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US3717684A
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Process for preparing chlorinated aromatics
Assignee: Gulf Research and Development Co
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Filing: 1970-09-11
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Granted: 1973-02-20
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Expires: 1990-09-11
Abstract
Abstract A process for preparing a nuclear polychloro alkyl aromatic compound which involves heating an alkyl aromatic in the presence of a nitrate ion, a nitrite ion, NO or NO2, HCl, water, oxygen and a strong acid, wherein the molar ratio of HCl to aromatic compound is initially at a level of about 4:1 to about 10:1 and such ratio is maintained at approximately such level during the course of the reaction.
Inventors
- 👤 V Notaro
- 👤 C Selwitz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 03:41
CPC Classifications
C; C07; C07C; C07C17/00; C07C17/093; C07C17/15; C07C17/152; C07C17/156
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
266 words
A process for preparing a nuclear polychloro alkyl aromatic hydrocarbon without undue chlorination of the alkyl substituent on the aromatic hydrocarbon which comprises contacting an alkyl aromatic hydrocarbon, wherein the alkyl substituent has from one to 20 carbon atoms, with (1) a nitrate ion, a nitrite ion, NO or NO2, (2) HCl, (3) water, (4) molecular oxygen and (5) a protonic acid having an ionization constant at 25* C. greater than about 10 2 selected from the group consisting of perchloric acid, toluene sulfonic acid, trifluoroacetic acid, sulfuric acid and iodic acid at a temperature of about 15* to about 200* C. and a pressure of about 0.1 to about 10,000 pounds per square inch gauge for about 0.0001 to about 200 hours, wherein the amount of nitrate ion, nitrite ion, NO or NO2, on a molar basis, relative to the alkyl aromatic hydrocarbon reactant, is from about 2:1 to about 1:106, the initial molar ratio of HCl to the alkyl aromatic hydrocarbon reactant is in the range of about 4:1 to about 10.1, the amount of water, on a molar basis, relative to the alkyl aromatic compound reactant is in the range of about 1000:1 to about 0.1:1, the amount of molecular oxygen, on a molar basis, relative to the alkyl aromatic hydrocarbon reactant, is from about 1000:1 to about 1:10, and the amount of protonic acid, on a molar basis, relative to water, is from about 2:1 to about 1:20, and maintaining the molar ratio of HCl to the alkyl aromatic hydrocarbon reactant at approximately the initial level during the course of the reaction.
Claim 2
Dependent Claim
266 words
A process for preparing a nuclear polychloro alkyl aromatic hydrocarbon without undue chlorination of the alkyl substituent on the aromatic hydrocarbon which comprises contacting an alkyl aromatic hydrocarbon, wherein the alkyl substituent has from one to 20 carbon atoms, with (1) a nitrate ion, a nitrite ion, NO or NO2, (2) HCl, (3) water, (4) molecular oxygen and (5) a protonic acid having an ionization constant at 25* C. greater than about 10 2 selected from the group consisting of perchloric acid, toluene sulfonic acid, trifluoroacetic acid, sulfuric acid and iodic acid at a temperature of about 15* to about 200* C. and a pressure of about 0.1 to about 10,000 pounds per square inch gauge for about 0.0001 to about 200 hours, wherein the amount of nitrate ion, nitrite ion, NO or NO2, on a molar basis, relative to the alkyl aromatic hydrocarbon reactant, is from about 2:1 to about 1:106, the initial molar ratio of HCl to the alkyl aromatic hydrocarbon reactant is in the range of about 4:1 to about 10.1, the amount of water, on a molar basis, relative to the alkyl aromatic compound reactant is in the range of about 1000:1 to about 0.1:1, the amount of molecular oxygen, on a molar basis, relative to the alkyl aromatic hydrocarbon reactant, is from about 1000:1 to about 1:10, and the amount of protonic acid, on a molar basis, relative to water, is from about 2:1 to about 1:20, and maintaining the molar ratio of HCl to the alkyl aromatic hydrocarbon reactant at approximately the initial level during the course of the reaction.
Claim 3
Dependent Claim
137 words
The process of claim 1 wherein the reaction temperature is in the range of 60* to about 150* C., the pressure about ten to about 1000 pounds per square inch gauge, the contact time about one to about ten hours, the molar ratio of nitrate ion, nitrite ion, NO or NO2 to the alkyl aromatic hydrocarbon reactant is in the range of about 1:1 to about 1:10, the initial molar ratio of HCl to the alkyl aromatic hydrocarbon reactant from about 5:1 to about 8:1, the molar ratio of water to the alkyl aromatic hydrocarbon reactant is from about 10:1 to about 2:1, molar ratio of molecular oxygen to alkyl aromatic hydrocarbon reactant is from about 10:1 to about 1:1 and the molar amount of protonic acid relative to water is from about 1:2 to about 1:10.
Claim 4
Dependent Claim
18 words
The process of claim 1 wherein a nitrate ion is present and the same is obtained from HNO3.
Claim 5
Dependent Claim
12 words
The process of claim 1 wherein said protonic acid is sulfuric acid.
Claim 6
Dependent Claim
13 words
The process of claim 1 wherein said alkyl aromatic hydrocarbon reactant is xylene.
References Cited (Backward Citations)
US3160653A
Cited
US3591644A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1976-02-20 | 1976-08-21 | 1977-02-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1980-02-20 | 1980-08-21 | 1981-02-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1984-02-20 | 1984-08-21 | 1985-02-20 | $7700.00 | Window Closed / Lapsed |