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.