Patent classifications
C07C17/087
PROCESS FOR THE REDUCTION OF R?C?CX IMPURITIES IN FLUOROOLEFINS
This disclosure relates to processes which involve: contacting a mixture comprising at least one fluoroolefin and at least one impurity with at least one zeolite to reduce the concentration of the at least one impurity in the mixture; and the at least one zeolite is selected from the group consisting of zeolites having pore opening of at least 4 Angstroms and no more than about 5 Angstroms, zeolites having pore opening of at least about 5 Angstroms and Sanderson electronegativity of no more than about 2.6, and mixtures thereof; provided that the at least one zeolite is not zeolite 4A. This disclosure also relates to processes for making at least one hydrotetrafluoropropene product selected from the group consisting of CF.sub.3CF═CH.sub.2, CF.sub.3CH═CHF, and mixtures thereof; and relates to processes for making at least one hydrochlorotrifluoropropene product selected from the group consisting of CF.sub.3CCl═CH.sub.2, CF.sub.3CH═CHCl, and mixtures thereof.
PROCESS FOR THE REDUCTION OF R?C?CX IMPURITIES IN FLUOROOLEFINS
This disclosure relates to processes which involve: contacting a mixture comprising at least one fluoroolefin and at least one impurity with at least one zeolite to reduce the concentration of the at least one impurity in the mixture; and the at least one zeolite is selected from the group consisting of zeolites having pore opening of at least 4 Angstroms and no more than about 5 Angstroms, zeolites having pore opening of at least about 5 Angstroms and Sanderson electronegativity of no more than about 2.6, and mixtures thereof; provided that the at least one zeolite is not zeolite 4A. This disclosure also relates to processes for making at least one hydrotetrafluoropropene product selected from the group consisting of CF.sub.3CF═CH.sub.2, CF.sub.3CH═CHF, and mixtures thereof; and relates to processes for making at least one hydrochlorotrifluoropropene product selected from the group consisting of CF.sub.3CCl═CH.sub.2, CF.sub.3CH═CHCl, and mixtures thereof.
Preparation of 2,3,3,3-tetrafluoropropene and intermediates thereof
The present invention provides a process for preparation of 2,3,3,3-tetrafluoropropene and intermediates thereof. Owing to its low global warming potential and zero ozone depleting potential, it is been proposed as a replacement for existing chlorofluorocarbons and hydrofluorocarbons as refrigerant.
Preparation of 2,3,3,3-tetrafluoropropene and intermediates thereof
The present invention provides a process for preparation of 2,3,3,3-tetrafluoropropene and intermediates thereof. Owing to its low global warming potential and zero ozone depleting potential, it is been proposed as a replacement for existing chlorofluorocarbons and hydrofluorocarbons as refrigerant.
Preparation of 2,3,3,3-tetrafluoropropene and intermediates thereof
The present invention provides a process for preparation of 2,3,3,3-tetrafluoropropene and intermediates thereof. Owing to its low global warming potential and zero ozone depleting potential, it is been proposed as a replacement for existing chlorofluorocarbons and hydrofluorocarbons as refrigerant.
METHODS OF MAKING HALOGENATED PARTIALLY FLUORINATED COMPOUNDS
Described herein is method of making a halogenated partially fluorinated compound, comprising: (a) providing a compound having the following structure of formula (I): R.sub.f—CF═CXY wherein X and Y are independently selected from F and Cl; wherein R.sub.f is a fluorinated monovalent group comprising 1 to 10 carbon atoms; (b) contacting the compound with at least one of (i) an iodine or bromine containing salt in the presence of an acid; and (ii) aqueous solution of HZ wherein Z is selected from I and Br to form the halogenated partially fluorinated compound of the formula (II): R′.sub.f—CFH—CXYZ wherein X and Y are independently selected from F and Cl; Z is selected from I and Br; and R′.sub.f is a fluorinated monovalent group comprising 1 to 10 carbon atoms.
METHODS OF MAKING HALOGENATED PARTIALLY FLUORINATED COMPOUNDS
Described herein is method of making a halogenated partially fluorinated compound, comprising: (a) providing a compound having the following structure of formula (I): R.sub.f—CF═CXY wherein X and Y are independently selected from F and Cl; wherein R.sub.f is a fluorinated monovalent group comprising 1 to 10 carbon atoms; (b) contacting the compound with at least one of (i) an iodine or bromine containing salt in the presence of an acid; and (ii) aqueous solution of HZ wherein Z is selected from I and Br to form the halogenated partially fluorinated compound of the formula (II): R′.sub.f—CFH—CXYZ wherein X and Y are independently selected from F and Cl; Z is selected from I and Br; and R′.sub.f is a fluorinated monovalent group comprising 1 to 10 carbon atoms.
METHODS OF MAKING HALOGENATED PARTIALLY FLUORINATED COMPOUNDS
Described herein is method of making a halogenated partially fluorinated compound, comprising: (a) providing a compound having the following structure of formula (I): R.sub.f—CF═CXY wherein X and Y are independently selected from F and Cl; wherein R.sub.f is a fluorinated monovalent group comprising 1 to 10 carbon atoms; (b) contacting the compound with at least one of (i) an iodine or bromine containing salt in the presence of an acid; and (ii) aqueous solution of HZ wherein Z is selected from I and Br to form the halogenated partially fluorinated compound of the formula (II): R′.sub.f—CFH—CXYZ wherein X and Y are independently selected from F and Cl; Z is selected from I and Br; and R′.sub.f is a fluorinated monovalent group comprising 1 to 10 carbon atoms.
Catalyst and process using the catalyst for manufacturing fluorinated hydrocarbons
A catalyst comprising one or more metal oxides, wherein the catalyst has a total pore volume equal to or greater than 0.3 cm.sup.3/g and a mean pore diameter greater than or equal to 90 Å, where in the pore volume is measured using N.sub.2 adsorption porosimetry and the mean pore diameter is measured using N.sub.2 BET adsorption porosimetry.
Catalyst and process using the catalyst for manufacturing fluorinated hydrocarbons
A catalyst comprising one or more metal oxides, wherein the catalyst has a total pore volume equal to or greater than 0.3 cm.sup.3/g and a mean pore diameter greater than or equal to 90 Å, where in the pore volume is measured using N.sub.2 adsorption porosimetry and the mean pore diameter is measured using N.sub.2 BET adsorption porosimetry.