MULTI-STAGE AXIAL FLOW CYCLONE SEPARATOR

• US 20180161785A1
• Filed: 02/08/2016
• Published: 06/14/2018
• Est. Priority Date: 06/02/2015
• Status: Active Grant

• Current Assignee: Luxnara Yaovaphankul
• Original Assignee: Luxnara Yaovaphankul
• Inventors: Yoavaphankul, Metha
• Granted Patent: US 10,639,651 B2
• Time in Patent Office: Days
• CPC Class Codes: B01D 21/267 by using a cyclone
• CPC Class Codes: B01D 45/08 by impingement against baffle separators
• CPC Class Codes: B01D 45/12 by centrifugal forces centrifuges B04B; cyclones B04C
• CPC Class Codes: B01D 45/16 generated by the winding course of the gas stream , the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
• CPC Class Codes: B01D 50/20 Combinations of devices covered by groups B01D45/00 and B01D46/00
• CPC Class Codes: B04C 2003/006 Construction of elements by which the vortex flow is generated or degenerated
• CPC Class Codes: B04C 3/04 Multiple arrangement thereof combined with types according to other groups, B04C7/00
• CPC Class Codes: B04C 3/06 Construction of inlets or outlets to the vortex chamber
• CPC Class Codes: F01M 13/04 having means for purifying air before leaving crankcase, e.g. removing oil

Abstract

A multi-stage axial flow cyclone separator comprising a primary swirl creating section, a swirl acceleration section, and a fluid separation section is disclosed. A fluid transfer tube is mounted axially in the middle of the inside of an outer structure of the fluid separation section for separating the light phase fluid and transferring it through an open end. Additionally, the swirl acceleration section and the fluid separation section can be annexed to a multi-stage axial flow cyclone separator according to the present invention to increase the velocity of the swirl and to increase the residence time to improve separation efficiency as desired.

Claims

1. A multi-stage axial flow cyclone separator comprising:

a primary swirl creating section (1) comprising an outer structure (4) having an open end and an inside fluid distribution chamber (5) for distributing fluid received from a primary fluid inlet (6) formed as at least one hole on a lateral side of the outer structure (4) or as at least one tube extending from the lateral side of the outer structure (4) for serving as ports for transferring fluid to the fluid distribution chamber (5) for transferring to a primary swirl generating chamber (7) of an apparatus for creating a swirling flow (8) mounted inside the outer structure (4),

wherein the apparatus for creating a swirling flow (8) is formed as an axial structure placed wholly or partially inside the outer structure (4) wherein the inside thereof is formed as a cylindrical primary swirl generating chamber (7) and having at least one lateral side penetrable hole (9) for transferring fluid to the primary swirl generating chamber (7),

a swirl acceleration section (2) comprising an outer structure (14) having an open end in fluid communication with the primary swirl creating section (1) and an inside fluid distribution chamber (15) for distributing fluid received from a fluid inlet (16) formed as at least one hole on a lateral side of the outer structure (14) or at least one tube extending from the lateral side of the outer structure (14) for serving as ports for transferring fluid to the fluid distribution chamber (15) for transferring to a swirl acceleration chamber (17) of an apparatus for accelerating a swirling flow (18)

wherein the apparatus for accelerating a swirling flow (18) is formed as an axial structure disposed wholly or partially inside the outer structure (14) having an inside conic swirl acceleration chamber (17) for receiving fluid from the fluid distribution chamber (15) and having at least one lateral side penetrable hole (19) on a lateral side of the apparatus for accelerating a swirling flow (18) for serving as inlets for fluid flowing from the fluid distribution chamber (15) into the swirl accelerating chamber (17); and

a fluid separation section (3) comprising an outer structure (22) having an open end in fluid communication with the swirl acceleration section (2) and an inside space (23) for gathering a heavy phase of the fluid for transfer through a lateral side outlet (24) formed as at least one hole on a lateral side of the outer structure (22) or at least one tube extending from the lateral side of the outer structure (22) for serving as ports for transferring the heavy phase fluid, and a fluid transfer tube (25) axially mounted in a center inside the outer structure (22),

wherein the fluid transfer tube (25) is formed as a cylindrical tube having an inside cylindrical cavity (26) for serving as an outlet of light phase fluid and to provide an annulus space (27), wherein a diameter of the fluid transfer tube (25) is smaller than a circular hole formed on a center of the outlet open end of the swirl acceleration section (2) and wherein the annulus space (27) serves as a space for fluid separation for separating heavy phase fluid and transferring the fluid to the fluid gathering space (23).

3. The multi-stage axial flow cyclone separator according to claim 7, wherein the primary fluid inlet (6) axially draws the fluid from an upstream open end, the primary fluid inlet (6) comprising the closure plate (10) for closing only the open end of the apparatus for creating a primary swirling flow (8) at the upstream open end and opening a space around the apparatus for creating the primary swirling flow to allow the fluid to flow in the fluid distribution chamber (5) and to the primary swirl generating chamber (7) through the side penetrable hole (9).

4. The multi-stage axial flow cyclone separator according to claim 1, further comprising at least one conic extension comprising one of a conical accelerating section longitudinally connected with a fluid separation section or a cylindrical acceleration section longitudinally connected with the fluid separation section to be coupled to the fluid separation section (3).

5. The multi-stage axial flow cyclone separator according to claim any one of claim 1, wherein the fluid separation section (3) is a divergent type of fluid separation section.

6. The multi-stage axial flow cyclone separator according to claim 1, wherein an edge surface next to the lateral side penetrable hole (9) is a convex surface c wherein a beginning of the convex surface has a minimum angle to an emerging axis a of the lateral side penetrable hole (9) and the convex surface c is closer compared with other surfaces surrounding the emerging axis a of the lateral side penetrable hole (9), wherein the composition of said lateral side penetrable hole (9) and the convex surface c of the edge surface next to the lateral side penetrable hole (9) is in accordance with a Coanda profile wherein fluid through the penetrable hole is deflected to the convex surface c creating a Coanda effect inducing the fluid in the primary swirl generating chamber (7) to flow along a flow line A in a laminar manner on a plane of the curved surface c such that a laminar swirling flow is formed in the primary swirl generating chamber (7).

7. The multi-stage axial flow cyclone separator according to claim 1, wherein the open end of the outer structure (4) is formed as a closure plate (10) to direct the fluid only through an inlet of the primary fluid inlet (6).

8. The multi-stage axial flow cyclone separator according to claim 1, wherein an edge surface of the lateral side penetrable hole is a convex surface, a beginning of the convex surface having a minimum angle to an emerging axis of the lateral side penetrable hole (19) and the convex surface c′

is closer compared with other surfaces surrounding the emerging axis a′

of the side penetrable hole (19) wherein a composition of said lateral side penetrable hole (19) and the convex surface c′

is in accordance with a Coanda profile wherein fluid pressed through the penetrable hole is deflected to the convex surface c′

creating a Coanda effect inducing the fluid in the swirl accelerating chamber transferred from the primary swirl creating section (1) to flow along a flow line A′

in a laminar manner on a plane of the convex surface c′

such that a laminar swirling flow is formed in the swirl accelerating chamber (17), wherein a diameter of an upstream open end is larger than that of a downstream open end of a transmission base of the apparatus for accelerating the swirling flow (18), wherein the acceleration of the fluid is increased as a circumference is shortened along the slope of a conic base of the apparatus for accelerating the swirling flow (18) before the fluid is transferred to the fluid separation section (3).

9. The multi-stage axial flow cyclone separator according to claim 1, wherein one open end of the outer structure of the fluid separation section (22) is formed as an outer attaching flange (28) for serving as an edge for attaching the fluid transfer tube (25).

2. The multi-stage axial flow cyclone separator according to claim h wherein the primary swirl generating chamber (7) has a throat (20) for promoting formation of a swirling flow in the primary swirl generating chamber (7) in a sufficient amount and velocity before it is transferred.

10. A multi-stage axial flow cyclone separator comprising:

a primary swirl creating section (1) including;

an outer structure (4) having;

an open end, and

a fluid distribution chamber (5),

a primary fluid inlet (6) adjacent the outer structure (4) of the primary

swirl creating section (1),

a primary swirl generating chamber (7), and

a side penetrable hole (9) for transferring fluid from the fluid distribution chamber (5) to the primary swirl generating chamber (7);

a swirl acceleration section (2) including;

an outer structure (14) having;

an open end in fluid communication with the primary swirl creating section (1), and

an inside fluid distribution chamber (15),

a fluid inlet (16) adjacent the outer structure (14) of the swirl acceleration section (2),

a swirl acceleration chamber (17), and

a side penetrable hole (19) transferring fluid from the fluid distribution chamber (15) to the swirl acceleration chamber (17); and

a fluid separation section (3) including;

an outer structure (22) having;

an open end in fluid communication with the swirl acceleration section (2), and

an inside space (23),

a lateral side outlet (24) adjacent the outer structure (22) of the fluid separation section (3), and

a fluid transfer tube (25) axially mounted to a center inside the outer structure (22).

11. The multi-stage axial flow cyclone separator according to claim 10, further comprising an apparatus for creating a swirling flow (8) inside the outer structure (4) of the primary swirl creating section (1), the apparatus including:

the primary swirl generating chamber (7) formed as a cylindrical primary swirl generating chamber (7);

the side penetrable hole (9) formed as a lateral side penetrable hole (9); and

an edge surface adjacent the lateral side penetrable hole (9), the edge surface having a convex surface beginning section having a minimum angle relative to an emerging axis of the lateral side penetrable hole (9).

12. The multi-stage axial flow cyclone separator according to claim 10, further comprising an apparatus for accelerating a swirling flow (18) inside the outer structure (14) of the swirl acceleration section (2), the apparatus including:

the swirl acceleration chamber (17) formed as an inside conic swirl acceleration chamber (17);

the side penetrable hole (19) formed as a lateral side penetrable hole (19);

an edge surface adjacent the lateral side penetrable hole (19), the edge surface having a convex surface beginning section having a minimum angle relative to an emerging axis of the lateral side penetrable hole (19),

a downstream open end; and

an upstream open end, wherein a diameter of the upstream open end is larger than a diameter of the downstream open end.

13. The multi-stage axial flow cyclone separator according to claim 10, wherein the fluid transfer tube (25) of the fluid separation section (3) is a cylindrical tube having an inside cylindrical cavity (26) with a diameter less than a diameter of the downstream open end of the swirl acceleration section (2).

14. The multi-stage axial flow cyclone separator according to claim 10, wherein the open end of the outer structure (22) of the fluid separation section (3) includes an outer flange (28) for attaching to the fluid transfer tube (25).