Patent US4364849A successfully refreshed from Google Patents.
US4364849A
Expired / Lapsed
US
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Fluid catalyst regeneration process and apparatus
Assignee: Honeywell UOP LLC
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Filing: 1981-09-14
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Granted: 1982-12-21
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Expires: 2001-09-14
Abstract
Abstract A catalyst regeneration process and apparatus for the oxidative removal of coke from a coke contaminated fluid catalyst. The process comprises a high temperature coke combustion zone, a catalyst disengagement zone and an external heat removal zone comprising a shell and tube heat exchanger. Catalyst is cooled by passing it through the shell side of the heat exchanger with a cooling medium through the tube side. A mixture of coke contaminated catalyst, oxygen containing gas, and cool regenerated catalyst from the heat removal zone are contacted in the high temperature combustion zone, the temperature of which is controlled by adjusting the rate at which catalyst is passed through the heat exchanger. This rate is adjusted by adjusting the difference in catalyst head between the catalyst inlet and outlet of the heat exchanger and thus the hydraulic driving force which effects catalyst circulation through the heat exchanger.
Inventors
- 👤 Anthony G. Vickers
- 👤 David A. Lomas
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 21:28
CPC Classifications
C; C10; C10G; C10G11/00; C10G11/14; C10G11/18; C10G11/182
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
333 words
A process for regenerating a coke contaminated fluid catalyst, said process including the steps of: (a) introducing oxygen containing regeneration gas, coke contaminated fluid catalyst, and cooled recycled regenerated catalyst from a source hereinafter described, into a lower locus of combustion zone maintained at a temperature sufficient for coke oxidation and therein oxidizing coke to produce hot regenerated catalyst and hot flue gas; (b) transporting said hot flue gas and said hot regenerated catalyst from an upper locus of said combustion zone into a regenerated catalyst disengaging zone, wherein said hot regenerated catalyst is separated from said flue gas and collected in a first collection zone at a lower locus of said disengaging zone as a fluidized bed the surface of which is at a first level; (c) transporting a portion of said hot regenerated catalyst from said first collection zone by means of downward gravity flow to the lower locus of a cooling zone separate from and below said disengaging zone wherein said cooling zone heat is withdrawn from said hot regenerated catalyst by indirect heat exchange with a cooling fluid enclosed in a heat exchange means inserted into said cooling zone to produce cool regenerated catalyst, said catalyst being maintained in said cooling zone as a dense phase fluidized bed by passing a fluidizing gas upwardly through such bed; (d) withdrawing said cool regenerated catalyst from said cooling zone by means of said catalyst overflowing from said cooling zone into a second collection zone at a lower locus of said disengaging zone, said catalyst being collected in said second collection zone as a dense phase fluidized bed the surface of which is at a second level, said first level being of sufficient height above said second level to provide the driving force required to circulate said catalyst through said cooling zone and; (e) transporting said catalyst by means of downward gravity flow from said second collection zone to said lower locus of said combustion zone as said cooled recycled regenerated catalyst.
Claim 2
Dependent Claim
333 words
A process for regenerating a coke contaminated fluid catalyst, said process including the steps of: (a) introducing oxygen containing regeneration gas, coke contaminated fluid catalyst, and cooled recycled regenerated catalyst from a source hereinafter described, into a lower locus of combustion zone maintained at a temperature sufficient for coke oxidation and therein oxidizing coke to produce hot regenerated catalyst and hot flue gas; (b) transporting said hot flue gas and said hot regenerated catalyst from an upper locus of said combustion zone into a regenerated catalyst disengaging zone, wherein said hot regenerated catalyst is separated from said flue gas and collected in a first collection zone at a lower locus of said disengaging zone as a fluidized bed the surface of which is at a first level; (c) transporting a portion of said hot regenerated catalyst from said first collection zone by means of downward gravity flow to the lower locus of a cooling zone separate from and below said disengaging zone wherein said cooling zone heat is withdrawn from said hot regenerated catalyst by indirect heat exchange with a cooling fluid enclosed in a heat exchange means inserted into said cooling zone to produce cool regenerated catalyst, said catalyst being maintained in said cooling zone as a dense phase fluidized bed by passing a fluidizing gas upwardly through such bed; (d) withdrawing said cool regenerated catalyst from said cooling zone by means of said catalyst overflowing from said cooling zone into a second collection zone at a lower locus of said disengaging zone, said catalyst being collected in said second collection zone as a dense phase fluidized bed the surface of which is at a second level, said first level being of sufficient height above said second level to provide the driving force required to circulate said catalyst through said cooling zone and; (e) transporting said catalyst by means of downward gravity flow from said second collection zone to said lower locus of said combustion zone as said cooled recycled regenerated catalyst.
Claim 3
Dependent Claim
65 words
The process of claim 1 wherein the quantity of catalyst circulated through said cooling zone and thereby the quantity of heat removed from said catalyst is controllably maintained by controlling the height of said second level by controlling the quantity of catalyst transported from said second collection zone to said lower locus of said combustion zone, the height of said first level being held constant.
Claim 4
Dependent Claim
39 words
The process of claim 2 wherein the temperature at a selected locus of said combustion zone is controllably maintained by controlling the quantity of catalyst circulated through said cooling zone in response to said temperature at said selected locus.
Claim 5
Dependent Claim
17 words
The process of claim 3 wherein said selected locus is a lower locus of said combustion chamber.
Claim 6
Dependent Claim
12 words
The process of claim 1 wherein said fluidizing gas comprises regeneration gas.
Claim 7
Dependent Claim
11 words
The process of claim 1 wherein said cooling fluid comprises water.
Claim 8
Dependent Claim
24 words
The process of claim 6 wherein said water cooling fluid changes from liquid to gas phase while absorbing heat in said heat exchange means.
Claim 9
Dependent Claim
35 words
The process of claim 1 wherein said regeneration gas and coke contaminated fluid catalyst are mixed together in a mixing zone and the resulting mixture is passed from said mixture zone to said combustion 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) | 1985-12-20 | 1986-06-21 | 1986-12-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-12-20 | 1990-06-21 | 1990-12-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-12-20 | 1994-06-21 | 1994-12-21 | $7700.00 | Window Closed / Lapsed |