US4428923A
Expired / Lapsed
US
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Continuous process for the production of hydrogen peroxide according to the anthraquinone process
Assignee: Evonik Operations GmbH
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Filing: 1982-11-09
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Granted: 1984-01-31
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Expires: 2002-11-09
Abstract
Abstract There is provided a continuous parallel current flow process for carrying out the catalytic hydrogenation with hydrogen or a hydrogen containing gas for the production of hydrogen peroxide in the anthraquinone process using palladium black suspended in the working solution at a temperature up to 100° C. and a pressure up to 15 bar absolute in a reaction space constructed as a meandering tube system in which the hydrogenation is carried out in a loop reactor made of tubes of the same nominal diameter and arranged either vertically or horizontally and connected by curving tubes (tube elbows) at flow velocities in the tubes of more than 3 m/sec.
Inventors
- 👤 Wolfgang Kunkel
- 👤 Jorg Kemnade
- 👤 Dietrich Schneider
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 07:34
CPC Classifications
C; C01; C01B; C01B15/00; C01B15/01; C01B15/022; C01B15/023; B; B01; B01J; B01J19/00; B01J19/24; B01J19/2415; B01J19/2435
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
109 words
In a process for the production of hydrogen peroxide by the anthraquinone process including a step of the catalyst hydrogenation with hydrogen or a hydrogen containing gas using a working solution having palladium black suspended therein and employing a meandering tube system as the reaction space at a temperature up to 100° C. and a pressure up to 15 bar, the improvement comprising carrying out the hydrogenation in a loop reactor made of tubes of the same nominal width and which are arranged vertically or horizontally and are connected by tube elbows of the same nominal width at a flow velocity in the tubes of at least 3 m/sec.
Claim 2
Dependent Claim
109 words
In a process for the production of hydrogen peroxide by the anthraquinone process including a step of the catalyst hydrogenation with hydrogen or a hydrogen containing gas using a working solution having palladium black suspended therein and employing a meandering tube system as the reaction space at a temperature up to 100° C. and a pressure up to 15 bar, the improvement comprising carrying out the hydrogenation in a loop reactor made of tubes of the same nominal width and which are arranged vertically or horizontally and are connected by tube elbows of the same nominal width at a flow velocity in the tubes of at least 3 m/sec.
Claim 3
Dependent Claim
13 words
A process according to claim 1 wherein the flow velocity is 4-7 m/sec.
Claim 4
Dependent Claim
20 words
A process according to claim 2 wherein the palladium black concentration is not over 10 kg/m 3 of reaction solution.
Claim 5
Dependent Claim
21 words
A process according to claim 3 wherein the palladium black concentration is between 0.5 and 3 kg/m 3 of reaction solution.
Claim 6
Dependent Claim
21 words
A process according to claim 1 wherein the palladium black concentration is not over 10 kg. m 3 of reaction solution.
Claim 7
Dependent Claim
21 words
A process according to claim 4 wherein the palladium black concentration is between 0.5 and 3 kg/m 3 of reaction solution.
Claim 8
Dependent Claim
45 words
A process according to claim 1 wherein the temperature is 20° to 100° C., the pressure is 1 to 15 bar, the flow velocity is 3 to 10 m/sec and the concentration of palladium black is 0.2 gram/1 to 10 kg/m 3 of reaction solution.
References Cited (Backward Citations)
US3423176A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-01-30 | 1987-08-01 | 1988-01-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-01-30 | 1991-08-01 | 1992-01-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-01-30 | 1995-08-01 | 1996-01-31 | $7700.00 | Window Closed / Lapsed |