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US4118337A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for regenerating fluidizable solid particles employed in hydrocarbon conversion

Assignee: Mobil Oil AS
•
Filing: 1977-06-20
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Granted: 1978-10-03
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Expires: 1997-06-20
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Abstract

Abstract A hydrocarbon conversion-catalyst regeneration operation and apparatus required is described. Hot regenerated catalyst is mixed with spent catalyst in a first upflow annular fluid catalyst bed regeneration operation about a second concentric downflow fluid catalyst bed regeneration operation. Catalyst flow-through passageways pass catalyst from said downflowing catalyst bed operation to said upflow catalyst bed regeneration operation.

Inventors

  • 👤 Benjamin Gross
  • 👤 Klaus Wilhelm Schatz

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 19:43
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/90; B01J8/00; B01J8/18; B01J8/24; B01J8/26; C; C10; C10G; C10G11/00; C10G11/14; C10G11/18; C10G11/182

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 265 words
In a fluid catalyst operation comprising conversion of hydrocarbons to lower and higher boiling products and regeneration of catalyst employed in said hydrocarbon conversion, the method for regenerating catalyst particles comprising carbonaceous material deposits which comprises passing spent catalyst into an annular catalyst regeneration zone about the periphery of an inner concentric catalyst regeneration zone, admixing hot freshly regenerated catalyst particles obtained from said concentric zone with said spent catalyst in said annular zone in an amount sufficient to raise the temperature of said spent catalyst to a temperature promoting the combustion of carbonaceous material in the presence of oxygen containing regeneration gas, causing said mixture of spent and regenerated catalyst to flow as a suspension in combustion supporting gases generally upwardly through vertical sections of said annular zone during combustion of carbonaceous material with controlled amounts of introduced combustion supporting gas, discharging the suspension from the top of said annular zone through an annular passageway into a dispersed phase of catalyst above said concentric catalyst regeneration zone for flow generally downwardly therethrough as a dense flowing bed of catalyst and countercurrent to rising regeneration gas, introducing combustion supporting regeneration gas to a bottom portion of said concentric downwardly flowing bed of catalyst beneath the inlet of a regeneration catalyst withdrawal zone, passing regenerated catalyst from a lower portion of said concentric bed through said withdrawal zone to a hydrocarbon conversion zone, separating particles of catalyst from combustion gases in said dispersed phase above said concentric bed of catalyst, withdrawing said combustion gases and passing catalyst separated in said dispersed phase into said concentric bed.
Claim 2
Dependent Claim 265 words
In a fluid catalyst operation comprising conversion of hydrocarbons to lower and higher boiling products and regeneration of catalyst employed in said hydrocarbon conversion, the method for regenerating catalyst particles comprising carbonaceous material deposits which comprises passing spent catalyst into an annular catalyst regeneration zone about the periphery of an inner concentric catalyst regeneration zone, admixing hot freshly regenerated catalyst particles obtained from said concentric zone with said spent catalyst in said annular zone in an amount sufficient to raise the temperature of said spent catalyst to a temperature promoting the combustion of carbonaceous material in the presence of oxygen containing regeneration gas, causing said mixture of spent and regenerated catalyst to flow as a suspension in combustion supporting gases generally upwardly through vertical sections of said annular zone during combustion of carbonaceous material with controlled amounts of introduced combustion supporting gas, discharging the suspension from the top of said annular zone through an annular passageway into a dispersed phase of catalyst above said concentric catalyst regeneration zone for flow generally downwardly therethrough as a dense flowing bed of catalyst and countercurrent to rising regeneration gas, introducing combustion supporting regeneration gas to a bottom portion of said concentric downwardly flowing bed of catalyst beneath the inlet of a regeneration catalyst withdrawal zone, passing regenerated catalyst from a lower portion of said concentric bed through said withdrawal zone to a hydrocarbon conversion zone, separating particles of catalyst from combustion gases in said dispersed phase above said concentric bed of catalyst, withdrawing said combustion gases and passing catalyst separated in said dispersed phase into said concentric bed.
Claim 3
Dependent Claim 34 words
The method of claim 1 wherein catalyst is separated from combustion flue gases in said dispersed phase in a cyclone separating zone and catalyst thus separated is returned to said concentric bed of catalyst.
Claim 4
Dependent Claim 24 words
The method of claim 1 wherein catalyst separated from combustion flue gases in said dispersed phase is passed in part to said annular zone.
Claim 5
Dependent Claim 39 words
The method of claim 1 wherein catalyst particles are passed from a lower portion of said concentric catalyst bed to said annular zone through downflowing catalyst passageways there-between for admixture with spent catalyst particles introduced to said annular zone.
Claim 6
Dependent Claim 25 words
The method of claim 1 wherein the mixture of spent catalyst particles and regenerated catalyst particles in the annular zone is at least 1100° F.
Claim 7
Dependent Claim 16 words
The method of claim 1 wherein the spent catalyst is introduced tangentially to said annular zone.
Claim 8
Dependent Claim 19 words
The method of claim 1 wherein regeneration of the catalyst is accomplished under conditions promoting the combustion of CO.
Claim 9
Dependent Claim 26 words
The method of claim 1 wherein catalyst separated from combustion flue gases in the dispersed phase is passed directly to said annular zone in substantial measure.
Claim 10
Dependent Claim 32 words
The method of claim 1 wherein combustion flue gas with entrained catalyst particles pass from said annular zone into a dispersed phase of catalyst above said concentric downwardly flowing bed of catalyst.
Claim 11
Dependent Claim 25 words
The method of claim 1 wherein substantially all of said catalyst particles passing upwardly through said annular zone pass into said concentric bed of catalyst.

References Cited (Backward Citations)

US3563911A Cited
US3886060A Cited
US4036779A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-10-02 1982-04-03 1982-10-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-10-02 1986-04-03 1986-10-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-10-02 1990-04-03 1990-10-03 $7700.00 Window Closed / Lapsed

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