Patent US3203193A successfully refreshed from Google Patents.
US3203193A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of nitrogen
Assignee: Petrocarbon Developments Ltd
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Filing: 1963-02-06
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Granted: 1965-08-31
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Expires: 1983-02-06
Abstract
No abstract record available.
Inventors
- 👤 Ruhemann Martin Siegfr William
- 👤 Seddon William Leslie
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 15:17
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/044; F25J3/04151; F25J3/04187; F25J3/04193; F25J3/04248; F25J3/04284
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
331 words
A PROCESS FOR PRODUCING HIGHLY PURE NITROGEN AT A SUBSTANTIAL SUPERATMOSPHERIC PRESSURE FROM AIR WHICH HAS BEEN COMPRESSED TO ABOUT SAID SUPERATMOSPHERIC PRESSURE AND FROM WHICH CO2 AND MOISTURE HAVE BEEN REMOVED, COMPRISING THE STEPS OF: (A) COOLING SAID AIR AT ABOUT SAID SUPERATMOSPHERIC PRESSURE TO A TEMPERATURE AT WHICH A MINOR PART OF SAID AIR IS LIQUEFIED; (B) SUPPLYING THE RESULTING PARTIALLY LIQUEFIED AIR TO THE BASE OF A SINGLE FRACTIONING COLUMN HAVING A CONDENSER FOR PROVIDING REFLUX AT THE UPPER END THEREOF AND OPERATING AT ABOUT SAID SUPERATMOSPHERIC PRESSURE; (C) SEPARATING SAID SUPPLIED AIR IN SAID COLUMN INTO A HIGHLY PURE NITROGEN GAS AS OVERHEAD PRODUCT AND AN OXYGEN-ENRICHED LIQUID AIR AS BOTTOMS PRODUCT; (D) WITHDRAWING SAID OXYGEN-ENRICHED LIQUID AIR FROM THE BOTTOM OF SAID COLUMN AND EXPANDING THE SAME TO A PRESSURE INTERMEDIATE SAID SUPERATMOSPHERIC PRESSURE AND ATMOSPHERIC PRESSURE; (E) PASSING SAID EXPANDED OXYGEN-ENRICHED LIQUID AIR THROUGH SAID CONDENSER IN INDIRECT HEAT EXCHANGE WITH THE NITROGEN GAS SEPARATED IN THE UPPER END OF SAID COLUMN WHEREBY SAID OXYGEN-ENRICHED LIQUID AIR IS EVAPORATED IN SAID CONDENSER INCONDENSING NITROGEN GAS TO PROVIDE REFLUX FOR SAID COLUMN; (F) WITHDRAWING SAID EVAPORATED OXYGEN-ENRICHED LIQUID AIR FROM SAID CONDENSER AND PASSIGN THE SAME IN INDIRECT HEAT EXCHANGE WITH INCOMING AIR TO COOL SAID INCOMING AIR AND WARM SAID EVAPORATED OXYGENENRICHED LIQUID AIR; (G) THEN EXPANDING AT LEAST A PART OF SAID WARMED OXYGEN-ENRICHED AIR TO A PRESSURE CLOSE TO ATMOSPHERIC PRESSURE IN AN EXPANSION TURBINE THEREBY TO PRODUCE COLD FOR USE IN SAID PROCESS; (H) UTILIZING THE OXYGEN-ENRICHED AIR AT CLOSE TO ATMOSPHERIC PRESSURE TO COOL INCOMING AIR BY INDIRECT HEAT EXCHANGE AND THEN VENTING IT FROM THE PROCESS; (I) WITHDRAWING GASEOUS NITROGEN PRODUCT FROM THE TOP OF SAID COLUMN; (J) PASSING AT LEAST A PART OF SAID WITHDRAWN GASEOUS NITROGEN PRODUCT IN INDIRECT HEAT EXCHANGE WITH INCOMING AIR TO COL SAID INCOMING AIR; AND (K) THEN COLLECTING AT LEAST SAID PART OF SAID WITHDRAWN GASEOUS NTIROGEN PRODUCT AT SUBSTANTIALLY SAID SUPERATMOSPHERIC PRESSURE.
Claim 2
Dependent Claim
331 words
A PROCESS FOR PRODUCING HIGHLY PURE NITROGEN AT A SUBSTANTIAL SUPERATMOSPHERIC PRESSURE FROM AIR WHICH HAS BEEN COMPRESSED TO ABOUT SAID SUPERATMOSPHERIC PRESSURE AND FROM WHICH CO2 AND MOISTURE HAVE BEEN REMOVED, COMPRISING THE STEPS OF: (A) COOLING SAID AIR AT ABOUT SAID SUPERATMOSPHERIC PRESSURE TO A TEMPERATURE AT WHICH A MINOR PART OF SAID AIR IS LIQUEFIED; (B) SUPPLYING THE RESULTING PARTIALLY LIQUEFIED AIR TO THE BASE OF A SINGLE FRACTIONING COLUMN HAVING A CONDENSER FOR PROVIDING REFLUX AT THE UPPER END THEREOF AND OPERATING AT ABOUT SAID SUPERATMOSPHERIC PRESSURE; (C) SEPARATING SAID SUPPLIED AIR IN SAID COLUMN INTO A HIGHLY PURE NITROGEN GAS AS OVERHEAD PRODUCT AND AN OXYGEN-ENRICHED LIQUID AIR AS BOTTOMS PRODUCT; (D) WITHDRAWING SAID OXYGEN-ENRICHED LIQUID AIR FROM THE BOTTOM OF SAID COLUMN AND EXPANDING THE SAME TO A PRESSURE INTERMEDIATE SAID SUPERATMOSPHERIC PRESSURE AND ATMOSPHERIC PRESSURE; (E) PASSING SAID EXPANDED OXYGEN-ENRICHED LIQUID AIR THROUGH SAID CONDENSER IN INDIRECT HEAT EXCHANGE WITH THE NITROGEN GAS SEPARATED IN THE UPPER END OF SAID COLUMN WHEREBY SAID OXYGEN-ENRICHED LIQUID AIR IS EVAPORATED IN SAID CONDENSER INCONDENSING NITROGEN GAS TO PROVIDE REFLUX FOR SAID COLUMN; (F) WITHDRAWING SAID EVAPORATED OXYGEN-ENRICHED LIQUID AIR FROM SAID CONDENSER AND PASSIGN THE SAME IN INDIRECT HEAT EXCHANGE WITH INCOMING AIR TO COOL SAID INCOMING AIR AND WARM SAID EVAPORATED OXYGENENRICHED LIQUID AIR; (G) THEN EXPANDING AT LEAST A PART OF SAID WARMED OXYGEN-ENRICHED AIR TO A PRESSURE CLOSE TO ATMOSPHERIC PRESSURE IN AN EXPANSION TURBINE THEREBY TO PRODUCE COLD FOR USE IN SAID PROCESS; (H) UTILIZING THE OXYGEN-ENRICHED AIR AT CLOSE TO ATMOSPHERIC PRESSURE TO COOL INCOMING AIR BY INDIRECT HEAT EXCHANGE AND THEN VENTING IT FROM THE PROCESS; (I) WITHDRAWING GASEOUS NITROGEN PRODUCT FROM THE TOP OF SAID COLUMN; (J) PASSING AT LEAST A PART OF SAID WITHDRAWN GASEOUS NITROGEN PRODUCT IN INDIRECT HEAT EXCHANGE WITH INCOMING AIR TO COL SAID INCOMING AIR; AND (K) THEN COLLECTING AT LEAST SAID PART OF SAID WITHDRAWN GASEOUS NTIROGEN PRODUCT AT SUBSTANTIALLY SAID SUPERATMOSPHERIC PRESSURE.
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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) | 1968-08-30 | 1969-03-01 | 1969-08-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1972-08-30 | 1973-03-01 | 1973-08-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1976-08-30 | 1977-03-01 | 1977-08-31 | $7700.00 | Window Closed / Lapsed |