US4065269A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Spent catalyst regeneration apparatus
Assignee: Honeywell UOP LLC
•
Filing: 1976-04-12
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Granted: 1977-12-27
•
Expires: 1996-04-12
Abstract
Abstract A catalyst regeneration process and apparatus for the oxidation of coke from a spent catalyst and for the conversion of CO resulting from the oxidation of coke to CO 2 . Novel feature of the process is the mixing of a portion of regenerated catalyst produced in a coke oxidation zone and heated to a higher temperature in a CO-conversion zone with spent catalyst and passing the mixture to a coke-oxidation zone to increase the temperature within the coke oxidation zone and to disperse spent catalyst more evenly across that zone thereby increasing the rate, extent and evenness of coke oxidation. The regeneration apparatus includes components by which this can be accomplished.
Inventors
- 👤 Richard P. Pulak
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 22:17
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/18; B01J8/24; B01J8/26; C; C10; C10G; C10G11/00; C10G11/14; C10G11/18; C10G11/182; Y; Y02; Y02P; Y02P30/00; Y02P30/40
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
310 words
An apparatus for oxidizing coke on spent catalyst which apparatus comprises in combination: a. a spent-catalyst-regenerated-catalyst admixture receiving chamber for containing a dense-phase fluidized bed of catalyst having a spent-catalyst-regenerated-catalyst admixture inlet means and a fresh-regeneration-gas inlet means connected thereto to allow passage of a spent-catalyst-regenerated-catalyst admixture and fresh regeneration gas respectively into said chamber and having a regenerated-catalyst/regeneration-gas outlet means connected thereto to allow passage of regenerated catalyst and spent-regeneration gas from said chamber; b. a spent-catalyst-regenerated-catalyst admixture conduit connected to said spent-catalyst-regenerated-catalyst admixture receiving chamber inlet means; c. a transfer conduit having a substantially vertical portion and a substantially horizontal portion, said vertical portion having an inlet connected to said regenerated-catalyst/regeneration-gas outlet means and said horizontal portion extending into the side of a hereinafter described regenerated-catalyst receiving chamber and having an outlet within said chamber whereby said regenerated catalyst and regeneration gas are carried from said spent-catalyst-regenerated-catalyst admixture receiving chamber in admixture to said regenerated-catalyst receiving chamber; d. a regenerated-catalyst receiving chamber for containing a dense-phase bed of regenerated catalyst, said chamber having a regenerated-catalyst outlet means and a spent-regeneration-gas outlet means connected thereto to allow passage of said regenerated catalyst and said spent regeneration gas from said chamber and said chamber being adjacent to and at an elevation with respect to said spent-catalyst-regenerated-catalyst admixture receiving chamber to maintain at least a portion of said dense-phase bed of said regenerated catalyst above said dense-phase fluidized bed of catalyst in said spent-catalyst-regenerated-catalyst admixture receiving chamber; and, e. an external regenerated-catalyst recycle means, external from said spent-catalyst-regenerated catalyst admixture receiving chamber, having an inlet means in said regenerated-catalyst receiving chamber and an outlet means in said spent-catalyst-regenerated-catalyst admixture conduit, to allow passage of a portion of said regenerated catalyst from said regenerated-catalyst receiving chamber in admixture with spent catalyst in said spent-catalyst conduit to said spent-catalyst-regenerated catalyst admixture receiving chamber.
Claim 2
Independent Claim
310 words
An apparatus for oxidizing coke on spent catalyst which apparatus comprises in combination: a. a spent-catalyst-regenerated-catalyst admixture receiving chamber for containing a dense-phase fluidized bed of catalyst having a spent-catalyst-regenerated-catalyst admixture inlet means and a fresh-regeneration-gas inlet means connected thereto to allow passage of a spent-catalyst-regenerated-catalyst admixture and fresh regeneration gas respectively into said chamber and having a regenerated-catalyst/regeneration-gas outlet means connected thereto to allow passage of regenerated catalyst and spent-regeneration gas from said chamber; b. a spent-catalyst-regenerated-catalyst admixture conduit connected to said spent-catalyst-regenerated-catalyst admixture receiving chamber inlet means; c. a transfer conduit having a substantially vertical portion and a substantially horizontal portion, said vertical portion having an inlet connected to said regenerated-catalyst/regeneration-gas outlet means and said horizontal portion extending into the side of a hereinafter described regenerated-catalyst receiving chamber and having an outlet within said chamber whereby said regenerated catalyst and regeneration gas are carried from said spent-catalyst-regenerated-catalyst admixture receiving chamber in admixture to said regenerated-catalyst receiving chamber; d. a regenerated-catalyst receiving chamber for containing a dense-phase bed of regenerated catalyst, said chamber having a regenerated-catalyst outlet means and a spent-regeneration-gas outlet means connected thereto to allow passage of said regenerated catalyst and said spent regeneration gas from said chamber and said chamber being adjacent to and at an elevation with respect to said spent-catalyst-regenerated-catalyst admixture receiving chamber to maintain at least a portion of said dense-phase bed of said regenerated catalyst above said dense-phase fluidized bed of catalyst in said spent-catalyst-regenerated-catalyst admixture receiving chamber; and, e. an external regenerated-catalyst recycle means, external from said spent-catalyst-regenerated catalyst admixture receiving chamber, having an inlet means in said regenerated-catalyst receiving chamber and an outlet means in said spent-catalyst-regenerated-catalyst admixture conduit, to allow passage of a portion of said regenerated catalyst from said regenerated-catalyst receiving chamber in admixture with spent catalyst in said spent-catalyst conduit to said spent-catalyst-regenerated catalyst admixture receiving chamber.
Claim 3
Dependent Claim
34 words
The apparatus of claim 1 further characterized in that said outlet of said transfer conduit is in communication with a disengaging space provided to separate regenerated catalyst and regeneration gas passing through said conduit.
Claim 4
Dependent Claim
55 words
The apparatus of claim 1 further characterized in that said apparatus includes an internal regenerated-catalyst recycle means having an inlet means in said transfer conduit and an outlet means in said spent-catalyst-regenerated-catalyst admixture receiving chamber to allow passage of a portion of said regenerated catalyst from said transfer conduit to said spent-catalyst-regenerated-catalyst admixture receiving chamber.
Claim 5
Dependent Claim
49 words
The apparatus of claim 3 further characterized in that said internal regenerated-catalyst recycle means comprises a regenerated-catalyst collecting means having a catalyst inlet means and a catalyst outlet means and a conduit having an inlet means attached to said outlet means of said collecting means and an outlet means.
Claim 6
Dependent Claim
23 words
The apparatus of claim 1 further characterized in that said external regenerated-catalyst recycle means comprises a conduit having a flow-regulating means located thereon.
Claim 7
Independent Claim
376 words
An apparatus for oxidizing coke on spent catalyst which apparatus comprises in combination: a. a spent-catalyst-regenerated-catalyst admixture receiving chamber for containing a dense-phase fluidized bed of catalyst, said chamber having upper and lower sections, a fresh-regeneration-gas inlet means connected to said chamber at said lower section to allow passage of fresh regeneration gas into said chamber through said lower section, a spent-catalyst-regenerated-catalyst admixture inlet means connected to said chamber to allow passage of a spent catalyst-regenerated-catalyst admixture into said chamber, and a regenerated-catalyst/regeneration-gas outlet means at the upper section of said chamber to allow passage of regenerated catalyst and regeneration gas in admixture from said chamber; b. a spent-catalyst-regenerated-catalyst admixture conduit connected to said spent-catalyst-regenerated catalyst admixture receiving chamber inlet means; c. a transfer conduit having a substantially vertical portion and a substantially horizontal portion, said vertical portion having an inlet connected to said regenerated-catalyst/regeneration-gas outlet means and said horizontal portion extending into the side of a hereinafter described regenerated-catalyst receiving chamber and having an outlet means within said chamber in communication with a disengaging space whereby said regenerated catalyst and regeneration gas are carried in admixture from said spent-catalyst-regenerated-catalyst admixture receiving chamber to said disengaging space; d. a regenerated-catalyst receiving chamber for containing a dense-phase bed of regenerated catalyst, said chamber being adjacent to and at an elevation with respect to said spent-catalyst-regenerated-catalyst admixture receiving chamber to maintain at least a portion of said bed of regenerated catalyst above said dense-phase fluidized bed of catalyst in the spent-catalyst-regenerated-catalyst admixture receiving chamber, said regenerated-catalyst receiving chamber having upper and lower sections, a spent-regeneration-gas outlet means connected to said chamber at its upper section to allow passage of spent regeneration gas from said chamber, and a regenerated-catalyst outlet means at its lower section to allow passage of said regenerated catalyst from said chamber; and, e. an external regenerated-catalyst recycle means, external to said spent-catalyst-regenerated-catalyst admixture receiving chamber, comprising a conduit having a flow-regulating means located thereon and having an inlet means in said regenerated-catalyst receiving chamber and an outlet means in the spent-catalyst-regenerated-catalyst admixture conduit to allow passage of a portion of said regenerated-catalyst from said regenerated-catalyst receiving chamber in admixture with spent catalyst to said dense-phase fluidized bed of catalyst in the spent-catalyst-regenerated-catalyst admixture receiving chamber.
Claim 8
Independent Claim
376 words
An apparatus for oxidizing coke on spent catalyst which apparatus comprises in combination: a. a spent-catalyst-regenerated-catalyst admixture receiving chamber for containing a dense-phase fluidized bed of catalyst, said chamber having upper and lower sections, a fresh-regeneration-gas inlet means connected to said chamber at said lower section to allow passage of fresh regeneration gas into said chamber through said lower section, a spent-catalyst-regenerated-catalyst admixture inlet means connected to said chamber to allow passage of a spent catalyst-regenerated-catalyst admixture into said chamber, and a regenerated-catalyst/regeneration-gas outlet means at the upper section of said chamber to allow passage of regenerated catalyst and regeneration gas in admixture from said chamber; b. a spent-catalyst-regenerated-catalyst admixture conduit connected to said spent-catalyst-regenerated catalyst admixture receiving chamber inlet means; c. a transfer conduit having a substantially vertical portion and a substantially horizontal portion, said vertical portion having an inlet connected to said regenerated-catalyst/regeneration-gas outlet means and said horizontal portion extending into the side of a hereinafter described regenerated-catalyst receiving chamber and having an outlet means within said chamber in communication with a disengaging space whereby said regenerated catalyst and regeneration gas are carried in admixture from said spent-catalyst-regenerated-catalyst admixture receiving chamber to said disengaging space; d. a regenerated-catalyst receiving chamber for containing a dense-phase bed of regenerated catalyst, said chamber being adjacent to and at an elevation with respect to said spent-catalyst-regenerated-catalyst admixture receiving chamber to maintain at least a portion of said bed of regenerated catalyst above said dense-phase fluidized bed of catalyst in the spent-catalyst-regenerated-catalyst admixture receiving chamber, said regenerated-catalyst receiving chamber having upper and lower sections, a spent-regeneration-gas outlet means connected to said chamber at its upper section to allow passage of spent regeneration gas from said chamber, and a regenerated-catalyst outlet means at its lower section to allow passage of said regenerated catalyst from said chamber; and, e. an external regenerated-catalyst recycle means, external to said spent-catalyst-regenerated-catalyst admixture receiving chamber, comprising a conduit having a flow-regulating means located thereon and having an inlet means in said regenerated-catalyst receiving chamber and an outlet means in the spent-catalyst-regenerated-catalyst admixture conduit to allow passage of a portion of said regenerated-catalyst from said regenerated-catalyst receiving chamber in admixture with spent catalyst to said dense-phase fluidized bed of catalyst in the spent-catalyst-regenerated-catalyst admixture receiving chamber.
Claim 9
Dependent Claim
93 words
The apparatus of claim 6 further characterized in that said apparatus includes an internal regenerated-catalyst recycle means comprising: a regenerated catalyst collecting means, located in the substantially vertical portion of said transfer conduit and having a catalyst inlet means and a catalyst outlet means; and, a downwardly extending conduit, having an inlet means attached to said outlet means of said collecting means and an outlet means located within said spent-catalyst-regenerated-catalyst admixture receiving chamber, to allow passage of a portion of said regenerated catalyst from said transfer conduit to said spent-catalyst-regenerated-catalyst admixture receiving chamber.
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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) | 1980-12-26 | 1981-06-27 | 1981-12-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-12-26 | 1985-06-27 | 1985-12-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-12-26 | 1989-06-27 | 1989-12-27 | $7700.00 | Window Closed / Lapsed |