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US3203193A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of nitrogen

Assignee: Petrocarbon Developments Ltd
•
Filing: 1963-02-06
•
Granted: 1965-08-31
•
Expires: 1983-02-06
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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 09:52
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.

References Cited (Backward Citations)

US1594336A Cited
US2040107A Cited
US2520862A Cited
US2626510A Cited
US2688238A Cited
US2850880A Cited
US3070966A Cited

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

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