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US2714550A Expired / Lapsed US ⏱️ 0.0 years remaining

Nonelectrolytic production of chlorine

Assignee: Chemical Foundation Inc
•
Filing: 1951-12-10
•
Granted: 1955-08-02
•
Expires: 1971-12-10
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Abstract

No abstract record available.

Inventors

  • 👤 Miller Ralph

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 15:24
CPC Classifications
C; C01; C01B; C01B7/00; C01B7/01; C01B7/03; C01B7/05

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 186 words
THE PROCESS OF PRODUCING CHLORINE AND AMMONIA FROM AMMONIUM CHLORIDE WHICH COMPRISES REACTING AMMONIUM CHLORIDE TO MANGANOUS OXIDE, THE MOL RATIO OF AMMONIUM CHLORIDE TO MANGANOUS OXIDE BEING SUBSTANTIALLY TWO TO ONE, TO FORM AMMONIA AND MANGANOUS CHLORIDE, SEPARATING THE AMMONIA FROM THE MANGANOUS CHLORIDE, REACTING THE MANGANOUS CHLORIDE WITH MANGANESE DIOXIDE AND NITRIC ACID, EMPLOYING NOT LESS THAN 1 MOL OF MANGANESE DIOXIDE AND NOT LESS THAN 4 MOLS OF NITRIC ACID FOR EACH MOL OF MANGANOUS CHLORIDE, AT A TEMPERATURE SUFFICIENTLY ELEVATED TO FORM GASEOUS CHLORINE AND MANGANOUS NITRATE, SEPARATING THE CHLORINE FROM THE MANGANOUS NITRATE, THERMALLY REACTING THE MANGANOUS NITRATE IN THE PRESENCE OF AIR AND WATER TO FORM NITRIC ACID AND MANGANESE DIOXIDE, SEPARATING AND RECOVERING THE NITRIC ACID, RECYCLING THE RECOVERED NITRIC ACID TO THE CHLORINE FORMATION STEP OF THE PROCESS, REDUCING A PART OF THE MANGANESE DIOXIDE TO MANGANOUS OXIDE, THE AMOUNT OF MANGANOUS OXIDE FORMED BEING NOT LESS THAN THE AMOUNT CONSUMED IN THE AMMONIA LIBERATION STEP RECYCLING THE MANGANOUS OXIDE TO THE AMMONIA LIBERATION STEP AND RECYCLING THE REMAINDER OF THE MANGANESE DIOXIDE TO THE CHLORINE FORMATION STEP.
Claim 2
Dependent Claim 186 words
THE PROCESS OF PRODUCING CHLORINE AND AMMONIA FROM AMMONIUM CHLORIDE WHICH COMPRISES REACTING AMMONIUM CHLORIDE TO MANGANOUS OXIDE, THE MOL RATIO OF AMMONIUM CHLORIDE TO MANGANOUS OXIDE BEING SUBSTANTIALLY TWO TO ONE, TO FORM AMMONIA AND MANGANOUS CHLORIDE, SEPARATING THE AMMONIA FROM THE MANGANOUS CHLORIDE, REACTING THE MANGANOUS CHLORIDE WITH MANGANESE DIOXIDE AND NITRIC ACID, EMPLOYING NOT LESS THAN 1 MOL OF MANGANESE DIOXIDE AND NOT LESS THAN 4 MOLS OF NITRIC ACID FOR EACH MOL OF MANGANOUS CHLORIDE, AT A TEMPERATURE SUFFICIENTLY ELEVATED TO FORM GASEOUS CHLORINE AND MANGANOUS NITRATE, SEPARATING THE CHLORINE FROM THE MANGANOUS NITRATE, THERMALLY REACTING THE MANGANOUS NITRATE IN THE PRESENCE OF AIR AND WATER TO FORM NITRIC ACID AND MANGANESE DIOXIDE, SEPARATING AND RECOVERING THE NITRIC ACID, RECYCLING THE RECOVERED NITRIC ACID TO THE CHLORINE FORMATION STEP OF THE PROCESS, REDUCING A PART OF THE MANGANESE DIOXIDE TO MANGANOUS OXIDE, THE AMOUNT OF MANGANOUS OXIDE FORMED BEING NOT LESS THAN THE AMOUNT CONSUMED IN THE AMMONIA LIBERATION STEP RECYCLING THE MANGANOUS OXIDE TO THE AMMONIA LIBERATION STEP AND RECYCLING THE REMAINDER OF THE MANGANESE DIOXIDE TO THE CHLORINE FORMATION STEP.

References Cited (Backward Citations)

US304260A Cited
US320256A Cited
US348348A Cited
US379488A Cited
US495462A Cited
US570624A Cited
US2176776A Cited
US2044799A Cited
US2534298A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1958-08-01 1959-01-31 1959-08-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1962-08-01 1963-01-31 1963-08-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1966-08-01 1967-01-31 1967-08-02 $7700.00 Window Closed / Lapsed

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