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Process for the manufacture of 2-chloro-3,3,3-trifluoropropene by gas phase fluorination of pentachloropropane

A technology of pentachloropropane and trifluoropropene, applied in the field of producing 2-chloro-3,3,3-trifluoropropene through gas-phase fluorination of pentachloropropane, which can solve the problems of not providing operation examples

Active Publication Date: 2015-10-14
ARKEMA FRANCE SA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

No working example provided with 240db as starting material

Method used

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  • Process for the manufacture of 2-chloro-3,3,3-trifluoropropene by gas phase fluorination of pentachloropropane

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0052] At 79.4cm 3 load on AlF 3 Fluorination of 240db (1,1,1,2,3-pentachloropropane) was carried out in the aforementioned reactor over a Ni-Cr catalyst.

[0053] The catalyst used is a mixed catalyst with a nickel / chromium atomic ratio Ni / Cr=1 supported on aluminum fluoride, and is impregnated with nickel and chromic anhydride (CrO 3 ) solution preparation. After impregnation and drying, the solid is treated in the presence of a mixture of hydrofluoric acid and nitrogen at a concentration of 5-10% by volume of the acid in nitrogen at a temperature of 320°C to 390°C.

[0054] 15 g / hour of anhydrous HF and about 4.5 g / hour of 1,1,1,2,3-pentachloropropane were continuously fed to the reactor for 86 hours at atmospheric pressure. Thus, the contact time was 7.4 seconds, the molar ratio of HF to 240 was 36, and the reaction temperature was 340°C. The amount of oxygen is about 4 mole % relative to 240db. The results are given in Table 1.

Embodiment 2

[0056] Fluorination of a mixture of 65.9 mol % of 240db or 1,1,1,2,3-pentachloropropane and 34.9 mol % of 240aa or 1,1,2,2,3-pentachloropropane was carried out according to the previous example 1 . The reactor was continuously fed with 16 g / hour of anhydrous HF and about 5.1 g / hour of 1,1,1,2,3-pentachloropropane at atmospheric pressure. Thus, the contact time was 6.9 seconds, the molar ratio was 34, and the reaction temperature was 340°C. The amount of oxygen is about 4 mole % relative to the total number of moles of 1,1,1,2,3-pentachloropropane and 1,1,2,2,3-pentachloropropane. The results are given in Table 1.

Embodiment 3 and 4

[0058] Example 2 was repeated at different temperatures as indicated in Table 1.

[0059] Table 1

[0060]

[0061] After 86 hours, no inactivation was observed in Example 1. Also, it is worth noting that the selectivity remains very high.

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Abstract

The present invention provides a process of catalytic fluorination in gas phase of product 1,1,1,2,3- pentachloropropane or / and 1,1,2,2,3-pentachloropropane into product 2-chloro-3,3,3-trifluoropropene in presence of a catalyst and oxygen.

Description

technical field [0001] The object of the present invention is the catalytic fluorination of the product 1,1,1,2,3-pentachloropropane (HCC240db) and / or 1,1,2,2,3-pentachloropropane (HCC240aa) in the gas phase to the product 2 -Chloro-3,3,3-trifluoropropene (HCFO1233xf). Background technique [0002] The Montreal Protocol for the protection of the ozone layer led to the end of the use of chlorofluorocarbons (CFCs). Compounds less aggressive to the ozone layer, such as hydrofluorocarbons (HFCs) such as HFC-134a, have replaced chlorofluorocarbons. These latter compounds have actually been shown to contribute greenhouse gases. There is a need to develop technologies exhibiting low ODP (Ozone Depletion Potential) and low GWP (Global Warming Potential). Although hydrofluorocarbons (HFCs), which are compounds that do not affect the ozone layer, were identified as interesting candidates, they exhibit relatively high GWP values. There is still a need to find compounds exhibiting l...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C17/20C07C17/25C07C17/42C07C21/18
CPCC07C17/206C07C17/25C07C17/42C07C21/18B01J23/866
Inventor P.邦尼特A.皮加莫L.温德林格N.杜塞特
Owner ARKEMA FRANCE SA