US3950445A
Expired / Lapsed
US
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Process for the production of benzotrifluoride
Assignee: Lonza AG
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Filing: 1974-12-23
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Granted: 1976-04-13
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Expires: 1994-12-23
Abstract
Abstract The process of preparing benzotrifluoride which involves reacting benzotrichloride with hydrogen fluoride in a reaction zone at a pressure between 20 and 45 atm. and at a temperature between 85° and 100°C. The reaction is conducted in the presence of a catalyst consisting of a mixture of aluminum chloride and activated charcoal. On a stoichiometric basis, the amount of hydrogen fluoride is 1.0 to 1.1 times the amount of the benzotrichloride. The benzotrichloride, catalyst and hydrogen fluoride are present as an admixture or intermixture having a Reynolds number between 65,000 and 100,000. The reaction can be conducted in a stirring vessel equipped with a stirring mechanism.
Inventors
- 👤 Kurt Ryf
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 15:26
CPC Classifications
C; C07; C07C; C07C17/00; C07C17/093; C07C17/20; C07C17/202; C07C17/206
Claims Analysis
Total Claims: 20
Claim 1
Independent Claim
121 words
The process of preparing benzotrifluoride which comprises reacting benzotrichloride with hydrogen fluoride in a reaction zone at a pressure between 20 and 45 atm. and at a temperature between 85° and 100°C. in the presence of a catalyst consisting of a mixture of aluminum chloride and activated charcoal, the ratio of said aluminum chloride to said activated charcoal in said catalyst being between 1:2.5 and 1:3.0, on a stoichiometric basis, said hydrogen fluoride being 1.0 to 1.1 times the amount of said benzotrichloride, said benzotrichloride, said catalyst and said hydrogen fluoride being present as a mixture, and said mixture being intensively mixed to an extent during the reaction that the admixture or intermixture has a Reynolds number between 65,000 and 100,000.
Claim 2
Dependent Claim
121 words
The process of preparing benzotrifluoride which comprises reacting benzotrichloride with hydrogen fluoride in a reaction zone at a pressure between 20 and 45 atm. and at a temperature between 85° and 100°C. in the presence of a catalyst consisting of a mixture of aluminum chloride and activated charcoal, the ratio of said aluminum chloride to said activated charcoal in said catalyst being between 1:2.5 and 1:3.0, on a stoichiometric basis, said hydrogen fluoride being 1.0 to 1.1 times the amount of said benzotrichloride, said benzotrichloride, said catalyst and said hydrogen fluoride being present as a mixture, and said mixture being intensively mixed to an extent during the reaction that the admixture or intermixture has a Reynolds number between 65,000 and 100,000.
Claim 3
Dependent Claim
28 words
The process of claim 1 wherein said benzotrichloride is placed in said reaction zone, and then said catalyst and said hydrogen fluoride are placed in said reaction zone.
Claim 4
Dependent Claim
34 words
The process of claim 2 wherein said benzotrichloride is treated with about one percent of phosphorous trichloride, based on said benzotrichloride, before said catalyst and said hydrogen fluoride are added to said reaction zone.
Claim 5
Dependent Claim
27 words
The process of claim 2 wherein said benzotrichloride is heated to said reaction temperature before said catalyst and said hydrogen fluoride are added to said reaction zone.
Claim 6
Dependent Claim
28 words
The process of claim 2 wherein said reaction zone is heated to said reaction temperature after said catalyst and said hydrogen fluoride are added to said reaction zone.
Claim 7
Dependent Claim
28 words
The process of claim 5 wherein the pressure in said reaction zone is raised to the reaction pressure after said reaction zone is heated to said reaction temperature.
Claim 8
Dependent Claim
40 words
The process of claim 5 wherein the pressure is raised in said reaction zone to said reaction pressure after addition of said benzotrichloride, said catalyst and said hydrogen fluoride by the introduction of an inert gas into said reaction zone.
Claim 9
Dependent Claim
11 words
The process of claim 7 wherein said inert gas is nitrogen.
Claim 10
Dependent Claim
14 words
The process of claim 1 wherein said reaction temperature is between 90° and 95°C.
Claim 11
Dependent Claim
15 words
The process of claim 1 wherein said reaction pressure is between 35 and 40 atmospheres.
Claim 12
Dependent Claim
17 words
The process of claim 1 wherein said benzotrichloride, said catalyst and said hydrogen fluoride are intensively mixed.
Claim 13
Dependent Claim
16 words
The process of claim 1 wherein said admixture has a Reynolds number between 80,000 and 90,000.
Claim 14
Dependent Claim
43 words
The process of claim 1 wherein said reaction is carried out continuously, said reaction zone comprises two separate reaction regions, and said reaction being carried out to a desired state in said first reaction region and being completed in said second reaction region.
Claim 15
Dependent Claim
20 words
The process of claim 1 wherein the reaction is conducted for a period of time between 55 and 75 minutes.
Claim 16
Dependent Claim
22 words
The process of claim 1 wherein the formed benzotrifluoride is conventionally separated from the reactants and catalyst and is purified by distillation.
Claim 17
Dependent Claim
25 words
The process of claim 1 wherein said catalyst is present in an amount between 10 and 100 ppm, based on the amount of said benzotrichloride.
Claim 18
Dependent Claim
25 words
The process of claim 1 wherein said catalyst is present in an amount between 40 and 70 ppm, based on the amount of said benzotrichloride.
Claim 19
Dependent Claim
24 words
The process of claim 1 wherein the ratio of said aluminum chloride to said activated charcoal in said catalyst is between 1:2.7 and 1:2.9.
Claim 20
Dependent Claim
43 words
The process of claim 1 wherein said catalyst is prepared by suspending aluminum chloride and activated charcoal in an aqueous hydrochloric acid, drying the solution and activating the mixture of aluminum chloride and activated charcoal by heating at a temperature of about 300°C.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-04-13 | 1979-10-13 | 1980-04-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-04-13 | 1983-10-13 | 1984-04-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-04-13 | 1987-10-13 | 1988-04-13 | $7700.00 | Window Closed / Lapsed |