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US4212653A Expired / Lapsed US ⏱️ 0.0 years remaining

Process and apparatus for separating particulate matter from gaseous media

Assignee: General Electric Co
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Filing: 1978-06-27
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Granted: 1980-07-15
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Expires: 1998-06-27
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Abstract

Abstract A process for separating particulate matter from a contaminated gaseous medium includes employing a swirling substantially contaminant-free gaseous medium between a zone for introducing the contaminated medium into a cyclonic separator zone and a product gas exhaust zone which extends into the separation zone. Apparatus suitable for carrying out the process is also described.

Inventors

  • 👤 Walter B. Giles

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 22:26
CPC Classifications
B; B04; B04C; B04C5/00; B04C5/02; B04C5/04; B01; B01D; B01D45/00; B01D45/12; B01D45/16; B04C5/14; B04C5/181; F; F23; F23J; F23J15/00; F23J15/02; F23J15/022; F23J15/027

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 253 words
In a process for separating particulate matter from a contaminated gaseous medium containing said particulate matter therein, comprising: (A) passing said contaminated gaseous medium through a first swirl-inducing zone to form a swirling contaminated gaseous medium, (B) introducing said swirling contaminated gaseous medium into a cyclonic separation zone via a path adjacent an inner surface of a wall defining a periphery of said separation zone to separate at least a portion of said particulate matter from said swirling contaminated gaseous medium and form a gaseous product which is at least partially depleted in said particulate matter, and (C) removing said gaseous product from said separation zone through a gaseous exhaust flow zone disposed radially inwardly of said first swirl-inducing zone, the improvement for increasing separation efficiency, which comprises: (D) passing a substantially contaminant-free gaseous medium through a second swirl-inducing zone to form a co-swirling substantially contaminant-free gaseous medium, (E) introducing said co-swirling gaseous medium into said separation zone through an introduction zone disposed radially inwardly of said swirling contaminated gaseous medium and radially outwardly of said exhaust flow zone, and (F) employing an additional wall to separate said introduction zone from the so-introduced swirling contaminated gaseous medium, said additional wall extending into said separation zone, said exhaust flow zone extending into said separation zone further than said additional wall so extends, such that separation of the introduced co-swirling contaminated gaseous medium from the introduced swirling substantially contaminant-free gaseous medium is terminated before the swirling contaminated gaseous medium has passed said exhaust flow zone.
Claim 2
Dependent Claim 253 words
In a process for separating particulate matter from a contaminated gaseous medium containing said particulate matter therein, comprising: (A) passing said contaminated gaseous medium through a first swirl-inducing zone to form a swirling contaminated gaseous medium, (B) introducing said swirling contaminated gaseous medium into a cyclonic separation zone via a path adjacent an inner surface of a wall defining a periphery of said separation zone to separate at least a portion of said particulate matter from said swirling contaminated gaseous medium and form a gaseous product which is at least partially depleted in said particulate matter, and (C) removing said gaseous product from said separation zone through a gaseous exhaust flow zone disposed radially inwardly of said first swirl-inducing zone, the improvement for increasing separation efficiency, which comprises: (D) passing a substantially contaminant-free gaseous medium through a second swirl-inducing zone to form a co-swirling substantially contaminant-free gaseous medium, (E) introducing said co-swirling gaseous medium into said separation zone through an introduction zone disposed radially inwardly of said swirling contaminated gaseous medium and radially outwardly of said exhaust flow zone, and (F) employing an additional wall to separate said introduction zone from the so-introduced swirling contaminated gaseous medium, said additional wall extending into said separation zone, said exhaust flow zone extending into said separation zone further than said additional wall so extends, such that separation of the introduced co-swirling contaminated gaseous medium from the introduced swirling substantially contaminant-free gaseous medium is terminated before the swirling contaminated gaseous medium has passed said exhaust flow zone.
Claim 3
Dependent Claim 43 words
The process of claim 1 wherein said substantially contaminant-free gaseous medium is introduced in step (e) at a mass flow rate of at least 20% by weight of the combined mass flow rate of said contaminated gaseous medium plus said contaminant-free gaseous medium.
Claim 4
Dependent Claim 34 words
The process of claim 1 wherein said swirling and said co-swirling gaseous mediums are provided with respective directional flow components which are co-directional and generally parallel to an axis of said cyclonic separation zone.
Claim 5
Dependent Claim 40 words
The process of claim 1 wherein said contaminant-free gaseous medium is introduced in step (e) at a mass flow rate of at least 80% of the combined mass flow rate of said contaminated gaseous medium plus said contaminant-free gaseous medium.
Claim 6
Dependent Claim 16 words
The process of claim 1 wherein said separation zone is defined by a reverse flow cyclone.
Claim 7
Dependent Claim 21 words
The process of claim 1 wherein said swirling and said co-swirling gaseous mediums are introduced at approximately equal axial flow velocities.
Claim 8
Dependent Claim 253 words
In an apparatus for separating particulate matter from a contaminated gaseous medium containing said particulate matter therein, comprising: (A) means for passing said contaminated gaseous medium through a first swirl-inducing chamber to form a swirling contaminated gaseous medium, (B) means for introducing said swirling contaminated gaseous medium into a cyclonic separation chamber via a path adjacent an inner surface of a wall defining a periphery of said separation chamber to separate at least a portion of said particulate matter from said swirling contaminated gaseous medium and form a gaseous product which is at least partially depleted in said particulate matter, and (C) means for removing said gaseous product from said separation chamber through a gaseous exhaust flow conduit disposed radially inwardly of said first swirl-inducing chamber, the improvement for increasing separation efficiency, which comprises: (D) means for passing a substantially contaminant-free gaseous medium through a second swirl-inducing chamber to form a co-swirling substantially contaminant-free gaseous medium, and (E) means for introducing said co-swirling gaseous medium into said separation chamber through an introduction chamber disposed radially inwardly of said swirling contaminated gaseous medium and radially outwardly of said exhaust flow conduit, and wherein: (a) said introduction chamber is an annular chamber defined by the outer surface of said exhaust conduit and an additional wall disposed intermediate said outer surface of said exhaust conduit and the inner surface of the wall defining said periphery of said separation chamber, and (b) said exhaust conduit extends into said separation chamber further than said additional wall so extends.
Claim 9
Dependent Claim 253 words
In an apparatus for separating particulate matter from a contaminated gaseous medium containing said particulate matter therein, comprising: (A) means for passing said contaminated gaseous medium through a first swirl-inducing chamber to form a swirling contaminated gaseous medium, (B) means for introducing said swirling contaminated gaseous medium into a cyclonic separation chamber via a path adjacent an inner surface of a wall defining a periphery of said separation chamber to separate at least a portion of said particulate matter from said swirling contaminated gaseous medium and form a gaseous product which is at least partially depleted in said particulate matter, and (C) means for removing said gaseous product from said separation chamber through a gaseous exhaust flow conduit disposed radially inwardly of said first swirl-inducing chamber, the improvement for increasing separation efficiency, which comprises: (D) means for passing a substantially contaminant-free gaseous medium through a second swirl-inducing chamber to form a co-swirling substantially contaminant-free gaseous medium, and (E) means for introducing said co-swirling gaseous medium into said separation chamber through an introduction chamber disposed radially inwardly of said swirling contaminated gaseous medium and radially outwardly of said exhaust flow conduit, and wherein: (a) said introduction chamber is an annular chamber defined by the outer surface of said exhaust conduit and an additional wall disposed intermediate said outer surface of said exhaust conduit and the inner surface of the wall defining said periphery of said separation chamber, and (b) said exhaust conduit extends into said separation chamber further than said additional wall so extends.
Claim 10
Dependent Claim 28 words
The apparatus of claim 7, further comprising a base plug disposed generally at the bottom of said separation zone in coaxial relationship with a discharge opening formed therein.
Claim 11
Dependent Claim 108 words
The apparatus of claim 8, wherein said separation zone is defined peripherally by a composite conical-cylindrical wall including a cylindrical wall portion defining an upper region of said separation zone and a conical wall portion depending from said cylindrical wall portion and defining a lower region of said separation zone, said base plug including (i) a frusto-conical portion tapered downwardly through said opening in generally parallel relationship with said conical portion and (ii) an upwardly tapering portion disposed atop said frusto-conical portion and having a generally conical surface, said frusto-conical portion of said base plug being spaced inwardly from said conical wall portion of said separation zone-defining wall.

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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) 1983-07-15 1984-01-14 1984-07-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-07-15 1988-01-14 1988-07-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-07-15 1992-01-14 1992-07-15 $7700.00 Window Closed / Lapsed

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