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Process for producing pentafluoroethane

A technology for pentafluoroethane and monochlorotrifluoroethane is applied in the field of preparation of pentafluoroethane to achieve the effects of cheap and easy-to-obtain raw materials, reduced production cost, high selectivity and yield

Inactive Publication Date: 2006-10-04
叶光武 +1
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Chinese patent document CN1035812 discloses a method for preparing pentafluoroethane by gas-phase fluorination at a temperature of 300-370° C. using dichlorotrifluoroethane (HCFC123 / 123a) as an initial reactant and using chromium trioxide as a catalyst, and Disclosed the preparation method of concrete catalyst, can obtain high yield and high transformation rate, but carry out comprehensive consideration from the angle of raw material used, dichlorotrifluoroethane (HCFC123 / 123a) is not as cheap as tetrachlorethylene or trichlorethylene and Easy to get, this method is not very ideal for industrial production

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  • Process for producing pentafluoroethane
  • Process for producing pentafluoroethane

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Embodiment 1

[0015] Such as figure 1 As shown, trichlorethylene and hydrogen fluoride are passed as a stream 1 into a fluorination reactor 2, and under the catalysis of a fluorination catalyst, a liquid-phase fluorination reaction is carried out at a temperature of 0-150°C. Catalyst using Sb-Cl x f y (wherein both x and y are positive numbers and the sum of x and y is 5), in the reaction process, the reaction can be guaranteed under the conditions of 0-150 ° C, and the yield and selectivity will increase when the temperature increases. However, the requirements for the reactor are also relatively high. The preferred reaction temperature is 50-150°C. By controlling the reaction time and the molar ratio and total flow of trichlorethylene and hydrogen fluoride in the feed stream 1, the monochlorotrifluoro The overall yield of ethane (HCFC133a) remained at a relatively high level. Chlorine gas can be fed intermittently during the reaction to maintain the activity of the catalyst and the hig...

Embodiment 2

[0019] In this embodiment, it is a continuous reaction process.

[0020] Such as figure 2 As shown, trichlorethylene and hydrogen fluoride are passed as a stream 1 into a fluorination reactor 2, and a liquid-phase fluorination reaction is carried out at a temperature of 0-150° C. under the catalytic action of a fluorination catalyst. The difference from Example 1 is that the reaction product stream 3 of the fluorination reactor 2 first enters the separator 11 for separation, and the separated unreacted raw material stream 11 is recycled back to the reactor 2 for further fluorination, and the stream 12 Together with chlorine, it is sent to chlorination reactor 4 for chlorination to chlorinate monochlorotrifluoroethane (HCFC133a) into dichlorotrifluoroethane (HCFC123a). The reaction product stream 5 is fluorinated with hydrogen fluoride in the fluorination reactor 6. After the fluorination reaction, the stream 7 enters the distillation tower 8 for separation. Fluoroethane (CF...

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Abstract

The disclosed preparation method for pentafluoethane comprises: with trichloroethylene as material, fluorinating, chlorinating and separating; recycling unreacted material to reaction system. This invention has well selectivity and high yield.

Description

technical field [0001] The invention relates to a preparation method of pentafluoroethane. Background technique [0002] Pentafluoroethane (HFC125) is a refrigerant and an important chemical raw material. At present, the synthesis method of pentafluoroethane mainly uses tetrachloroethylene or dichlorotrifluoroethane (HCFC123) and hydrogen fluoride in fluorine It is prepared by fluorination reaction under the catalytic action of chemical catalyst. [0003] Studies have shown that the use of tetrachloroethylene to prepare pentafluoroethane (HFC125) has a higher conversion rate, but the selectivity to pentafluoroethane (HFC125) is not ideal, and many by-products and intermediates will be produced, and These by-products and intermediates should be separated by multiple distillations, in which dichlorotrifluoroethane (HCFC123 / 123a) and chlorotetrafluoroethane (HCFC124 / 124a) can be refluxed into the fluorination reaction system for further fluorination , tetrafluoroethane (HCFC1...

Claims

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Application Information

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IPC IPC(8): C07C19/08C07C17/087
Inventor 叶光武王平
Owner 叶光武