Production of 2-chloro-2-hydrohexafluoropropane and azeotropes t

Organic compounds -- part of the class 532-570 series – Organic compounds – Halogen containing

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203 50, 203 67, C07C19/08

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059029110

DESCRIPTION:

BRIEF SUMMARY
FIELD OF THE INVENTION

This invention relates to the production of hydrohalofluorocarbons and their azeotropes with HF, and more particularly to the hydrogenolysis reactions of 2,2-dichlorohexafluoropropane using palladium-containing catalysts and products which can be produced thereby.


BACKGROUND

Various processes for the catalytic hydrogenolysis of chlorofluorocarbons and hydrochlorofluorocarbons are known. For example, U.S. Pat. No. 2,942,036 discloses the reaction of 1,2,2-trichloropentafluoropropane with hydrogen in the presence of palladium on activated carbon catalyst to produce 1,2,2-trihydropentafluoropropane. The examples show that under the conditions of the experiments one of the products from this reaction is CF.sub.3 CH.dbd.CF.sub.2. Japanese Patent Application Publication Hei 1(1989)-319441 discloses a process where one chlorine atom is selectively replaced by hydrogen in 1,1,1-trichlorotrifluoroethane using a platinum catalyst. For comparison, a palladium on carbon catalyst is disclosed to produce 1,1,1-trifluoroethane as the major product under the conditions of the experiment.
It is well known that the hydrogenolysis of compounds such as chlorofluorocarbons to replace chlorine by hydrogen produces hydrogen chloride as a co-product. Loss of fluorine when it occurs (e.g., to produce overhydrogenated products) can produce HF as a by-product.


SUMMARY OF THE INVENTION

The present invention provides a process for the monohydrogenolysis of 2,2-dichlorohexafluoropropane (i.e., CF.sub.3 CCl.sub.2 CF.sub.3, or CFC-216aa) to 2-chloro-2-hydrohexafluoropropane (i.e., CF.sub.3 CHClCF.sub.3, or HCFC-226da). The process comprises reacting said 2,2-dichlorohexafluoropropane with hydrogen at an elevated temperature of about 150.degree. C. or less in the presence of a catalyst containing a catalytically effective amount of palladium supported on trivalent chromium oxide in the presence of an acid of the formula HZ, where Z is selected from the group consisting of Cl, F and mixtures thereof, to produce 2-chloro-2-hydrohexafluoropropane with a selectivity of over 70% based upon the 2,2-dichlorohexafluoropropane converted.
Azeotropic compositions (e.g., an azeotropic composition comprising from about 80 to 47 mole percent HF and from about 20 to 53 mole percent CF.sub.3 CHClCF.sub.3) are also provided; as is a process for producing an azeotropic composition of HF and 2-chloro-2-hydrohexafluoropropane as a product of the monohydrogenolysis of 2,2-dichlorohexafluoropropane where HF is present.


DETAILED DESCRIPTION

The catalysts suitable for the process of this invention comprise palladium and may optionally contain other components such as other Group VIII metals. The palladium is supported on chromium oxide. Any source of chromium oxide is suitable, but chromium oxide prepared by the thermal decomposition of (NH.sub.4).sub.2 Cr.sub.2 O.sub.7 is especially preferred. A procedure for the preparation of Cr.sub.2 O.sub.3 by the thermal decomposition of (NH.sub.4).sub.2 Cr.sub.2 O.sub.7 is disclosed in U.S. Pat. No. 5,036,036, the entire contents of which are incorporated herein by reference.
The acid HZ is at least partially produced during the reaction as the halogen Cl is removed from the starting material as a result of the hydrogenolysis. Accordingly, Z is ordinarily at least in part Cl. Also of note are embodiments where Z is partially F (i.e., the acid is a mixture of HCl and HF). HF can be present for example, as a result of overhydrogenolysis, wherein fluorine substituents of the starting material are partially replaced by hydrogen. HF can also be present in the reaction feed. For example, residual HF can be present from processes used to make the 2,2-dichlorohexafluoropropane. Of note in this regard are embodiments where said starting material is a component of an azeotrope of HF and said starting material, and starting material from said azeotrope is reacted with hydrogen in the presence of HF from said azeotrope.
Unlike alumina supports which are readily fluorinated, chromia fluorinates much mo

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