US5039508A
Expired / Lapsed
US
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Production of hydrogen peroxide
Assignee: Lyondell Chemical Technology LP
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Filing: 1990-07-19
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Granted: 1991-08-13
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Expires: 2010-07-19
Abstract
Abstract Hydrogen peroxide is produced by liquid phase molecular oxygen oxidation of methyl benzyl alcohol, the reaction being carried out such that the oxygen absorption rate is 90% or more of the maximum at the reaction conditions and the exit gas oxygen partial pressure is not greater than 3.0, the minimum necessary to establish the maximum oxygen absorption rate.
Inventors
- 👤 Robert N. Cochran
- 👤 Lawrence M. Candela
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 16:02
CPC Classifications
C; C01; C01B; C01B15/00; C01B15/01; C01B15/022; C01B15/026; C01B15/013; C07; C07C; C07C45/00; C07C45/27; C07C45/32; C07C45/37; C07C45/39
Claims Analysis
Total Claims: 3
Claim 1
Independent Claim
186 words
The process for the production of hydrogen peroxide which comprises continuously reacting methyl benzyl alcohol in the liquid phase in a plurality of separate back-mixed reaction zones with molecular oxygen at non-flammable reaction conditions, at a temperature in the range 120°-180° C. and a pressure in the range 5 to 1000 psig while maintaining the water content of the liquid reaction mixture below 4 wt. % in each zone, introducing molecular oxygen in parallel into each reaction zone, maintaining the rate at which molecular oxygen is absorbed into the liquid phase in each of the separate zones during the reaction at a value which is at least 90% of the maximum rate at which oxygen can be absorbed at the conditions of the reaction, maintaining the partial pressure of oxygen in the gases exiting each of the separate reaction zones at a value not more than 3.0 times the minimum value necessary to establish the maximum oxygen absorption rate, passing reaction liquid in series from one reaction zone to the next, the concentration of hydrogen peroxide in the reaction liquid increasing in each successive reaction zone.
Claim 2
Dependent Claim
186 words
The process for the production of hydrogen peroxide which comprises continuously reacting methyl benzyl alcohol in the liquid phase in a plurality of separate back-mixed reaction zones with molecular oxygen at non-flammable reaction conditions, at a temperature in the range 120°-180° C. and a pressure in the range 5 to 1000 psig while maintaining the water content of the liquid reaction mixture below 4 wt. % in each zone, introducing molecular oxygen in parallel into each reaction zone, maintaining the rate at which molecular oxygen is absorbed into the liquid phase in each of the separate zones during the reaction at a value which is at least 90% of the maximum rate at which oxygen can be absorbed at the conditions of the reaction, maintaining the partial pressure of oxygen in the gases exiting each of the separate reaction zones at a value not more than 3.0 times the minimum value necessary to establish the maximum oxygen absorption rate, passing reaction liquid in series from one reaction zone to the next, the concentration of hydrogen peroxide in the reaction liquid increasing in each successive reaction zone.
Claim 3
Dependent Claim
34 words
The process of claim 1 wherein the exit gas oxygen partial pressure from each zone is not more than 2.0 times the minimum value necessary to establish the maximum absorption rate for that zone.
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) | 1994-08-12 | 1995-02-11 | 1995-08-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1998-08-12 | 1999-02-11 | 1999-08-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2002-08-12 | 2003-02-11 | 2003-08-13 | $7700.00 | Window Closed / Lapsed |