US2878099A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of deacidifying gases
Assignee: RUHRSTAHL AG FA
•
Filing: 1955-07-22
•
Granted: 1959-03-17
•
Expires: 1975-07-22
Abstract
No abstract record available.
Inventors
- 👤 Breuing Wilhelm
- 👤 Spolders Rudolf
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 07:31
CPC Classifications
C; C10; C10K; C10K1/00; C10K1/08; C10K1/10; B; B01; B01D; B01D53/00; B01D53/14; B01D53/18; B01D53/34; B01D53/46; B01D53/48; B01D53/52; B01D53/526
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
305 words
A METHOD OF REMOVING ACID CONSTITUENTS SELECTED FROM THE GROUP CONSISTING OF CARBON DIOXIDE AND HYDROGEN SULFIDE FROM A GAS CONTAINING THE SAME DURING PASSAGE THEREOF THROUGH A GAS WASHER, COMPRISING THE STEPS OF PASSING A GAS CONTAINING GASEOUS ACID-FORMING CONSTITUENTS SELECTED FROM THE GROUP CONSISTING OF CARBON DIOXIDE AND HYDROGEN SULFIDE THROUGH A FIRST STAGE OF THE GAS WASHER IN WHICH AN AQUEOUS SOLUTION OF AN AMMONIUM SALT ADAPTED TO REACT OF THE PRESENCE OIF WATER WITH SAID GASEOUS ACID-FORMING CONSTITUENTS TO FROM THE CORRESPONDING ACID SALT THEREOF IS CONSTINUOUSLY PASSED IN COUNTERCURRENT AND RECIRCULATED THROUGH THE PASSING GAS SO AS TO REMOVE A PORTION OF SAID GASEOUS ACID-FORMING CONSTITUENTS FROM SAID GAS AND FROM THE CORRESPONDING AMMONIUM ACID SALT THEREOF; PASSING SAID GAS CONTAINING REMAINING GASEOUS ACID-FORMING CONSTITUENTS THROUGH A SUBSEQUENT SECOND STAGE OF THE GAS WASHER IN WHICH AN AQUEROUS AMMONIUM CURRENT AND RECIRCULATED THROUGH THE PASSING GAS AT A RATE CURRENT AND RECIRCULATED THROUGH THE PASSING GAS AT A RATE ADAPTED TO REMOVE SAID REMAINING GASEOUS ACID-FOARMING CONSTITUENTS FROM SAID GAS WHILE SAID GAS PASSES THROUGH SAID SECOND STAGE OF THE GAS WASHERS SO AS TO FROM THE CORRESPONDING AMMONIUM SALT OF SAID ACID-FORMING CONSTITUENTS, THUS REMOVING SAID REMAING ACID-FORMING CONSTITUENTS FROM SAID GAS AND OBTAINING A DEACIDIFIED GAS; PASSING SAID AMMONIUM SALT OF SAID ACID-FORMING CONSTITUENTS FORMED IN SAID SECOND STAGE OF THE GAS WASHER TO SAID FIRST STAGE OF THE GAS WASHER FOR REACTION WHEREIN WITH ADDITIONAL GASEOUS ACID-FORMING CONSTITUENTS TO FORM THE CORRESPONDING AMMONIUM ACID SALT THEREOF; WITHDRAWING AT LEAST A PORTION OF SAID AMMONIUM ACID SALT IN THE AQUEOUS SOLUTION FROM SAID FIRST STAGE OF THE GAS WASHER; REGENERATING SAID AMMONIUM ACID SALT TO AMMONIUM HYDROXIDE AND SAID GASEOUS ACID FORMING CONSTITUENTS; AND RECIRCULATING THE THUS REGENERATED AMMONIUM HYDROXIDE TO SAID SECOND STAGE OF THE GAS WASHER.
Claim 2
Independent Claim
305 words
A METHOD OF REMOVING ACID CONSTITUENTS SELECTED FROM THE GROUP CONSISTING OF CARBON DIOXIDE AND HYDROGEN SULFIDE FROM A GAS CONTAINING THE SAME DURING PASSAGE THEREOF THROUGH A GAS WASHER, COMPRISING THE STEPS OF PASSING A GAS CONTAINING GASEOUS ACID-FORMING CONSTITUENTS SELECTED FROM THE GROUP CONSISTING OF CARBON DIOXIDE AND HYDROGEN SULFIDE THROUGH A FIRST STAGE OF THE GAS WASHER IN WHICH AN AQUEOUS SOLUTION OF AN AMMONIUM SALT ADAPTED TO REACT OF THE PRESENCE OIF WATER WITH SAID GASEOUS ACID-FORMING CONSTITUENTS TO FROM THE CORRESPONDING ACID SALT THEREOF IS CONSTINUOUSLY PASSED IN COUNTERCURRENT AND RECIRCULATED THROUGH THE PASSING GAS SO AS TO REMOVE A PORTION OF SAID GASEOUS ACID-FORMING CONSTITUENTS FROM SAID GAS AND FROM THE CORRESPONDING AMMONIUM ACID SALT THEREOF; PASSING SAID GAS CONTAINING REMAINING GASEOUS ACID-FORMING CONSTITUENTS THROUGH A SUBSEQUENT SECOND STAGE OF THE GAS WASHER IN WHICH AN AQUEROUS AMMONIUM CURRENT AND RECIRCULATED THROUGH THE PASSING GAS AT A RATE CURRENT AND RECIRCULATED THROUGH THE PASSING GAS AT A RATE ADAPTED TO REMOVE SAID REMAINING GASEOUS ACID-FOARMING CONSTITUENTS FROM SAID GAS WHILE SAID GAS PASSES THROUGH SAID SECOND STAGE OF THE GAS WASHERS SO AS TO FROM THE CORRESPONDING AMMONIUM SALT OF SAID ACID-FORMING CONSTITUENTS, THUS REMOVING SAID REMAING ACID-FORMING CONSTITUENTS FROM SAID GAS AND OBTAINING A DEACIDIFIED GAS; PASSING SAID AMMONIUM SALT OF SAID ACID-FORMING CONSTITUENTS FORMED IN SAID SECOND STAGE OF THE GAS WASHER TO SAID FIRST STAGE OF THE GAS WASHER FOR REACTION WHEREIN WITH ADDITIONAL GASEOUS ACID-FORMING CONSTITUENTS TO FORM THE CORRESPONDING AMMONIUM ACID SALT THEREOF; WITHDRAWING AT LEAST A PORTION OF SAID AMMONIUM ACID SALT IN THE AQUEOUS SOLUTION FROM SAID FIRST STAGE OF THE GAS WASHER; REGENERATING SAID AMMONIUM ACID SALT TO AMMONIUM HYDROXIDE AND SAID GASEOUS ACID FORMING CONSTITUENTS; AND RECIRCULATING THE THUS REGENERATED AMMONIUM HYDROXIDE TO SAID SECOND STAGE OF THE GAS WASHER.
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1962-03-16 | 1962-09-15 | 1963-03-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1966-03-16 | 1966-09-15 | 1967-03-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1970-03-16 | 1970-09-15 | 1971-03-17 | $7700.00 | Window Closed / Lapsed |