US2741584A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process and apparatus for concentrating hydrogen peroxide
Assignee: Evonik LCL Ltd
•
Filing: 1952-01-29
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Granted: 1956-04-10
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Expires: 1972-01-29
Abstract
No abstract record available.
Inventors
- 👤 Holmes William Raymond
- 👤 Godfrey Charles Stanley
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 20:21
CPC Classifications
C; C01; C01B; C01B15/00; C01B15/01; C01B15/013; Y; Y10; Y10S; Y10S159/00; Y10S159/901
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
277 words
A PROCESS FOR THE CONCENTRATION OF HYDROGEN PEROXIDE WHICH COMPRISES PASSING THE HYDROGEN PEROXIDE SOLUTION TO BE CONCENTRATED IN CO-CURRENT FLOW WITH HOT VAPOUR UP A TUBE WHOSE LENGTH IS AT LEAST TEN TIMES ITS WIDTH, CAUSING SAID HOT VAPOUR TO FLOW AT A SUFFICIENT VELOCITY TO CARRY SAID SOLUTION THEREWITH MIXED WITH THE VAPOUR AND FOR A DISTANCE SUFFICIENT TO ESTABLISH SUBSTANTIAL THERMODYNAMIC EQUILIBRIUM BETWEEN THE LIQUID AND VAPOR PHASES OF SAID MIXTURE PASSING THE MIXTURE OF VAPOUR AND LIQUID LEAVING THE TUBE TO A SEPARATOR WHERE IT IS SEPARATED INTO A VAPOUR CONTAINING HYDROGEN PEROXIDE AND A CONCENTRATED LIQUID CONTAINING HYDROGEN PEROXIDE, RETURNING A PART OF THE CONCENTRATED LIQUID TO THE LOWER PART OF SAID TUBE AND REMOVING THE REMAINDER FROM CIRCULATION, PASSING THE VAPOUR CONTAINING HYDROGEN PEROXIDE TO THE LOWER PART OF A SECOND TUBE WHOSE LENGTH IS AT LEAST TEN TIMES ITS WIDTH THROUGH WHICH IT IS PASSED UPWARDLY IN CO-CURRENT FLOW WITH A LIQUID SELECTED FROM THE GROUP CONSISTING OF WATER AND HYDROGEN PEROXIDE SOLUTIONS WHICH ARE MORE DILUTE THAN THE HYDROGEN PEROXIDE INTRODUCED INTO SAID FIRST TUBE, CAUSING SAID VAPOUR TO FLOW AT A SUFFICIENT VELOCITY TO CARRY SAID LIQUID THEREWITH MIXED WITH THE VAPOUR AND FOR A DISTANCE SUFFICIENT TO ESTABLISH SUBSTANTIAL THERMODYNAMIC EQUILIBRIUM BETWEEN THE LIQUID AND VAPOR PHASES OF SAID MIXTURE, PASSING THE MIXTURE OF VAPOUR AND LIQUID LEAVING THE SECOND TUBE INTO A SECOND SEPARATOR WHERE IT IS SEPARATED INTO A RELATIVELY CONCENTRATED LIQUID CONTAINING HYDROGEN PEROXIDE AND VAPOUR, RETURNING A PART OF THE RELATIVELY CONCENTRATED LIQUID TO THE LOWER END OF SAID SECOND TUBE AND FEEDING ANOTHER PART TO THE LOWER END OF SAID FIRST TUBE.
Claim 2
Dependent Claim
277 words
A PROCESS FOR THE CONCENTRATION OF HYDROGEN PEROXIDE WHICH COMPRISES PASSING THE HYDROGEN PEROXIDE SOLUTION TO BE CONCENTRATED IN CO-CURRENT FLOW WITH HOT VAPOUR UP A TUBE WHOSE LENGTH IS AT LEAST TEN TIMES ITS WIDTH, CAUSING SAID HOT VAPOUR TO FLOW AT A SUFFICIENT VELOCITY TO CARRY SAID SOLUTION THEREWITH MIXED WITH THE VAPOUR AND FOR A DISTANCE SUFFICIENT TO ESTABLISH SUBSTANTIAL THERMODYNAMIC EQUILIBRIUM BETWEEN THE LIQUID AND VAPOR PHASES OF SAID MIXTURE PASSING THE MIXTURE OF VAPOUR AND LIQUID LEAVING THE TUBE TO A SEPARATOR WHERE IT IS SEPARATED INTO A VAPOUR CONTAINING HYDROGEN PEROXIDE AND A CONCENTRATED LIQUID CONTAINING HYDROGEN PEROXIDE, RETURNING A PART OF THE CONCENTRATED LIQUID TO THE LOWER PART OF SAID TUBE AND REMOVING THE REMAINDER FROM CIRCULATION, PASSING THE VAPOUR CONTAINING HYDROGEN PEROXIDE TO THE LOWER PART OF A SECOND TUBE WHOSE LENGTH IS AT LEAST TEN TIMES ITS WIDTH THROUGH WHICH IT IS PASSED UPWARDLY IN CO-CURRENT FLOW WITH A LIQUID SELECTED FROM THE GROUP CONSISTING OF WATER AND HYDROGEN PEROXIDE SOLUTIONS WHICH ARE MORE DILUTE THAN THE HYDROGEN PEROXIDE INTRODUCED INTO SAID FIRST TUBE, CAUSING SAID VAPOUR TO FLOW AT A SUFFICIENT VELOCITY TO CARRY SAID LIQUID THEREWITH MIXED WITH THE VAPOUR AND FOR A DISTANCE SUFFICIENT TO ESTABLISH SUBSTANTIAL THERMODYNAMIC EQUILIBRIUM BETWEEN THE LIQUID AND VAPOR PHASES OF SAID MIXTURE, PASSING THE MIXTURE OF VAPOUR AND LIQUID LEAVING THE SECOND TUBE INTO A SECOND SEPARATOR WHERE IT IS SEPARATED INTO A RELATIVELY CONCENTRATED LIQUID CONTAINING HYDROGEN PEROXIDE AND VAPOUR, RETURNING A PART OF THE RELATIVELY CONCENTRATED LIQUID TO THE LOWER END OF SAID SECOND TUBE AND FEEDING ANOTHER PART TO THE LOWER END OF SAID FIRST TUBE.
References Cited (Backward Citations)
US1013791A
Cited
US1536213A
Cited
US1738625A
Cited
GB445334A
Cited
GB473343A
Cited
US2298064A
Cited
US2438252A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1959-04-10 | 1959-10-10 | 1960-04-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1963-04-10 | 1963-10-10 | 1964-04-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1967-04-10 | 1967-10-10 | 1968-04-10 | $7700.00 | Window Closed / Lapsed |