PROCESS FOR THE MANUFACTURE OF HALOGENATED PROPANES CONTAINING END-CARBON FLUORINE
A process is disclosed for producing a compound of the formula: CF3CHXCF3-zYz where X and Y are independently selected from the group consisting of H and Cl, and z is 0 or 1. The process involves (1) contacting CCl3CHXCC3-zYz,CCl2-zYz=CXCC3, and/or CCl2CX=CC3-zYz starting material, with hydrogen flu...
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Main Authors | , , |
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Format | Patent |
Language | English French |
Published |
16.10.1997
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Edition | 6 |
Subjects | |
Online Access | Get full text |
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Abstract | A process is disclosed for producing a compound of the formula: CF3CHXCF3-zYz where X and Y are independently selected from the group consisting of H and Cl, and z is 0 or 1. The process involves (1) contacting CCl3CHXCC3-zYz,CCl2-zYz=CXCC3, and/or CCl2CX=CC3-zYz starting material, with hydrogen fluoride at a temperature of less than 200 ~C to produce a fluorination product of said starting material which includes at least 90 mole percent total of C3HXYzCl6-z-xFx saturated compounds and C3XYzCl5-z-yFy olefinic compounds, wherein x is an integer from 1 to 6-z and y is an integer from 1 to 5-z, (the fluorination product including no more than about 40 mole percent of the desired product, CF3CHXCF3-zYz); (2) contacting saturated compounds and olefinic compounds produced in (1) with hydrogen fluoride in the vapor phase at a temperature of from 200 ~C to about 400 ~C in the presence of a fluorination catalyst; and (3) reacting a sufficient amount of said compounds, wherein x is an integer from 1 to 5-z and olefinic compounds produced in (1) with hydrogen fluoride in the vapor phase at a temperature of from 200 ~C to about 400 ~C in the presence of a vapor phase fluorination catalyst to provide an overall selectivity to CF3CHXCF3-zYz of at least about 90 percent based upon the amount of starting material reacted with HF in (1) and (2). |
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AbstractList | A process is disclosed for producing a compound of the formula: CF3CHXCF3-zYz where X and Y are independently selected from the group consisting of H and Cl, and z is 0 or 1. The process involves (1) contacting CCl3CHXCC3-zYz,CCl2-zYz=CXCC3, and/or CCl2CX=CC3-zYz starting material, with hydrogen fluoride at a temperature of less than 200 ~C to produce a fluorination product of said starting material which includes at least 90 mole percent total of C3HXYzCl6-z-xFx saturated compounds and C3XYzCl5-z-yFy olefinic compounds, wherein x is an integer from 1 to 6-z and y is an integer from 1 to 5-z, (the fluorination product including no more than about 40 mole percent of the desired product, CF3CHXCF3-zYz); (2) contacting saturated compounds and olefinic compounds produced in (1) with hydrogen fluoride in the vapor phase at a temperature of from 200 ~C to about 400 ~C in the presence of a fluorination catalyst; and (3) reacting a sufficient amount of said compounds, wherein x is an integer from 1 to 5-z and olefinic compounds produced in (1) with hydrogen fluoride in the vapor phase at a temperature of from 200 ~C to about 400 ~C in the presence of a vapor phase fluorination catalyst to provide an overall selectivity to CF3CHXCF3-zYz of at least about 90 percent based upon the amount of starting material reacted with HF in (1) and (2). |
Author | SIEVERT, ALLEN CAPRON WARWAS, EDWIN J NAPPA, MARIO JOSEPH |
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DocumentTitleAlternate | PROCEDE POUR LA FABRICATION DE PROPANES HALOGENES CONTENANT DU FLUOR A CARBONE TERMINAL |
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Snippet | A process is disclosed for producing a compound of the formula: CF3CHXCF3-zYz where X and Y are independently selected from the group consisting of H and Cl,... |
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Title | PROCESS FOR THE MANUFACTURE OF HALOGENATED PROPANES CONTAINING END-CARBON FLUORINE |
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