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A kind of method utilizing cyclic reaction to prepare hexafluoroethane

A hexafluoroethane, cycle reaction technology, applied in the direction of halogen addition preparation, organic chemistry, etc., can solve the problems of detonation reaction, high risk of operation, slow reaction speed, etc., achieve mild reaction conditions, avoid cracking reaction, fast response effect

Active Publication Date: 2017-08-25
PERIC SPECIAL GASES CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] In the above methods, there are different problems, such as low yield, harsh process conditions, expensive reactor, high risk of operation, high corrosiveness of raw materials, slow reaction speed, low product concentration, etc.
As in method (5), there is a large amount of low-temperature tetrafluoroethylene in the reactor, and tetrafluoroethylene is very unstable, prone to detonation reaction, and the risk is high; in method (6), chlorofluoroalkane diluent and hexafluoroethane It is an azeotrope, which is difficult to separate by rectification

Method used

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  • A kind of method utilizing cyclic reaction to prepare hexafluoroethane

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] The volume of the tube-and-tube reactor 1 is 100L; the circulating air volume generated by the centrifugal fan 2 is 990L / min; the frozen brine with a mass fraction of 30% enters from the cooling medium inlet 6 and exits from the cooling medium outlet 7.

[0036] Fluorine gas with a flow rate of 4.95 L / min enters the tube-and-tube reactor 1 with a temperature of 10°C and a pressure of 0.15 MPa from the feed port 3 and tetrafluoroethylene with a flow rate of 4.95 L / min from the feed port 4. The space velocity of the gas in the tube-and-tube reactor 1 is 10 / min, and the reaction is carried out. Part of the reaction product obtained is circulated back to the column through the external circulation equipment centrifugal fan 2 of the tube-and-tube reactor 1 at the outlet of the tube-and-tube reactor 1. The inlet end of the tubular reactor 1 is mixed with the fluorine gas and tetrafluoroethylene that come in through the feed port 3 and the feed port 4, and then enters the tubul...

Embodiment 2

[0041] The volume of the tubular reactor 1 is 100L; the circulating air volume generated by the centrifugal fan 2 is 9.1L / min; water enters from the cooling medium inlet 6 and comes out from the cooling medium outlet 7; in the mixed gas of nitrogen and fluorine, fluorine The volume fraction of nitrogen is 10%, the volume fraction of nitrogen is 90%, and the flow rate of fluorine is 0.91L / min.

[0042] The mixed gas of nitrogen and fluorine enters the tube-and-tube reactor 1 with a temperature of 60°C and a pressure of 0.1 MPa from the feed port 3 and tetrafluoroethylene with a flow rate of 0.87 L / min from the feed port 4. The space velocity in the tube-and-tube reactor 1 is 0.2 / min, and the reaction is carried out. Part of the reaction product obtained is circulated back to the tube-and-tube reactor 1 through the centrifugal fan 2 of the external circulation equipment at the outlet of the tube-and-tube reactor 1. The inlet end of the reactor 1 is mixed with the mixed gas of ni...

Embodiment 3

[0047] The volume of the tube-and-tube reactor 1 is 100L; the circulating air volume generated by the centrifugal fan 2 is 289L / min; water enters from the cooling medium inlet 6 and comes out from the cooling medium outlet 7; in the mixed gas of nitrogen and fluorine, fluorine The volume fraction is 50%, the volume fraction of nitrogen gas is 50%, and the flow rate of fluorine gas is 3.6 L / min.

[0048]The mixed gas of nitrogen and fluorine enters the tube-and-tube reactor 1 with a temperature of 30°C and a pressure of 0.12 MPa from the feed port 3 and tetrafluoroethylene with a flow rate of 3.5 L / min from the feed port 4. The space velocity in the tube-and-tube reactor 1 is 3 / min, and the reaction is carried out. Part of the reaction product obtained is circulated back to the tube-and-tube reactor 1 through the external circulation equipment centrifugal fan 2 at the outlet of the tube-and-tube reactor 1. The inlet end of the reactor 1 is mixed with the mixed gas of nitrogen a...

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Abstract

The invention relates to a method for preparing hexafluoroethane by cyclic reaction, which belongs to the technical field of fluorine chemical industry. The method steps: fluorine gas or a mixed gas of nitrogen gas and fluorine gas, and tetrafluoroethylene enter a reactor with a temperature of 10-60° C. and a pressure of 0.1-0.15 MPa from different feed ports, and control the gas flow in the reactor The space velocity is 0.2-10 / min, and the reaction is carried out. The obtained part of the reaction product is circulated at the outlet of the reactor through the centrifugal fan of the external circulation equipment of the reactor and returned to the inlet of the reactor, and the fluorine or nitrogen gas and The mixed gas of fluorine gas and tetrafluoroethylene enters the reactor after being mixed, and the reaction is circulated; another part of the obtained reaction product comes out directly from the discharge port to obtain the hexafluoroethane. The method of the invention has the advantages of simple process, mild reaction conditions and cheap reactor price; the prepared hexafluoroethane has high concentration, low impurity content and high yield.

Description

technical field [0001] The invention relates to a method for preparing hexafluoroethane by cyclic reaction, which belongs to the technical field of fluorine chemical industry. Background technique [0002] Hexafluoroethane is an important chemical product, mainly used in integrated circuit etching and cleaning, refrigeration, high dielectric strength cooling, etc. At present, the methods for preparing hexafluoroethane are as follows: [0003] (1) In the patent CN00118734.1, cobalt difluoride is contacted with fluorine gas to be activated into cobalt trifluoride, and hydrofluoroethane is converted into perfluoroethane through the activated cobalt trifluoride catalyst at 300-350°C ; [0004] (2) In the patent CN1165803A, under high temperature, fluorine gas reacts with a hydrofluorocarbon with two carbon atoms in the presence of a diluent; [0005] (3) In patent CN1651370, in the presence of a fluorination catalyst, the mixed gas of hexafluoroethane and chlorotrifluorometha...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C19/08C07C17/04
Inventor 徐海云黄华璠胡帅董云海王斌吕灵华宋富财
Owner PERIC SPECIAL GASES CO LTD
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