
Scientific EffectPhase separation: Liquid-Liquid Extraction

Implementation Method 3

removing an azeotrope composition comprising HF and HFC-1234yf as a first distillate

Methodology Applied
Scientific EffectAzeotropic distillation: Distillation

Data Source

PatentEP2247561B1Processes for separation of 2,3,3,3-tetrafluoropropene from hydrogen fluoride by azeotropic distillation
Publication Date: 2014.03.26 EI DU PONT DE NEMOURS & CO
  • EP2247561B1 patent drawingFigure 1
  • EP2247561B1 patent drawingFigure 2
  • EP2247561B1 patent drawingFigure 3

AI summary

Disclosed herein are processes for separation of 2,3,3,3-tetrafluoropropene and hydrogen fluoride using azeotropic distillation. Additionally, disclosed are processes for separating mixtures of 2,3,3,3-tetrafluoropropene, hydrogen fluoride and 1,1,1,2,3-pentafluoropropane (HFC-245eb) and/or 1,1,1,2,2-pentafluoropropane (HFC-245cb) by azeotropic distillation.