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US3891402A Expired / Lapsed US ⏱️ 0.0 years remaining

Transfer line burner system

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1973-06-25
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Granted: 1975-06-24
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Expires: 1993-06-25
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Abstract

Abstract Carbonaceous solids are heated by introducing a stream of such solids into a transfer line burner, injecting sufficient oxygencontaining gas into the burner at two or more separate points to burn a portion of the carbon and generate heat, controlling distribution of the oxygen-containing gas to maintain temperatures below the ash fusion temperature and convert carbon monoxide to carbon dioxide, and withdrawing heated solids from the burner.

Inventors

  • 👤 Nicholas C Nahas
  • 👤 Edward L Wilson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 22:04
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/72; C10J3/723; C10J3/46; C10J3/48; C10J3/482; C10J3/54; C10J3/78; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0946; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/0973; C10J2300/0976; C10J2300/16; C10J2300/1603; C10J2300/1606; C10J2300/18; C10J2300/1807

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 227 words
IN A PROCESS WHEREIN A SOLIDS STREAM CONSISTING ESSENTIALLY OF CARBONACEOUS PARTICLES WITHDRW FROM A FLUIDIZED BED REACTORS IS CONTACTED WITH AN OXYGEN-CONTAINING GAS IN A TRANSFER LINE BURNER TO BURN CARBON PRESENT IN SAID PARTICLES AND RAISE THE TEMPERATURE OF SAID STREAM, WHEREIN HEATED PARTICLES AND COMBUSTION GASES CONTAINING CARBON MONOXIDE ARE WITHDRAW OVERHEAD FROM SAID TRANSFER LINE BURNER, AND WHEREIN SAID HEATED PARICLES ARE SEPARATED FROM SAID COMBUSTION GASES AND RETURNED TO SAID FLUIDIZED BED REACTOR; THE IMPROVEMENT WHICH COMPRISES INTRODUCING A FIRST STREAM OF OXYGEN-CONTAINING GAS INTO SAID TRANSFER LINE BURNER AT A POINT NEAR THE LOWER END THEREOF IN A QUANTITY SUFFICIENT TO INITATE THE COMBUSTION OF CARBON IN SAID PARTICLES INTRODUCING ADDITIONAL OXYGEN-CONTAINING GAS INTO SAID BURNER AT A SECOND POINT NEAR THE LOWER END OF SAID BURNER IN A QUANTITY SUFFICIENT TO BURN CARBON MONOXIDE PRESENT IN THE COMBUSTION GASES REACHING SAID SECOND POINT AND GENERATE ADDITIONAL HEAT, MONITORING THE CARBON MONOXIDE CONTENT OF THE COMBUSTION GASES WITHDRAWN FROM SAID BURNER, REGULATING THE RELATIVE QUANTITIES OF OXYGEN-CONTAINING GAS INTRODUCED INTO SAID BURNER AT SAID FIRST POINT AND SAID SECOND POINT IN RESPONSE TO CHANGES IN THE CARBON MONOXIDE CONTENT OF SAID COMBUSTION GASES WITHDRAWN FROM SAID BURNER, AND CONTROLLING THE TOTAL AMOUNT OF OXYGEN-CONTAINING GAS INTRODUCED INTO SAID BURNER IN RESPONSE TO CHANGES IN THE TEMPERATURE IN SAID FLUIDIZED BED REACTOR.
Claim 2
Dependent Claim 227 words
IN A PROCESS WHEREIN A SOLIDS STREAM CONSISTING ESSENTIALLY OF CARBONACEOUS PARTICLES WITHDRW FROM A FLUIDIZED BED REACTORS IS CONTACTED WITH AN OXYGEN-CONTAINING GAS IN A TRANSFER LINE BURNER TO BURN CARBON PRESENT IN SAID PARTICLES AND RAISE THE TEMPERATURE OF SAID STREAM, WHEREIN HEATED PARTICLES AND COMBUSTION GASES CONTAINING CARBON MONOXIDE ARE WITHDRAW OVERHEAD FROM SAID TRANSFER LINE BURNER, AND WHEREIN SAID HEATED PARICLES ARE SEPARATED FROM SAID COMBUSTION GASES AND RETURNED TO SAID FLUIDIZED BED REACTOR; THE IMPROVEMENT WHICH COMPRISES INTRODUCING A FIRST STREAM OF OXYGEN-CONTAINING GAS INTO SAID TRANSFER LINE BURNER AT A POINT NEAR THE LOWER END THEREOF IN A QUANTITY SUFFICIENT TO INITATE THE COMBUSTION OF CARBON IN SAID PARTICLES INTRODUCING ADDITIONAL OXYGEN-CONTAINING GAS INTO SAID BURNER AT A SECOND POINT NEAR THE LOWER END OF SAID BURNER IN A QUANTITY SUFFICIENT TO BURN CARBON MONOXIDE PRESENT IN THE COMBUSTION GASES REACHING SAID SECOND POINT AND GENERATE ADDITIONAL HEAT, MONITORING THE CARBON MONOXIDE CONTENT OF THE COMBUSTION GASES WITHDRAWN FROM SAID BURNER, REGULATING THE RELATIVE QUANTITIES OF OXYGEN-CONTAINING GAS INTRODUCED INTO SAID BURNER AT SAID FIRST POINT AND SAID SECOND POINT IN RESPONSE TO CHANGES IN THE CARBON MONOXIDE CONTENT OF SAID COMBUSTION GASES WITHDRAWN FROM SAID BURNER, AND CONTROLLING THE TOTAL AMOUNT OF OXYGEN-CONTAINING GAS INTRODUCED INTO SAID BURNER IN RESPONSE TO CHANGES IN THE TEMPERATURE IN SAID FLUIDIZED BED REACTOR.
Claim 3
Dependent Claim 77 words
A process as defined by claim 1 wherein said carbon monoxide content of said combustion gases is monitored by continually sampling said gases and analyzing the gas samples for carbon monoxide and wherein the relative amounts of oxygen-containing gas introduced at said first and said second points are regulated by varying the amount of oxygen-containing gas supplied to said burner at said second point in response to changes in the carbon monoxide content of said gas samples.
Claim 4
Dependent Claim 28 words
A process as defined by claim 1 wherein oxygen-containing gas is also introduced into said burner at at least one point intermediate said first and said second points.
Claim 5
Dependent Claim 40 words
A process as defined by claim 1 wherein said oxygen-containing gas is introduced into said burner at said second point in a quantity in excess of that required to burn essentially all of the carbon monoxide reaching said second point.
Claim 6
Dependent Claim 33 words
A process as defined by claim 1 wherein said oxygen-containing gas is introduced into said burner at each of said points through a plurality of nozzles spaced about the periphery of said burner.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-06-23 1978-12-23 1979-06-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-06-23 1982-12-23 1983-06-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-06-23 1986-12-23 1987-06-24 $7700.00 Window Closed / Lapsed

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