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US2804376A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for production of hydrogen peroxide

Assignee: Olin Corp
•
Filing: 1952-07-12
•
Granted: 1957-08-27
•
Expires: 1972-07-12
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Abstract

No abstract record available.

Inventors

  • 👤 John F Haller
  • 👤 Theodore M Jenney
  • 👤 John W Churchill

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 10:35
CPC Classifications
C; C01; C01B; C01B15/00; C01B15/01; C01B15/022; C01B15/023

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 175 words
IN THE PRODUCTION OF HYDROGEN PEROXIDE FROM AN ALKYL ANTHRAQUINONE BY REDUCTION OF THE ANTHRAQUINONE IN SOLUTION WITH HYDROGEN IN THE PRESENCE OF A REDUCTION CATALYST FOLLOWED BY OXIDATION OF THE REDUCED SOLUTION, THE METHOD OF RECOVERING HYDROGEN PEROXIDE FROM THE OXIDIZED SOLUTION AND CONCENTRATING IT WHICH COMPRISES SUBJECTING THE OXIDIZED SOLUTION TO DISTILLATION IN A TOWER IN THE PRESSENCE OF STRIPPING STEAM AT A TOP TEMPERATURE WITHIN THE RANGE OF ABOUT 70* TO 105*C. UNDER A REDUCED PRESSURE WITHIN THE RANGE OF ABOUT 5 TO 65 MM. OF MERCURY SUCH THAT SUBSTANTIALLY ALL OF THE PEROXIDE AND WATER IS VAPORIZED FROM THE DISTILLATION SYSTEM AND THE BULK OF THE ORGANIC SOLUTION IS SEPARATED FROM THE DISTILLATION SYSTEM AS A LIQUID FRACTION FOR RECYCLE, SUBJECTING AQUEOUS PEROXIDE RECOVERED FROM THE FIRST DISTILLATION TO REDISTILLATION AT REDUCED PRESSURE AND AN ELEVATED TEMPERATURE BOILING WATER OVERHEAD, RECOVERING THE WATER OVERHEAD FRACTION AND RETURNING IT AS STRIPPING STEAM TO THE FIRST DISTILLATION, AND RECOVERING A CONCENTRATED HYDROGEN PEROXIDE PRODUCT AS A HIGHER BOILING FRACTION IN THE REDISTILLATION OPERATION.
Claim 2
Dependent Claim 175 words
IN THE PRODUCTION OF HYDROGEN PEROXIDE FROM AN ALKYL ANTHRAQUINONE BY REDUCTION OF THE ANTHRAQUINONE IN SOLUTION WITH HYDROGEN IN THE PRESENCE OF A REDUCTION CATALYST FOLLOWED BY OXIDATION OF THE REDUCED SOLUTION, THE METHOD OF RECOVERING HYDROGEN PEROXIDE FROM THE OXIDIZED SOLUTION AND CONCENTRATING IT WHICH COMPRISES SUBJECTING THE OXIDIZED SOLUTION TO DISTILLATION IN A TOWER IN THE PRESSENCE OF STRIPPING STEAM AT A TOP TEMPERATURE WITHIN THE RANGE OF ABOUT 70* TO 105*C. UNDER A REDUCED PRESSURE WITHIN THE RANGE OF ABOUT 5 TO 65 MM. OF MERCURY SUCH THAT SUBSTANTIALLY ALL OF THE PEROXIDE AND WATER IS VAPORIZED FROM THE DISTILLATION SYSTEM AND THE BULK OF THE ORGANIC SOLUTION IS SEPARATED FROM THE DISTILLATION SYSTEM AS A LIQUID FRACTION FOR RECYCLE, SUBJECTING AQUEOUS PEROXIDE RECOVERED FROM THE FIRST DISTILLATION TO REDISTILLATION AT REDUCED PRESSURE AND AN ELEVATED TEMPERATURE BOILING WATER OVERHEAD, RECOVERING THE WATER OVERHEAD FRACTION AND RETURNING IT AS STRIPPING STEAM TO THE FIRST DISTILLATION, AND RECOVERING A CONCENTRATED HYDROGEN PEROXIDE PRODUCT AS A HIGHER BOILING FRACTION IN THE REDISTILLATION OPERATION.

References Cited (Backward Citations)

US2169128A Cited
US2158525A Cited
US2369912A Cited
US2282184A Cited
US2215833A Cited
US2689169A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1960-08-26 1961-02-25 1961-08-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1964-08-26 1965-02-25 1965-08-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1968-08-26 1969-02-25 1969-08-27 $7700.00 Window Closed / Lapsed

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