Patent US2865864A successfully refreshed from Google Patents.
← Back to Patent Explorer
US2865864A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of ammonia synthesis feed gas

Assignee: Texaco Inc
•
Filing: 1955-08-19
•
Granted: 1958-12-23
•
Expires: 1975-08-19
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

No abstract record available.

Inventors

  • 👤 Eastman Du Bois
  • 👤 Roger M Dille
  • 👤 Ronald W Chapman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 20:57
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04521; C; C01; C01B; C01B3/00; C01B3/02; C01B3/025; F25J3/0204; F25J3/0219; F25J3/0223; F25J3/0228; F25J3/0276; F25J3/04527; F25J3/04539; F25J3/04563; F25J3/04587; F25J2205/00; F25J2205/30; F25J2210/00; F25J2210/12; F25J2210/42

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 233 words
A PROCESS FOR THE PRODUCTION OF A MIXTURE OF HYDROGEN AND NITROGEN IN PREDETERMINED PROPORTIONS COMPRISING SUBJECTING AIR TO LIQUEFACTION AND RECTIFICATION PRODUCING AN OXYGEN-RICH FRACTION CONTAINING ARGON AND A NITROGEN FRACTION SUBSTANTIALLY FREE FROM OXYGEN AND ARGON; REACTING A CARBONACEOUS FUEL WITH SAID OXYGEN-RICH FRACTION IN A GAS GENERATION ZONE UNDER CONDITIONS OF PARTIAL COMBUSTION PRODUCING CARBON MONOXIDE AND HYDROGEN AS THE PRINCIPAL PRODUCTS OF REACTION AND YIELDING A PRODUCT GAS COMPRISING CARBON MONOXIDE, HYDROGEN, ARGON, AND METHANE; CONVERTING SAID CARBON MONOXIDE TO CARBON DIOXIDE WITH CONCOMITANT PRODUCTION OF HYDROGEN BY REACTION WITH STEAM IN A WATER GAS SHIFT REACTION ZONE; SEPARATING CARBON DIOXIDE AND WATER FROM THE EFFLUENT OF SAID WATER GAS SHIFT REACTION ZONE FORMING A HYDROGEN-RICH GAS STREAM CONTAINING MINOR AMOUNTS OF METHANE, NITROGEN, AND ARGON; COOLING SAID HYDROGEN-RICH GAS STREAM TO A TEMPERATURE BELOW THE FREEZING POINT OF METHANE AND CONTACTING SAID GAS STREAM WITH SAID NITROGEN FRACTION IN LIQUID PHASE CONDENSING METHANE AND ARGON FROM SAID GAS STREAM; SEPARATING A GASEOUS MIXTURE OF NITROGEN AND HYDROGEN SUBSTANTIALLY COMPLETELY FREE FROM OTHER CONSTITUENTS FROM THE LIQUID FRACTION COMPRISING NITROGEN, ARGON, AND METHANE; AND VAPORIZING AND RETURNING A SUFFICIENT AMOUNT OF SAID LIQUID FRACTION TO SAID GAS GENERATION ZONE TO MAINTAIN THE CONCENTRATION OF ARGON IN SAID HYDROGENRICH GAS STREAM AT LEAST EQUAL TO THE CONCENTRATION REQUIRED TO PREVENT FREEZING OF METHANE AND EFFECTIVE TO SATISFY THE FOLLOWING FORMULA:
Claim 2
Dependent Claim 233 words
A PROCESS FOR THE PRODUCTION OF A MIXTURE OF HYDROGEN AND NITROGEN IN PREDETERMINED PROPORTIONS COMPRISING SUBJECTING AIR TO LIQUEFACTION AND RECTIFICATION PRODUCING AN OXYGEN-RICH FRACTION CONTAINING ARGON AND A NITROGEN FRACTION SUBSTANTIALLY FREE FROM OXYGEN AND ARGON; REACTING A CARBONACEOUS FUEL WITH SAID OXYGEN-RICH FRACTION IN A GAS GENERATION ZONE UNDER CONDITIONS OF PARTIAL COMBUSTION PRODUCING CARBON MONOXIDE AND HYDROGEN AS THE PRINCIPAL PRODUCTS OF REACTION AND YIELDING A PRODUCT GAS COMPRISING CARBON MONOXIDE, HYDROGEN, ARGON, AND METHANE; CONVERTING SAID CARBON MONOXIDE TO CARBON DIOXIDE WITH CONCOMITANT PRODUCTION OF HYDROGEN BY REACTION WITH STEAM IN A WATER GAS SHIFT REACTION ZONE; SEPARATING CARBON DIOXIDE AND WATER FROM THE EFFLUENT OF SAID WATER GAS SHIFT REACTION ZONE FORMING A HYDROGEN-RICH GAS STREAM CONTAINING MINOR AMOUNTS OF METHANE, NITROGEN, AND ARGON; COOLING SAID HYDROGEN-RICH GAS STREAM TO A TEMPERATURE BELOW THE FREEZING POINT OF METHANE AND CONTACTING SAID GAS STREAM WITH SAID NITROGEN FRACTION IN LIQUID PHASE CONDENSING METHANE AND ARGON FROM SAID GAS STREAM; SEPARATING A GASEOUS MIXTURE OF NITROGEN AND HYDROGEN SUBSTANTIALLY COMPLETELY FREE FROM OTHER CONSTITUENTS FROM THE LIQUID FRACTION COMPRISING NITROGEN, ARGON, AND METHANE; AND VAPORIZING AND RETURNING A SUFFICIENT AMOUNT OF SAID LIQUID FRACTION TO SAID GAS GENERATION ZONE TO MAINTAIN THE CONCENTRATION OF ARGON IN SAID HYDROGENRICH GAS STREAM AT LEAST EQUAL TO THE CONCENTRATION REQUIRED TO PREVENT FREEZING OF METHANE AND EFFECTIVE TO SATISFY THE FOLLOWING FORMULA:

References Cited (Backward Citations)

US1957744A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1961-12-22 1962-06-23 1962-12-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1965-12-22 1966-06-23 1966-12-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1969-12-22 1970-06-23 1970-12-23 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag