Fluorination Process Temperature Control for Catalyst Stability

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Solution Overview

Problem

Current methods for producing hydrofluoroolefins like 2,3,3,3-tetrafluoropropene (HFO-1234yf) face challenges with catalyst instability, decreased selectivity, and increased undesirable by-products due to high temperatures and pressures, leading to economic and safety issues.

Innovation Solution

A process controlling reaction temperature and pressure during fluorination, maintaining temperatures below 300°C and pressures between 50-125 psig, using specific catalysts like chromium oxide, to prolong catalyst life and improve selectivity and product yield.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If high temperature and pressure are used during fluorination, then reaction rate increases, but catalyst stability decreases and selectivity worsens

Engineering Contradiction:
Improvereaction rateVSAvoidcatalyst stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent applies parameter changes by optimizing the temperature and pressure conditions during fluorination. Specifically, it maintains temperature below 300°C and pressure between 50-125 psig, which are controlled parameter ranges that balance reaction rate with catalyst stability and product selectivity.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If high temperature is used during fluorination, then reaction rate increases, but by-product formation increases

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

Solution Approach 1:

The patent controls the reaction temperature to remain below 300°C and pressure between 50-125 psig. These parameter changes ensure that the reaction proceeds at a reasonable rate while minimizing the formation of undesirable by-products such as carbon black and other impurities.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If vaporized feed streams are used, then reaction efficiency increases, but temperature control becomes more difficult

Engineering Contradiction:
Improvereaction efficiencyVSAvoidtemperature control complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent specifies operating the fluorination reaction with vaporized feed streams at temperatures below 300°C and pressures between 50-125 psig. This approach maintains reaction efficiency while the controlled parameter ranges simplify temperature and pressure management compared to broader operating windows.

Inventive Principle:
Principle #35Parameter changes

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 extends catalyst life, enhances product selectivity, and reduces by-products, resulting in a more efficient and cost-effective production of HFO-1234yf with improved safety and environmental benefits.

Implementation Method 1

contacting said starting composition with a fluorinating agent to produce a final composition comprising 2-chloro-3, 3,3trifluoropropene

Methodology Applied
Scientific EffectChemical substitution reaction: Chemical Bonding

Implementation Method 2

contacting said starting composition with a fluorinating agent to produce a final composition comprising 2-chloro-3, 3,3trifluoropropene

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentEP3808721A1Process for preparing 2-chloro-3,3,3-trifluoropropene
Publication Date: 2021.04.21 SOLSTICE ADVANCED MATERIALS US INC
  • EP3808721A1 patent drawingFigure 1
  • EP3808721A1 patent drawing
  • EP3808721A1 patent drawing

AI summary

The present invention relates, in part, to the discovery that high temperatures during the fluorination of 1, 1, 2, 3-tetrachloropropene (HCO-1230xa) to 2-chloro-3, 3, 3-trifluoropropene (HCFO-1233xf) results in catalyst instability, reduced selectivity of the conversion, and/or the formation of one or more undesirable by-products. By controlling the reaction temperature, it is shown that the catalyst life may be extended and the selectivity of the reaction improved. Such control similarly results in an overall improvement in the production of certain hydrofluoroolefins, particularly 2, 3, 3, 3-tetrafluoropropene (HFO-1234yf).