Patent US4397738A successfully refreshed from Google Patents.
US4397738A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the separation of particulate solids from vapors
Assignee: Honeywell UOP LLC
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Filing: 1982-09-16
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Granted: 1983-08-09
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Expires: 2002-09-16
Abstract
Abstract A process and related apparatus for separating particulate solids from a stream comprising vapors and particulate solids passed in admixture through an elongated contacting zone. The stream is discharged at an angle to the vertical along the inside wall of a cylindrical disengagement zone. The solids separate due to centripetal acceleration and fall to the bottom of the disengagement zone.
Inventors
- 👤 Thomas L. Kemp
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 17:03
CPC Classifications
C; C10; C10G; C10G11/00; C10G11/14; C10G11/18; B; B01; B01J; B01J8/00; B01J8/005; B01J8/0055
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
141 words
A process for separating particulate solids from a stream comprising vapors and particulate solids passed in admixture through a vertically elongated contacting zone, which process comprises discharging said stream from said contacting zone into the main body of a disengagement zone, said disengagement zone having an interior cylindrical surface, the cylindrical axis of which is substantially vertical, altering the direction of flow of said stream upon the discharge of said stream from said contacting zone so as to effect the flow of said stream to be in a downward direction along the curvature of said interior surface and at a positive angle to the vertical, said stream having a downward progression while maintaining a helical twist of a vertical axis, whereby said solids fall to a bottom portion of said disengagement zone and said vapors rise to an upper portion thereof.
Claim 2
Dependent Claim
141 words
A process for separating particulate solids from a stream comprising vapors and particulate solids passed in admixture through a vertically elongated contacting zone, which process comprises discharging said stream from said contacting zone into the main body of a disengagement zone, said disengagement zone having an interior cylindrical surface, the cylindrical axis of which is substantially vertical, altering the direction of flow of said stream upon the discharge of said stream from said contacting zone so as to effect the flow of said stream to be in a downward direction along the curvature of said interior surface and at a positive angle to the vertical, said stream having a downward progression while maintaining a helical twist of a vertical axis, whereby said solids fall to a bottom portion of said disengagement zone and said vapors rise to an upper portion thereof.
Claim 3
Dependent Claim
18 words
The process of claim 1 wherein said angle to the vertical is from about 15° to about 45°.
Claim 4
Dependent Claim
65 words
The process of claim 1 wherein said contacting zone is substantially axial to said cylindrical axis of said interior surface, said contacting zone having at least two discharge outlets evenly spaced around said contacting zone in a horizontal plane, the respective direction of flow of the streams from each said discharge outlet along said interior surface of said disengagement zone being in substantially helical orientation.
Claim 5
Dependent Claim
41 words
The process of claim 1 wherein said process comprises a catalytic cracking process in which said elongated contacting zone comprises a reactor riser, said particulate solids comprise catalyst, said vapors comprise hydrocarbons and said process comprises a fluid catalytic cracking process.
Claim 6
Independent Claim
130 words
An apparatus useful for separating particulate solids from a stream comprising vapors and particulate solids in admixture, said apparatus comprising in combination; (a) a vertical riser conduit having a discharge opening through which said stream may pass; (b) a cylindrical vessel containing said discharge opening, the cylindrical axis of said vessel being vertical and said opening discharging into the main body of the vessel; (c) a deflecting means comprising a curved surface juxtaposed with respect to said discharge opening such that said stream passing from said discharge opening is deflected in a downward direction along the curvature of the interior surface of said vessel at a positive angle to the vertical, said deflecting means providing a downward progression to said stream while maintaining a helical twist of a vertical axis.
Claim 7
Independent Claim
130 words
An apparatus useful for separating particulate solids from a stream comprising vapors and particulate solids in admixture, said apparatus comprising in combination; (a) a vertical riser conduit having a discharge opening through which said stream may pass; (b) a cylindrical vessel containing said discharge opening, the cylindrical axis of said vessel being vertical and said opening discharging into the main body of the vessel; (c) a deflecting means comprising a curved surface juxtaposed with respect to said discharge opening such that said stream passing from said discharge opening is deflected in a downward direction along the curvature of the interior surface of said vessel at a positive angle to the vertical, said deflecting means providing a downward progression to said stream while maintaining a helical twist of a vertical axis.
Claim 8
Dependent Claim
18 words
The apparatus of claim 5 wherein said angle to the vertical is from about 15° to about 45°.
Claim 9
Dependent Claim
81 words
The apparatus of claim 5 wherein said riser conduit is substantially axial to said cylindrical axis of said cylindrical vessel, there being at least two discharge openings in said riser conduit evenly spaced around said conduit in a horizontal plane, the respective deflecting means juxtaposed with each of said discharge openings being orientated to effect the respective directions of flow of the streams from each said discharge opening along said interior surface of said vessel to be in substantially helical orientation.
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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) | 1986-08-08 | 1987-02-07 | 1987-08-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-08-08 | 1991-02-07 | 1991-08-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-08-08 | 1995-02-07 | 1995-08-09 | $7700.00 | Window Closed / Lapsed |