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US2602809A Expired / Lapsed US ⏱️ 0.0 years remaining

Treatment of solid carbon containing materials to produce carbon monoxide for the synthesis of organic materials

Assignee: MW Kellogg Co
•
Filing: 1948-07-10
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Granted: 1952-07-08
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Expires: 1968-07-10
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Abstract

No abstract record available.

Inventors

  • 👤 Norman L Dickinson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 23:17
CPC Classifications
C; C10; C10G; C10G2/00; C10G2/30; C10G2/32; B; B01; B01J; B01J8/00; B01J8/18; B01J8/24; B01J8/26; C10J; C10J3/00; C10J3/46; C10J3/48; C10J3/482; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0933; Y; Y10; Y10S; Y10S48/00; Y10S48/04

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 361 words
A CONTINUOUS PROCESS FOR PRODUCING A GAS RICH IN HYDROGEN AND CARBON MONOXIDE WHICH COMPRISES PASSING A GASIFORM FLUID SUBSTANTIALLY FREE FROM FREE OXYGEN UPWARDLY IN A FIRST REACTION ZONE THROUGH A MASS COMPRISING FINELY-DIVIDED REDUCIBLE METAL OXIDE AND COAL AT A VELOCITY SUFFICIENT TO MAINTAIN SAID MASS IN A PSEUDO-LIQUID FLUIDIZED CONDITION, MAINTAINING SAID FIRST REACTION ZONE AT A TEMPERATURE SUCH THAT CARBON IS OXIDIZED TO CARBON MONOXIDE AS THE PRINCIPAL REACTION BY THE REDUCTION OF SAID METAL OXIDE, SAID REDUCIBLE METAL OXIDE BEING THE PRINCIPAL SOURCE OF OXYGEN FOR THE OXIDATION OF SAID CARBON TO CARBON MONOXIDE, SEPARATELY WITHDRAWING FROM SAID FIRST REACTION ZONE FINELY-DIVIDED REDUCED METAL OXIDE AND AN EFFLUENT COMPRISING CARBON MONOXIDE, PASSING A PORTION OF SAID WITHDRAWN REDUCED METAL OXIDE TO A SECOND REACTION ZONE, PASSING STEAM UPWARDLY IN SAID SECOND REACTION ZONE THROUGH A MASS COMPRISING FINELY-DIVIDED REDUCED METAL OXIDE AT A VELOCITY SUFFICIENT TO MAINTAIN SAID MASS IN A PSEUDO-LIQUID FLUIDIZED CONDITION, MAINTAINING SAID SECOND REACTION ZONE AT A TEMPERATURE SUCH THAT SAID REDUCED METAL OXIDE IS REOXIDIZED BY REACTION WITH STEAM TO PRODUCE HYDROGEN AS THE PRINCIPAL REACTION, THE COMBINED REACTIONS OF SAID FIRST AND SAID SECOND REACTION ZONES BEING ENDOTHERMIC, SEPARATELY WITHDRAWING FROM SAID SECOND REACTION ZONE FINELY-DIVIDED REOXIDIZED METAL OXIDE AND AN EFFLUENT COMPRISNG HYDROGEN, COMBINING THE EFFLUENT FROM SAID FIRST REACTION ZONE WITH THE EFFLUENT FROM SAID SECOND REACTION ZONE TO FORM A GASEOUS MIXTURE COMPRISING HYDROGEN AND CARBON MONOXIDE AS THE PRODUCT OF THE PROCESS, PASSING ANOTHER PORTION OF SAID REDUCED METAL OXIDE FROM SAID FIRST REACTION ZONE TO A THIRD REACTION ZONE, PASSING AIR UPWARDLY IN SAID THIRD REACTION ZONE THROUGH A MASS COMPRISING FINELY-DIVIDED REDUCED METAL OXIDE AT A VELOCITY SUFFICIENT TO MAINTAIN SAID MASS IN A PSEUDO-LIQUID FLUIDIZED CONDITION WHEREBY SAID REDUCED METAL OXIDE IS REOXIDIZED AT A TEMPERATURE ABOE THAT MAINTAINED IN BOTH OF SAID FIRST AND SAID SECOND REACTION ZONES AND HEAT IS LIBERATED, AND WITHDRAWING REOXIDIZED METAL OXIDE AT A RELATIVELY HIGH TEMPERATURE FROM SAID THIRD REACTION ZONE AND PASSING SAME TO SAID FIRST REACTION ZONE AT A TEMPERATURE ABOVE THE TEMPERATURE LEVEL MAINTAINED THEREIN AS MEANS FOR SUPPLYING HEAT OF REACTION THERETO.
Claim 2
Dependent Claim 361 words
A CONTINUOUS PROCESS FOR PRODUCING A GAS RICH IN HYDROGEN AND CARBON MONOXIDE WHICH COMPRISES PASSING A GASIFORM FLUID SUBSTANTIALLY FREE FROM FREE OXYGEN UPWARDLY IN A FIRST REACTION ZONE THROUGH A MASS COMPRISING FINELY-DIVIDED REDUCIBLE METAL OXIDE AND COAL AT A VELOCITY SUFFICIENT TO MAINTAIN SAID MASS IN A PSEUDO-LIQUID FLUIDIZED CONDITION, MAINTAINING SAID FIRST REACTION ZONE AT A TEMPERATURE SUCH THAT CARBON IS OXIDIZED TO CARBON MONOXIDE AS THE PRINCIPAL REACTION BY THE REDUCTION OF SAID METAL OXIDE, SAID REDUCIBLE METAL OXIDE BEING THE PRINCIPAL SOURCE OF OXYGEN FOR THE OXIDATION OF SAID CARBON TO CARBON MONOXIDE, SEPARATELY WITHDRAWING FROM SAID FIRST REACTION ZONE FINELY-DIVIDED REDUCED METAL OXIDE AND AN EFFLUENT COMPRISING CARBON MONOXIDE, PASSING A PORTION OF SAID WITHDRAWN REDUCED METAL OXIDE TO A SECOND REACTION ZONE, PASSING STEAM UPWARDLY IN SAID SECOND REACTION ZONE THROUGH A MASS COMPRISING FINELY-DIVIDED REDUCED METAL OXIDE AT A VELOCITY SUFFICIENT TO MAINTAIN SAID MASS IN A PSEUDO-LIQUID FLUIDIZED CONDITION, MAINTAINING SAID SECOND REACTION ZONE AT A TEMPERATURE SUCH THAT SAID REDUCED METAL OXIDE IS REOXIDIZED BY REACTION WITH STEAM TO PRODUCE HYDROGEN AS THE PRINCIPAL REACTION, THE COMBINED REACTIONS OF SAID FIRST AND SAID SECOND REACTION ZONES BEING ENDOTHERMIC, SEPARATELY WITHDRAWING FROM SAID SECOND REACTION ZONE FINELY-DIVIDED REOXIDIZED METAL OXIDE AND AN EFFLUENT COMPRISNG HYDROGEN, COMBINING THE EFFLUENT FROM SAID FIRST REACTION ZONE WITH THE EFFLUENT FROM SAID SECOND REACTION ZONE TO FORM A GASEOUS MIXTURE COMPRISING HYDROGEN AND CARBON MONOXIDE AS THE PRODUCT OF THE PROCESS, PASSING ANOTHER PORTION OF SAID REDUCED METAL OXIDE FROM SAID FIRST REACTION ZONE TO A THIRD REACTION ZONE, PASSING AIR UPWARDLY IN SAID THIRD REACTION ZONE THROUGH A MASS COMPRISING FINELY-DIVIDED REDUCED METAL OXIDE AT A VELOCITY SUFFICIENT TO MAINTAIN SAID MASS IN A PSEUDO-LIQUID FLUIDIZED CONDITION WHEREBY SAID REDUCED METAL OXIDE IS REOXIDIZED AT A TEMPERATURE ABOE THAT MAINTAINED IN BOTH OF SAID FIRST AND SAID SECOND REACTION ZONES AND HEAT IS LIBERATED, AND WITHDRAWING REOXIDIZED METAL OXIDE AT A RELATIVELY HIGH TEMPERATURE FROM SAID THIRD REACTION ZONE AND PASSING SAME TO SAID FIRST REACTION ZONE AT A TEMPERATURE ABOVE THE TEMPERATURE LEVEL MAINTAINED THEREIN AS MEANS FOR SUPPLYING HEAT OF REACTION THERETO.
Claim 3
Dependent Claim 81 words
THE PROCESS OF CLAIM 11 IN WHICH SAID GASEOUS MIXTURE OF HYDROGEN AND CARBON MONOXIDE IS PASSED TO A FOURTH REACTION ZONE IN WHICH HYDROGEN AND CARBON MONOXIDE ARE CONVERTED TO ORGANIC COMPOUNDS INCLUDING METHANE, REMOVING AN EFFLUENT FROM SAID FOURTH REACTION ZONE COMPRISING UNREACTED HYDROGEN, METHANE AND HIGHER BOILING ORGANIC COMPOUNDS, SEPARATING UNREACTED HYDROGEN AND METHANE FROM SAID EFFLUENT, AND PASSING SAID UNREACTED HYDROGEN AND METHANE TO SAID FIRST REACTION ZONE AS AT LEAST A PORTION OF THE GASIFORM FLUID.

References Cited (Backward Citations)

GB190008239A Cited
US1969264A Cited
US2449635A Cited
US2400075A Cited
US2507502A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1955-07-08 1956-01-07 1956-07-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1959-07-08 1960-01-07 1960-07-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1963-07-08 1964-01-07 1964-07-08 $7700.00 Window Closed / Lapsed

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