Process for the preparation of trifluoromethylated aromatic compounds

Claim 2

A process for the preparation of mono-trifluoromethylated aromatic compounds which comprises reacting an aromatic comound with carbon tetrahalide in the presence of a strong Bronsted or Lewis acid in anhydrous hydrogen fluoride at temperatures from about -20° C. to about 300° C. under pressures from about 10 millimeters to about 3,000 psig wherein the catalyst to carbon tetrahalide to aromatic compound to hydrogen fluoride molar ratios are in the range of from about 0.01/0.2/1.0/0.6 to about 5/10/1/100.

Claim 3

A process according to claim 1 wherein the aromatic compound utilized is selected from the group consisting of benzene, naphthalene, polycyclic aromatic hydrocarbons, derivatives thereof and polymers containing same such that the unsubstituted position of the aromatic compound has a reactivity equivalent to a Hammett sigma values of 0 to +0.8 and the compound is inert to anhydrous hydrogen fluoride.

Claim 4

Process according to claim 2 wherein the aromatic compound is benzene or a deactivated benzene derivative which is inert to anhydrous hydrogen fluoride containing unsubstituted positions having a reactivity equivalent to a Hammett sigma value of 0 to +0.8.

Claim 5

A process according to claim 3 wherein the catalyst is selected from the class of strong acids selected from fluorides and chlorides of elements of groups 4B to 6B and 3A to 5A of the Periodic Table and mixtures thereof.

Claim 6

The process according to claim 4 wherein the catalysts are selected from antimony trichloride, antimony trifluoride, antimony pentachloride, antimony pentafluoride, titanium tetrachloride, titanium tetrafluoride, niobium pentachloride, niobium pentafluoride, tantalum pentachloride, tantalum pentafluoride and mixtures thereof.

Claim 7

A process according to claim 5 wherein the reaction is carried out in a batch process.

Claim 8

A process according to claim 5 wherein the process is carried out in a continuous process.

Claim 9

A process according to claim 5 wherein the range of catalyst to carbon tetrahalide to aromatic compound to hydrogen fluoride molar ratios are from about 0.1/0.5/1.0/2.0 to about 1/2/1/20.

Claim 10

A process according to claim 8 wherein the reaction is run at pressures from about 1 atmosphere to about 750 psig.

Claim 11

A process according to claim 9 wherein the temperature utilized is in the range from about 0 to about 130° C.

Claim 12

A process according to claim 10 wherein the carbon tetrahalide has the formula CCl x Br 4-x or CCl y F 4-y wherein x is an integer from 0 to 4 and y is an integer from 1 to 4.

Claim 13

A process according to claim 11 wherein the carbon tetrahalide is carbon tetrachloride.

Claim 14

A process according to claim 12 wherein the aromatic compound utilized is selected from the group consisting of benzene, halobenzene, dihalobenzenes, mono- and dihalotoluenes except fluorotoluenes, benzoic acid, acetophenone, nitrobenzene, mononitrotoluenes, phenylacetic acid, azobenzene, benzenethiol, thioanisole, phenyl methyl sulfone, diphenyl sulfide, o-chloroanisole, o-nitroanisole, diphenyl sulfone, diphenyl sulfide, phenyldifluorophosphine, p-chloroanisole, p-nitroanisole, diphenyl sulfone, phenyldifluorophosphine, phenyltrifluorosilane, cinnamic acid, and 1- or 2-nitronaphthalenes.

Claim 15

A process according to claim 13 wherein the aromatic compound is selected from benzene mono- and dihalobenzenes, and all mono- and dihalotoluenes except monofluorotoluenes.