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Process for manufacturing perfluoroolefins by pyrolysis of perfluorocarbons in the presence of hydrogen

A technology of perfluorinated hydrocarbons and difluorocarbons, which is applied in the field of manufacturing perfluoroolefins, and can solve problems such as difficult removal of products and expensive purification steps

Active Publication Date: 2013-03-20
3M INNOVATIVE PROPERTIES CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since this method uses a chlorinated feedstock, it produces partially fluorinated and chlorinated low molecular weight products that are difficult to remove from TFE and HFP
Therefore, providing high-purity TFE involves expensive purification steps
In addition, a large amount of hydrochloric acid by-product containing HF as an impurity is also formed

Method used

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  • Process for manufacturing perfluoroolefins by pyrolysis of perfluorocarbons in the presence of hydrogen
  • Process for manufacturing perfluoroolefins by pyrolysis of perfluorocarbons in the presence of hydrogen

Examples

Experimental program
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Effect test

example

[0096] The pyrolysis experiments were carried out in a shock tube with an inner diameter of 10 cm as a model system of a pyrolysis reactor. The shock tube was heated with a heating mantle and had a viewing window for continuous recording by a UV photometer. The shock tube experiment is as and J. Troe, Helvetica Chimica Acta (Swiss Chemical Acta) 1972, 55, 2884. In a shock tube experiment, the test substance, a reactant mixture of perfluorinated hydrocarbons, hydrogen, and an inert carrier gas or diluent (argon), is fed into the low pressure section of the shock tube. The high pressure section contains hydrogen as the driving gas. The drive gas (in the observed portion of the test mixture) does not come into contact with the reaction mixture in the low pressure section. The low pressure section is separated from the high pressure section by an aluminum diaphragm. By increasing the pressure of the driving gas, the diaphragm ruptures and a shock wave is generated which propa...

example 1

[0101] A mixture of perfluoroethane (1.5 mol%), hydrogen (1.7 mol%), and argon (96.8 mol%) was fed into the high-pressure section of the shock tube (total gas concentration was 5.6 × 10 -5 mol cm -3 ). The mixture is incident on the shock wave ( figure 2 The first peak in ) is heated to a temperature of 610K, at which temperature, after the induction period, forms: CF 2 , and then the reflected shock reaches the observation window. The arrival of the reflected wave is determined by the second peak, namely figure 2 Indicated by distinct peaks in . The temperature behind the reflected wave is 1010K. The total gas concentration behind the reflected wave is 1.06×10 -4 mol cm -3 . :CF 2 Degradation curve and reaction 2: CF 2 →C 2 f 4 The rate constants at 1000K are in good agreement. The rate constant is k=1.3×10 17 cm 6 mol -2 the s -1 .

[0102] Thus, Example 1 shows that difluorocarbenes are formed under these reaction conditions and that difluorocarbenes are c...

example 2

[0103] Example 2 (comparative example)

[0104] Example 1 was repeated without using hydrogen. Failed to log to: CF 2 formed signal.

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Abstract

A process is described of pyrolyzing at least one perfluorinated hydrocarbon, or a material containing at least one perfluorinated hydrocarbon, in the presence of hydrogen, to yield a reaction mixture containing difluorocarbene.

Description

technical field [0001] The present invention relates to a chlorine-free process for the manufacture of perfluoroolefins, especially tetrafluoroethylene, by the thermal decomposition (pyrolysis) of perfluorocarbons in the presence of hydrogen. The invention also relates to a process for the production of difluorocarbenes as precursors of perfluoroalkenes, especially tetrafluoroethylene, by thermally decomposing (pyrolyzing) perfluorocarbons in the presence of hydrogen. body. Background technique [0002] Tetrafluoroethylene (TFE) and hexafluoropropylene (HFP) are widely used as monomers for the manufacture of plastic and elastic fluoropolymers. See, eg, Modern Fluoropolymers by J. Scheirs, Wiley, 1996. Worldwide consumption of TFE exceeds 10 5 tons / year. HFP is used as a comonomer for the manufacture of thermoplastic and elastomeric fluoropolymers and as a raw material for the preparation of hexafluoropropylene oxide (HFPO). It is estimated that the consumption of HFP wo...

Claims

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Application Information

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IPC IPC(8): C07C17/269C07C17/35C07C17/361C07C21/185
CPCC07C17/25C07C17/281C07C17/361C07C17/278C07C21/185C07C21/18C07C17/23
Inventor 克劳斯·辛策安德烈·施特赖特尔京特·J·肯普夫凯·赫尔穆特·洛哈斯米夏埃尔·尤尔根斯奥列格·夏伊绍科夫蒂尔曼·C·兹普利斯于尔根·特罗埃克劳斯·卢瑟尔
Owner 3M INNOVATIVE PROPERTIES CO