US4118338A
Expired / Lapsed
US
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Method for regenerating a fluid cracking catalyst
Assignee: Mobil Oil AS
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Filing: 1977-09-01
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Granted: 1978-10-03
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Expires: 1997-09-01
Abstract
Abstract A hydrocarbon conversion-catalyst regeneration system is described which particularly relies upon a fluidized catalyst regeneration operation arranged to restrict the catalyst inventory of the system by employing upflowing and downflowing fluid masses of catalyst in cooperative arrangement with one another providing a limited dispersed catalyst phase section and wherein the recycle of regenerated hot catalyst admixed with spent catalyst is controlled principally as a function of the pressure differential between the upflowing and downflowing catalyst masses.
Inventors
- 👤 Benjamin Gross
- 👤 Klaus Wilhelm Schatz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 20:23
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: 9
Claim 1
Independent Claim
301 words
In a hydrocarbon conversion-catalyst regeneration operation employing fluidized catalyst particles comprising a crystalline zeolite wherein catalyst particles comprising carbonaceous deposits are recovered from hydrocarbon conversion and passed to a catalyst regeneration operation to remove carbonaceous deposits by burning thereby heating the catalyst particles to an elevated temperature within the range of 1200° F. to 1500° F. and catalyst particles thus heated are returned to the hydrocarbon conversion operation, the improved method for regenerating the catalyst particles which comprises, forming a suspension of spent catalyst particles comprising carbonaceous deposits in upflowing gaseous material passing upwardly through a first riser zone communicating with the bottom open end of a larger diameter cylindrical combustion zone for burning carbonaceous material, recovering regenerated catalyst in an annular zone about said cylindrical zone, passing regenerated catalyst from the bottom of said annular zone in admixture with said catalyst suspension adjacent the upper end of said first riser zone and before passage into the bottom open end of said larger diameter cylindrical combustion zone, passing a mass of regenerated catalyst particles in admixture with spent catalyst upwardly through said combustion zone under conditions supporting combustion of carbon containing material thereby heating said catalyst particles to a temperature above 1200° F., separating catalyst particles thus regenerated from gaseous combustion products following upward flow through said larger diameter combustion zone, recovering hot regenerated catalyst thus separated in said annular zone, and maintaining a catalyst head of pressure between said annular zone and said cylindrical zone to maintain a flow of hot regenerated catalyst from said annular zone into the bottom open end of said larger diameter cylindrical zone to form a mix temperature with carbon containing catalyst particles suspended in oxygen containing gas sufficient to particularly promote the combustion of carbon material in the presence of oxygen containing regeneration gas.
Claim 2
Dependent Claim
301 words
In a hydrocarbon conversion-catalyst regeneration operation employing fluidized catalyst particles comprising a crystalline zeolite wherein catalyst particles comprising carbonaceous deposits are recovered from hydrocarbon conversion and passed to a catalyst regeneration operation to remove carbonaceous deposits by burning thereby heating the catalyst particles to an elevated temperature within the range of 1200° F. to 1500° F. and catalyst particles thus heated are returned to the hydrocarbon conversion operation, the improved method for regenerating the catalyst particles which comprises, forming a suspension of spent catalyst particles comprising carbonaceous deposits in upflowing gaseous material passing upwardly through a first riser zone communicating with the bottom open end of a larger diameter cylindrical combustion zone for burning carbonaceous material, recovering regenerated catalyst in an annular zone about said cylindrical zone, passing regenerated catalyst from the bottom of said annular zone in admixture with said catalyst suspension adjacent the upper end of said first riser zone and before passage into the bottom open end of said larger diameter cylindrical combustion zone, passing a mass of regenerated catalyst particles in admixture with spent catalyst upwardly through said combustion zone under conditions supporting combustion of carbon containing material thereby heating said catalyst particles to a temperature above 1200° F., separating catalyst particles thus regenerated from gaseous combustion products following upward flow through said larger diameter combustion zone, recovering hot regenerated catalyst thus separated in said annular zone, and maintaining a catalyst head of pressure between said annular zone and said cylindrical zone to maintain a flow of hot regenerated catalyst from said annular zone into the bottom open end of said larger diameter cylindrical zone to form a mix temperature with carbon containing catalyst particles suspended in oxygen containing gas sufficient to particularly promote the combustion of carbon material in the presence of oxygen containing regeneration gas.
Claim 3
Dependent Claim
22 words
The method of claim 1 wherein an oxygen containing regeneration gas is used to form said suspension in said first riser zone.
Claim 4
Dependent Claim
19 words
The method of claim 1 wherein oxygen containing regeneration gas is introduced to lower portion of said combustion zone.
Claim 5
Dependent Claim
19 words
The method of claim 1 wherein burning of residual carbon on catalyst particles is accomplished in said annular zone.
Claim 6
Dependent Claim
19 words
The method of claim 1 wherein the combustion of formed carbon monoxide is promoted particularly in said combustion zone.
Claim 7
Dependent Claim
21 words
The method of claim 1 wherein regenerated catalyst is mixed with catalyst containing carbonaceous deposits passed to said first riser zone.
Claim 8
Dependent Claim
17 words
The method of claim 1 wherein combustion of carbonaceous material is initiated in said first riser zone.
Claim 9
Dependent Claim
32 words
The method of claim 1 wherein a suspension of hot combustion products and regenerated catalyst particles is discharged from the upper end of said combustion zone generally downward into said annular zone.
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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 |