← Back to Patent Explorer
US2919240A Expired / Lapsed US ⏱️ 0.0 years remaining

Means for introducing lift gas to vertical catalyst riser within a reaction chamber

Assignee: MW Kellogg Co
•
Filing: 1956-02-29
•
Granted: 1959-12-29
•
Expires: 1976-02-29
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

No abstract record available.

Inventors

  • 👤 William J Degnen

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 05:48
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/0015; B01J8/0025; B01J8/18; B01J8/1818

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 277 words
A HYDROFORMING PROCESS WHICH COMPRISES CONTACTING A NAPHTHA FEED WITH A DENSE FLUIDIZED MASS OF FINELY DIVIDED SOLID REFORMING CATALYST IN A REACTION ZONE AT A PRESSURE OF AT LEAST ABOUT 30 P.S.I.G., THUS CONTAMINATING THE CATALYST WITH VOLATILE AND NON-VOLATILE HYDROCARBONACEOUS MATERIAL, WITHDRAWING THE CONTAMINATED CATALYST DIRECTLY FROM THE LOWER PORTION OF THE DENSE MASS OF FLUIDIZED CATALYST IN SAID REACATION ZONE AND PASSING THE SAME UPWARDLY AS A MORE DILUTE PHASE SUSPENDED IN A GASEOUS MATERIAL AT A LINEAR VELOCITY OF AT LEAST ABOUT 8 FEET PER SECOND IN A SUBTANTIALLY VERTICAL ELONGATED CONFINED ZONE ENCOMPASSED BY AID RECTION ZONE TO AN ACCUMULATION ZONE POSITIONED ABOVE SAID REACTION ZONE TO AN SAID DILUTE PHASE FORMED BY PASSING SAID GASEOUS MTERIAL THROUGH A GRID WHICH REDUCES THE TENDENCY OF BACKFLOW OF CATALYST THEREBY FORMING A PLURALITY OF HIGH VELOCITY STREAMS WHICH COMBINE TO FORM A SINGLE GASEOUS STEAM OF REDUCED VELOCITY PRIOR TO CONTACTING THE CATALYST IN SAID ELONGATED CONFINED ZONE, PASSING THE CONTAMINATED CONTACT MATERIAL TO A STRIPPING ZONE ADJACENT TO SAID ACCUMULATION ZONE, AID STRIPPING ZONE, ACCUMULATION ZONE AND REACTION ZONE BEING IN OPEN COMMUNICATION WITH ONE ANOTHER IN THE UPPER PORTION THEREOF, STRIPPING VOLATILE REACTION PRODUCTS FROM SAID CATALYST AS A DENSE FLUIDZIED MASS IN SAID STRIPING ZONE, CMMINGLING STRIPPED PRODUCTS OF REACTION WITH REACTION PRODUCTS, REMOVING COMMINGLED PRODUCTS OF REACTION FROM SAID REACTION ZONE, WITHDRAWING STRIPPED CATALYST FROM SAID STRIPPING ZONE AND PASSING THE SAME DOWNWARDLY TO A REGENERATION ZONE, REMOVING AT LEAST A PORTION OF THE NON-VOLATILE HYDROCARBONACEOUS MATERIAL FROM THE CATALYST IN THE REGENERATION ZONE AND PASSING CATALYST FROM THE REGENERATION ZONE TO THE LOWER PORTION OF THE REACTION ZONE.
Claim 2
Dependent Claim 277 words
A HYDROFORMING PROCESS WHICH COMPRISES CONTACTING A NAPHTHA FEED WITH A DENSE FLUIDIZED MASS OF FINELY DIVIDED SOLID REFORMING CATALYST IN A REACTION ZONE AT A PRESSURE OF AT LEAST ABOUT 30 P.S.I.G., THUS CONTAMINATING THE CATALYST WITH VOLATILE AND NON-VOLATILE HYDROCARBONACEOUS MATERIAL, WITHDRAWING THE CONTAMINATED CATALYST DIRECTLY FROM THE LOWER PORTION OF THE DENSE MASS OF FLUIDIZED CATALYST IN SAID REACATION ZONE AND PASSING THE SAME UPWARDLY AS A MORE DILUTE PHASE SUSPENDED IN A GASEOUS MATERIAL AT A LINEAR VELOCITY OF AT LEAST ABOUT 8 FEET PER SECOND IN A SUBTANTIALLY VERTICAL ELONGATED CONFINED ZONE ENCOMPASSED BY AID RECTION ZONE TO AN ACCUMULATION ZONE POSITIONED ABOVE SAID REACTION ZONE TO AN SAID DILUTE PHASE FORMED BY PASSING SAID GASEOUS MTERIAL THROUGH A GRID WHICH REDUCES THE TENDENCY OF BACKFLOW OF CATALYST THEREBY FORMING A PLURALITY OF HIGH VELOCITY STREAMS WHICH COMBINE TO FORM A SINGLE GASEOUS STEAM OF REDUCED VELOCITY PRIOR TO CONTACTING THE CATALYST IN SAID ELONGATED CONFINED ZONE, PASSING THE CONTAMINATED CONTACT MATERIAL TO A STRIPPING ZONE ADJACENT TO SAID ACCUMULATION ZONE, AID STRIPPING ZONE, ACCUMULATION ZONE AND REACTION ZONE BEING IN OPEN COMMUNICATION WITH ONE ANOTHER IN THE UPPER PORTION THEREOF, STRIPPING VOLATILE REACTION PRODUCTS FROM SAID CATALYST AS A DENSE FLUIDZIED MASS IN SAID STRIPING ZONE, CMMINGLING STRIPPED PRODUCTS OF REACTION WITH REACTION PRODUCTS, REMOVING COMMINGLED PRODUCTS OF REACTION FROM SAID REACTION ZONE, WITHDRAWING STRIPPED CATALYST FROM SAID STRIPPING ZONE AND PASSING THE SAME DOWNWARDLY TO A REGENERATION ZONE, REMOVING AT LEAST A PORTION OF THE NON-VOLATILE HYDROCARBONACEOUS MATERIAL FROM THE CATALYST IN THE REGENERATION ZONE AND PASSING CATALYST FROM THE REGENERATION ZONE TO THE LOWER PORTION OF THE REACTION ZONE.
Claim 3
Dependent Claim 207 words
AN INTEGRATED VESSEL FOR EFFECTING CONVERSION OF REACTANTS IN THE PRESENCE OF FINELY DIVIDED FLUIZIZED CONTACT MATERIAL COMPRISING IN COMBINATION A REACTION CHAMBER, AN ACCUMULATION CHAMBER ADJACENT TO A STRIPPING CHAMBER POSITIONED ABOVAE SAID REACTION CHAMBER, SAID STRIPPING CHAMBER AND SAID REACATION CHAMBER, SID OPEN COMMUNICATIONWITH ONE ANOTER, A SUBSTANTIALLY VERTICAL ELONGATED FIRST CONDUIT EXTENDING UPWARDLY FROM THE LOWER PORTION OF SAID REACTION CHAMBER INTO SAID ACCUMULATION CHAMBER AND IN OPEN COMMUNICATION THEREWITH, A HOPPER ENCOMPASSING THE INLET TO SAID FIRST ELONGATED CONDUIT IN THE LOWER PORTION OF SAID REACTION CHAMBER, A SECOND CONDUIT TERMINATING IN AN EXPANDED CYLINDRICAL CONDUIT OF LARGER DIAMETER THAN SAID SECOND CONDUIT, SAID EXPANDED CYCLINDRICAL CONDUIT EXTENDING VERTICALLY UPWARD INTO THE BOTTOM OF SAID FIRST CONDUIT THEREBY FORMING AN OPEN ANNULAR ZONE THEREBETWEEN, SAID EXPANDED CONDUIT CONTAINING A PERFORATED MEMBER WITHIN AND BELOW THE OUTLET OF SAID EXPANDED CONDUIT, MEANS FOR INTRODUCING REACTANTS TO THE BOTTOM OF SAID REACTION CHAMBER, MEANS FOR REMOVING CONVERSION PRODUCTS FROM SAID VESSEL, MEANS FOR REMOVING CONVERSION PRODUCTS FROM ACCUMULATION CHAMBER TO SAID STRPPPING CHAMBER, MEANS FOR REMOVING AND PASSING CONSTACAT MATERIAL FROM SAID STRIPPING CHAMBER TO A REGENERATION CHAMBER, AND MEANS FOR PASSING CONTACT MATERIAL TO THE BOTTOM OF SAID REACTION CHAMBER FROM SAID REGENERATION CHAMBER.
Claim 4
Dependent Claim 207 words
AN INTEGRATED VESSEL FOR EFFECTING CONVERSION OF REACTANTS IN THE PRESENCE OF FINELY DIVIDED FLUIZIZED CONTACT MATERIAL COMPRISING IN COMBINATION A REACTION CHAMBER, AN ACCUMULATION CHAMBER ADJACENT TO A STRIPPING CHAMBER POSITIONED ABOVAE SAID REACTION CHAMBER, SAID STRIPPING CHAMBER AND SAID REACATION CHAMBER, SID OPEN COMMUNICATIONWITH ONE ANOTER, A SUBSTANTIALLY VERTICAL ELONGATED FIRST CONDUIT EXTENDING UPWARDLY FROM THE LOWER PORTION OF SAID REACTION CHAMBER INTO SAID ACCUMULATION CHAMBER AND IN OPEN COMMUNICATION THEREWITH, A HOPPER ENCOMPASSING THE INLET TO SAID FIRST ELONGATED CONDUIT IN THE LOWER PORTION OF SAID REACTION CHAMBER, A SECOND CONDUIT TERMINATING IN AN EXPANDED CYLINDRICAL CONDUIT OF LARGER DIAMETER THAN SAID SECOND CONDUIT, SAID EXPANDED CYCLINDRICAL CONDUIT EXTENDING VERTICALLY UPWARD INTO THE BOTTOM OF SAID FIRST CONDUIT THEREBY FORMING AN OPEN ANNULAR ZONE THEREBETWEEN, SAID EXPANDED CONDUIT CONTAINING A PERFORATED MEMBER WITHIN AND BELOW THE OUTLET OF SAID EXPANDED CONDUIT, MEANS FOR INTRODUCING REACTANTS TO THE BOTTOM OF SAID REACTION CHAMBER, MEANS FOR REMOVING CONVERSION PRODUCTS FROM SAID VESSEL, MEANS FOR REMOVING CONVERSION PRODUCTS FROM ACCUMULATION CHAMBER TO SAID STRPPPING CHAMBER, MEANS FOR REMOVING AND PASSING CONSTACAT MATERIAL FROM SAID STRIPPING CHAMBER TO A REGENERATION CHAMBER, AND MEANS FOR PASSING CONTACT MATERIAL TO THE BOTTOM OF SAID REACTION CHAMBER FROM SAID REGENERATION CHAMBER.

References Cited (Backward Citations)

US2666731A Cited
US2601676A Cited
US2761820A Cited
US2689973A Cited
US2695866A Cited
US2791542A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1962-12-28 1963-06-29 1963-12-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1966-12-28 1967-06-29 1967-12-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1970-12-28 1971-06-29 1971-12-29 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag