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US3918930A Expired / Lapsed US ⏱️ 0.0 years remaining

Countercurrent catalytic contact of a reactant stream in a multiple-stage process and the apparatus therefor

Assignee: Universal Oil Products Co
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Filing: 1974-08-27
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Granted: 1975-11-11
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Expires: 1994-08-27
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Abstract

Abstract A unitary, multiple-stage reaction system for countercurrently contacting a fluid reactant stream with catalyst particles movable through the system via gravity-flow. The reaction zones, or stages, are vertically stacked in a single chamber wherein catalyst particles flow from one annular-form bed to the next lower annular-form bed. A first portion of the hydrocarbonaceous charge stock flows downwardly into the lowermost reaction zone, laterally (outward to inward flow) through the annular-form catalyst bed into a center reactant conduit, is admixed with the second portion of the charge stock, flows upwardly through the reactant conduit into the next upper zone and laterally (inward to outward flow) through the annular-form catalyst bed. A preferred embodiment involves three reaction zones within the reaction chamber, with heat-exchange provisions between the middle and upper zones.

Inventors

  • 👤 James T Forbes
  • 👤 James E Gantt

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 20:11
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/08; B01J8/12; B01J8/125; B01J8/02; B01J8/04; B01J8/0403; C; C10; C10G; C10G2400/00; C10G2400/26

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 213 words
A PROCESS FOR EFFECTING THE MULTIPLE-STAGE, COUNTERCURRENT CONTACT AND CONVERSION OF A HYDROCARBON REACTANT STREAM WITH HYDROCARBON CONVERSION CATALYST PARTICLES MOVABLE THROUGH SAID STAGES VIA GRAVITY-FLOW, WHICH PROCESS COMPRISES THE STEPS OF A. INTRODUCING A FIRST PORTION OF SAID REACANT STREAM INTO A REACTION CHAMBER, CONTAINING AT LEAST TOW VERTICALLY-DISPOSED REACTION ZONES, AT A LOCUS INTERMEDIATE SAID REACTION ZONES, B. PASSING SAID FIRST PORTION DOWNWARDLY THROUGH THE LOWER OF SAID REACTION ZONES AND FLOWING SAID PORTION LATERALLY, IN RADIAL FLOW, THROUGH A FIRST ANNULAR-FORM CATALYST BED, IN WHICH THE CATALYST PARTICLES ARE MOVABLE VIA GRAVITYFLOW, INTO A CENTER REACTANT CONDUIT, C. INTRODUCING A SECOND PORTION OF SAID REACTANT STREAM INTO THE LOWER EXTREMITY OF SAID CENTER REACANT CONDUIT, WITHIN SAID LOWER REACTION ZONE, D. INTRODUCING THE RESULTING MIXTURE OF SAID SECOND REACTANT STREAM PORTION AND THE REACTION PRODUCT OF SAID FIRST REACTANT STREAM PORTION INTO A CENTER REACTANT CONDUIT WITHIN THE UPPER OF SAID REACTION ZONES, E. PASSING SAID MIXTURE UPWARDLY THROUGH SAID UPPER REACTION ZONE AND FLOWING SAID MIXTURE LATERALLY, IN RADIAL FLOW, THROUGH A SECOND ANNULAR-FORM CATALYST BED, IN WHICH THE CATALYST PARTICLES ARE MOVABLE VIA GRAVITY-FLOW, INTO AN OUTER ANNULAR-FORM VOID VOLUME, AND, F. WITHDRAWING THE RESULTING CONVERTED REACTANT STREAM FROM AN UPPER PORTION OF SAID SECOND ANNULAR-FORM CATALYST BED.
Claim 2
Dependent Claim 213 words
A PROCESS FOR EFFECTING THE MULTIPLE-STAGE, COUNTERCURRENT CONTACT AND CONVERSION OF A HYDROCARBON REACTANT STREAM WITH HYDROCARBON CONVERSION CATALYST PARTICLES MOVABLE THROUGH SAID STAGES VIA GRAVITY-FLOW, WHICH PROCESS COMPRISES THE STEPS OF A. INTRODUCING A FIRST PORTION OF SAID REACANT STREAM INTO A REACTION CHAMBER, CONTAINING AT LEAST TOW VERTICALLY-DISPOSED REACTION ZONES, AT A LOCUS INTERMEDIATE SAID REACTION ZONES, B. PASSING SAID FIRST PORTION DOWNWARDLY THROUGH THE LOWER OF SAID REACTION ZONES AND FLOWING SAID PORTION LATERALLY, IN RADIAL FLOW, THROUGH A FIRST ANNULAR-FORM CATALYST BED, IN WHICH THE CATALYST PARTICLES ARE MOVABLE VIA GRAVITYFLOW, INTO A CENTER REACTANT CONDUIT, C. INTRODUCING A SECOND PORTION OF SAID REACTANT STREAM INTO THE LOWER EXTREMITY OF SAID CENTER REACANT CONDUIT, WITHIN SAID LOWER REACTION ZONE, D. INTRODUCING THE RESULTING MIXTURE OF SAID SECOND REACTANT STREAM PORTION AND THE REACTION PRODUCT OF SAID FIRST REACTANT STREAM PORTION INTO A CENTER REACTANT CONDUIT WITHIN THE UPPER OF SAID REACTION ZONES, E. PASSING SAID MIXTURE UPWARDLY THROUGH SAID UPPER REACTION ZONE AND FLOWING SAID MIXTURE LATERALLY, IN RADIAL FLOW, THROUGH A SECOND ANNULAR-FORM CATALYST BED, IN WHICH THE CATALYST PARTICLES ARE MOVABLE VIA GRAVITY-FLOW, INTO AN OUTER ANNULAR-FORM VOID VOLUME, AND, F. WITHDRAWING THE RESULTING CONVERTED REACTANT STREAM FROM AN UPPER PORTION OF SAID SECOND ANNULAR-FORM CATALYST BED.
Claim 3
Dependent Claim 76 words
The process of claim 1 further characterized in that said reaction chamber contains three annular-form, movable catalyst beds and (i) a heat-exchange fluid medium is introduced at a locus between the upper two of said catalyst beds, and (ii) the resulting mixture of said fluid medium and the converted reactant stream from the next lower annular-form catalyst bed flows upwardly into a center reactant conduit and laterally, in radial flow, through an annular-form third catalyst bed.
Claim 4
Dependent Claim 24 words
The process of claim 1 further characterized in that said reactant stream is a mixture of steam and a naphtha boiling range hydrocarbon fraction.
Claim 5
Dependent Claim 15 words
The process of claim 2 further characterized in that said heat-exchange fluid medium comprises methane.

References Cited (Backward Citations)

US2512562A Cited
US3837822A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-11-10 1979-05-12 1979-11-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-11-10 1983-05-12 1983-11-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-11-10 1987-05-12 1987-11-11 $7700.00 Window Closed / Lapsed

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