Patent US3176444A successfully refreshed from Google Patents.
US3176444A
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US
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Adsorption separation process
Assignee: Union Carbide Corp
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Filing: 1962-09-04
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Granted: 1965-04-06
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Expires: 1982-09-04
Abstract
No abstract record available.
Inventors
- 👤 Kiyonaga Kazuo
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 17:12
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; C; C01; C01B; C01B13/00; C01B13/02; C01B13/0229; C01B13/0248; C01B13/0259; C01B23/00; C01B3/00; C01B3/50; C01B3/56; C10; C10G; C10G25/00; C10G25/02; C10G25/03; B01D2253/00; B01D2253/10; B01D2253/102; B01D2253/104; B01D2253/106; B01D2253/108; B01D2256/00; B01D2256/10; B01D2256/12; B01D2256/16; B01D2256/18; B01D2256/24; B01D2256/245; B01D2257/00; B01D2257/10; B01D2257/102; B01D2257/104; B01D2257/108; B01D2257/11; B01D2257/40; B01D2257/406; B01D2257/50; B01D2257/502; B01D2257/504; B01D2257/70; B01D2257/702; B01D2257/80; B01D2259/00; B01D2259/40; B01D2259/40001; B01D2259/40011; B01D2259/40028; B01D2259/4003; B01D2259/40043; B01D2259/4005; B01D2259/40052; B01D2259/40077; B01D2259/40081; B01D2259/403; B01D2259/404; B01D2259/414; B01D2259/4141; B01D2259/4145; B01D2259/4146; B01D2259/65; C01B2203/00; C01B2203/04; C01B2203/042; C01B2203/043; C01B2203/0465; C01B2203/047; C01B2203/0475; C01B2203/048; C01B2203/0485; C01B2203/0495; C01B2210/00; C01B2210/0043; C01B2210/0046; Y; Y02; Y02C; Y02C20/00; Y02C20/40; Y02P; Y02P20/00; Y02P20/151
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
263 words
A PROCESS FOR PURIFYING A FLUID STREAM WHICH COMPRISES PROVIDING A FEED FLUID STREAM CONTAINING AN ADMIXTURE OF IMPURITY AND PRODUCT FLUID; PROVIDING AN ADSORPTION ZONE HAVING AN INLET AND A DISCHARGE END AND CONTAINING THEREIN A BED OF ADSORBENT PARTICLES CAPABLE OF SELECTIVELY ADSORBING SAID IMPURITY FROM SAID FEED FLUID STREAM, SAID BED HAVING VOIDS BETWEEN THE ADSORBENT PARTICLES; INTRODUCING SAID FEED FLUID STREAM TO SAID INLET END OF SAID ADSORPTION ZONE AND CONTACTING SUCH STREAM WITH SAID BED AT A FIRST HIGHER PRESSURE THEREBY ADSORBING SAID IMPURITY WITHIN SAID BED AND TRAPPING PART OF SAID FEED FLUID IN SAID VOIDS; CONTINUOUSLY DISCHARGING AN IMPURITY-DEPLETED PRODUCT FLUID STREAM FROM SAID ADSORPTION ZONE DISCHARGE END AT SUBSTANTIALLY SAID FIRST HIGHER PRESSURE DURING THE INTRODUCTION OF SAID FEED FLUID STREAM TO THE ADSORPTION ZONE INLET END; ESTABLISHING AN IMPURITY ADSORPTION FRONT AT SAID INLET END OF SAID ADSORPTION ZONE; PROGRESSIVELY MOVING SUCH FRONT LONGITUDINALLY THROUGH SAID ADSORPTION ZONE TOWARD SAID DISCHARGE END TO A PREDETERMINED LOCATION WITHIN SAID ADSORPTION ZONE; TERMINATING THE INTRODUCTION OF SAID FEED FLUID STREAM AT SAID FIRST HIGHER PRESSURE TO SAID INLET END OF SAID ADSORPTION ZONE; REMOVING AT LEAST MOST OF THE TRAPPED PRODUCT FLUID COMPONENT OF THE FEED FLUID IN SAID VOIDS THROUGH SAID DISCHARGE END OF SAID ADSORPTION ZONE AS A SEPARATE FLUID STREAM THEREBY COCURRENTLY DEPRESSURIZING SAID ADSORPTION ZONE FROM SAID FIRST HIGHER PRESSURE TO A SECOND LOWER PRESSURE AND THEREBY FURTHER MOVING SAID IMPURITY ADSORPTION FRONT TOWARD SAID DISCHARGE END OF SAID ADSORPTION ZONE; AND THEREAFTER DESORBING SAID ADSORPTION ZONE TO REMOVE SAID IMPURITY THEREFROM.
Claim 2
Dependent Claim
263 words
A PROCESS FOR PURIFYING A FLUID STREAM WHICH COMPRISES PROVIDING A FEED FLUID STREAM CONTAINING AN ADMIXTURE OF IMPURITY AND PRODUCT FLUID; PROVIDING AN ADSORPTION ZONE HAVING AN INLET AND A DISCHARGE END AND CONTAINING THEREIN A BED OF ADSORBENT PARTICLES CAPABLE OF SELECTIVELY ADSORBING SAID IMPURITY FROM SAID FEED FLUID STREAM, SAID BED HAVING VOIDS BETWEEN THE ADSORBENT PARTICLES; INTRODUCING SAID FEED FLUID STREAM TO SAID INLET END OF SAID ADSORPTION ZONE AND CONTACTING SUCH STREAM WITH SAID BED AT A FIRST HIGHER PRESSURE THEREBY ADSORBING SAID IMPURITY WITHIN SAID BED AND TRAPPING PART OF SAID FEED FLUID IN SAID VOIDS; CONTINUOUSLY DISCHARGING AN IMPURITY-DEPLETED PRODUCT FLUID STREAM FROM SAID ADSORPTION ZONE DISCHARGE END AT SUBSTANTIALLY SAID FIRST HIGHER PRESSURE DURING THE INTRODUCTION OF SAID FEED FLUID STREAM TO THE ADSORPTION ZONE INLET END; ESTABLISHING AN IMPURITY ADSORPTION FRONT AT SAID INLET END OF SAID ADSORPTION ZONE; PROGRESSIVELY MOVING SUCH FRONT LONGITUDINALLY THROUGH SAID ADSORPTION ZONE TOWARD SAID DISCHARGE END TO A PREDETERMINED LOCATION WITHIN SAID ADSORPTION ZONE; TERMINATING THE INTRODUCTION OF SAID FEED FLUID STREAM AT SAID FIRST HIGHER PRESSURE TO SAID INLET END OF SAID ADSORPTION ZONE; REMOVING AT LEAST MOST OF THE TRAPPED PRODUCT FLUID COMPONENT OF THE FEED FLUID IN SAID VOIDS THROUGH SAID DISCHARGE END OF SAID ADSORPTION ZONE AS A SEPARATE FLUID STREAM THEREBY COCURRENTLY DEPRESSURIZING SAID ADSORPTION ZONE FROM SAID FIRST HIGHER PRESSURE TO A SECOND LOWER PRESSURE AND THEREBY FURTHER MOVING SAID IMPURITY ADSORPTION FRONT TOWARD SAID DISCHARGE END OF SAID ADSORPTION ZONE; AND THEREAFTER DESORBING SAID ADSORPTION ZONE TO REMOVE SAID IMPURITY THEREFROM.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1968-04-05 | 1968-10-05 | 1969-04-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1972-04-05 | 1972-10-05 | 1973-04-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1976-04-05 | 1976-10-05 | 1977-04-06 | $7700.00 | Window Closed / Lapsed |