Hydrofluoroethers having at least one hydrogenated -OCFX'CH3 end group wherein X'=F, CF3 and their preparation process

a technology of hydrofluoroethers and end groups, applied in the field of hydrofluoroethers, can solve the problems of further equipment choice, low yield and selectivity, and inability to obtain hydrofluoroethers with a high yield

Inactive Publication Date: 2007-05-10
SOLVAY SOLEXIS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The above methods employ starting compounds having a low molecular weight with a number of carbon atoms equal to or lower than 12, besides they give low yields and selectivity, and do not give hydrofluoroethers having at least one OCFX′CH3 end group with X′=F, CF3.
The reaction shows the limitation that to obtain acceptable conversions it is necessary to use CH3F as alkylating agent, has the drawback to require the use of Lewis acids which are aggressive and need the use of pressure resistant equipments built in special substances.
Furthermore HF forms, producing further problems in the equipment choice.
Since the alkylation reaction is an equilibrium reaction, it does not allow the obtainment of hydrofluoroethers with a high yield.
Besides they found application for the wide range of utilization temperatures as substituents of HFCs which in some cases have a limited application as refrigerants due to their very low boiling temperature or their very high freezing point.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0047] In a 1,000 ml flask, equipped with mechanical stirrer, bubbling pipe to introduce hydrogen / nitrogen, condenser with a bubble-counter

36.7 g of Pt supported on CaF2 (Pt=1.5% by weight), 400 ml of mixture 1:1 of perfluorobutyltetrahydrofuran and perfluoropropyltetrahydropyran (D100), are introduced.

[0048] By external heating with thermostated oil bath, the solvent is brought to the boiling temperature (100° C.), then hydrogen is fed at atmospheric pressure at a flow-rate of 20 1 / h, and 36.7 g of perfluoropolyether (PFPE) acylchloride of formula (IV)

CF3O(CF2CF (CF3) O) n (CF2O) pCF2COCl   (IV)

wherein n / p=25 and n, p are integers such that the number average molecular weight is 400, are fed by dropping funnel in 30 minutes.

[0049] When the PFPE-COCl feeding is over, the reduction is let complete for 15 minutes in hydrogen flow. It is then cooled to room temperature in nitrogen flow. The raw reaction compound is filtered to recover the catalyst.

[0050] The NMR (19F and 1H) an...

example 2

[0053] In the same equipment of the Example 1

32.5 g of Pt supported on CaF2 (Pt=1.5%), 150 ml of D100, are introduced.

[0054] One operates as described in the Example 1, by feeding 38.9 g of PFPE acylchloride of formula (VII):

Cl (CF2CF (CF3) O) nCF2COCl   (VII)

wherein n=3 and the number average molecular weight equal to 647.

[0055] The NMR (19F and 1H) analysis of the compound shows a 100% conversion of the starting PFPE-acylchloride, and a yield of 70% by moles in hydrofluoroether of formula (VIII):

Cl (CF2CF (CF3) O) nCF2CH3   (VIII)

[0056] The NMR analysis shows furthermore the presence of the alcohol compound in an amount equal to 30% by moles, having structure (IX):

Cl (CF2CF (CF3) O) nCF2CH2OH   (IX)

[0057] To separate the hydrofluoroether from the alcohol, the raw reaction compound is chromatographed on silica gel using D 100 as eluent. From the extract, after solvent distillation, 23 g of a compound are obtained which by the NMR. (19F and 1H) analysis shows to be the hy...

example 3

[0059] In a 100 ml flask equipped with mechanical stirrer, bubbling pipe to introduce hydrogen / nitrogen, condenser with bubble-counter,

1 g of Pt supported on C (Pt=5%),

40 ml of D100, are introduced.

[0060] One operates as described in the Example 1, by feeding 3.54 g of PFPE-acylchloride of the Example 2.

[0061] The NMR (19F and 1H) analysis of the compound shows a partial conversion of the starting PFPE-acylchloride (53% by moles) and the converted compound shows to be a mixture of compounds of which the formula (VIII) hydrofluoroether forms the 64% by moles.

[0062] The difference to 100 is constituted by the acid of formula (X):

Cl (CF2CF (CF3) O) nCF2CO2H   (X)

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Abstract

Hydrofluoroethers of formula:
T-CFX′—O—Rf—CFX-T′  (II)
wherein:
  • T=CH3;
  • X, X′, equal to or different from each other, are selected between F, CF3;
  • T′=F, Cl, H, C1—C3 perfluoroalkyl, CH3, CH20H, COC1, CHO, CO2H;
  • Rf is a perfluoroalkylene or a perfluoropolyoxyalkylene and respective preparation process by reduction with hydrogen in the presence of a platinum catalyst supported on metal fluorides of the corresponding compounds with at least one —COCl end group.

Description

CROSS-REFERENCE TO RELATED APPLICATION [0001] This is a Divisional Application, which claims the benefit of pending U.S. patent application Ser. No. 10 / 630,697, filed Jul. 3, 2003. The disclosure of the prior application is hereby incorporated herein in its entirety by reference.BACKGROUND OF THE INVENTION [0002] The present invention relates to hydrofluoroethers characterized in having at least one hydrogenated —OCFX′CH3 end group wherein X′=F, CF3 and their preparation process. [0003] More specifically, the preparation process relates to the reduction with H2, in the presence of platinum catalysts (Pt), of the corresponding fluorinated acylchloride precursors. [0004] Hydrofluoroethers prepared by direct fluorination with F2 or electrochemical fluorination of an ether compound or by alkylation of fluorinated alcohols are known. [0005] In patent application WO 99 / 47,480 it is shown that hydrofluoroethers can be obtained by alkylation of fluorinated carbonyl compounds. The above meth...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C07C59/10C07C47/02C07C51/58C07B61/00C07C41/18C07C43/12C07C43/13C07C43/315C07C47/198C07C51/04C07C59/135C08G65/00C08G65/22C08G65/322
CPCC07C43/126C07C43/137C07C43/315C07C59/135C08G65/007C08G65/226C08G65/322
Inventor PICOZZI, ROSALDODI MEO, ANTONELLATONELLI, CLAUDIO
Owner SOLVAY SOLEXIS
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