Axisymmetrical separator for separating particulate matter from a fluid carrying medium

• US 4,469,497 A
• Filed: 02/04/1982
• Issued: 09/04/1984
• Est. Priority Date: 02/04/1982
• Status: Expired due to Fees

• Current Assignee: Dulux Australia Limited, Linhardt & Associates Incorporated
• Original Assignee: Linhardt & Associates Incorporated
• Inventors: Linhardt, Hans D.
• Primary Examiner(s): LACEY, DAVID LYNN
• Application Number:
  US06/345,731
• Time in Patent Office: 943 Days
• Field of Search: 55/17, 55/261, 55/263, 55/277, 55/282, 55/343, 55/347, 55/391, 55/392, 55/458, 55/461, 55/DIG. 14, 55/394, 55/397, 55/431, 210/512.1, 210/512.2, 209/143, 209/145
• US Class Current: 55/282
• CPC Class Codes: B01D 45/12 by centrifugal forces centrifuges B04B; cyclones B04C
• CPC Class Codes: Y10S 55/14 Inertia separator

Abstract

A separator for separating particles carried in a fluid carrying medium is disclosed. The separator includes an elongated duct and associated openings incorporated in a solid body. The duct is axisymmetrical relative to its longitudinal axis, and includes a curved wall portion having a curved cross-section taken along the longitudinal axis. An axisymmetrical opening located downstream of the curved wall portion leads from the duct into an axisymmetrical channel which is substantially radially disposed relative to the longitudinal axis. Continuation of the duct downstream of the opening is a discharge portion which is substantially colinear with the longitudinal axis. In operation, a substantial majority of the fluid carrying medium leaves the duct radially through the opening and channel in a state substantially free of particles. A remaining small portion of the fluid carrying medium and a substantial majority of the particles are channelled into the discharge portion by centrifugal forces arising due to travel of the particles along the curved walls. For industrial scale separation of particles from a fluid carrying medium, such as for the clean-up of stack gases, an array of several hundred to several thousand of the separators is provided.

Claims

1. A separator adapted for separating particulate matter carried in a carrier gas, from the carrier gas, the separator comprising:

a solid body incorporating an opening leading into a duct having a substantially straight longitudinal axis, adjacent to the opening the duct having walls defining a nozzle axisymmetrically arranged relative to the longitudinal axis of the duct, the nozzle walls positioned at an angle α

relative to the longitudinal axis for accelerating the carrier gas toward the longitudinal axis, the duct having adjacent to and downstream from the nozzle a curved portion, the walls of said curved portion being comprised by the body and being axisymmetrical relative to the longitudinal axis of the duct and having an effective radius of curvature R, an opening being disposed in the duct adjacent to the curved portion, the opening leading into a channel formed in the body, a minimum diameter of the duct between the nozzle and the opening adjacent to the curved portion being D*, the opening and the channel being axisymmetrical relative to the longitudinal axis of the duct, the channel forming an angle β

with said longitudinal axis as measured from the downstream side of the axis for receiving the substantial majority of the gas, an outlet portion of the duct being adjacent to said opening, the walls of said outlet portion being formed by the body and being axisymmetrical relative to the longitudinal axis of the duct, said outlet portion having a diameter D₂, and terminating in a second opening in the body, the angle β

being at least 90° and

the sum of the angles α and

β

consisting of angle θ

wherein θ

is approximately between 120°

to 180°

, R is approximately between 0.04 to 0.20 inches, and D₂ /D* is approximately between 1.085 to 1.52, whereby the gas and particulate matter are subjected to a certrifugal force by the walls of the curved portion and the channel which carries the majority of the particulate matter to flow along the longitudinal axis and into the outlet portion together with an appropriate amount of carrier gas.

2. The separator of claim 1 wherein D* is approximately between 0.15 to 0.75 inches, and D₂ is approximately between 0.30 to 1.025 inches.

3. The separator of claim 1 wherein the body is a ceramic body.

4. The separator of claim 1 wherein the opening in the duct adjacent to the curved portion has a width of between 0.02 to 0.65 inches.

5. The separator of claim 1 wherein the angle θ

is approximately 135°

.

6. The separator of claim 1 wherein the nozzle is constructed and arranged to accelerate the flow of carrier gas to a maximum velocity in the diameter D* of the duct within the range of 0.04 to 0.2 Mach.

7. The separator of claim 1 wherein the body incorporates at least one collection slot, said collection slot being in communication with the channel and being adapted for collecting carrier gas substantially free of particulate matter larger than approximately 2 microns.

8. A system for separating particulate matter carried in a fluid-carrying medium, from the carrying medium, the system comprising an array of first collection elements, said elements being mounted parallel with one another for passing the carrying medium through the elements, each element comprising:

a solid body incorporating a first opening leading into a duct formed in the body, said first opening comprising an inlet to the duct, the body incorporating a second opening leading into the duct, the second opening comprising an outlet for the duct, the body incorporating a channel connected to the duct around the periphery thereof and having an outlet from the body, internal walls of body forming the duct and the channel, the duct having a substantially straight longitudinal axis, an inlet nozzle portion adjacent and downstream from the first opening, and a curved wall portion adjacent to the downstream of the inlet portion, the curved wall portion having a curved cross-section taken in the direction of the general longitudinal axis of the duct and joining the walls of the inlet nozzle portion with the adjacent walls of the channel to prevent turbulence of the medium and separation of the boundary layer as the medium flows through the inlet nozzle and into the channel, the channel being arranged so that medium entering the channel from a path parallel to the longitudinal axis will have a turning angle of greater than 90°

an outlet portion of the duct being disposed adjacent to and downstream of the channel, the outlet portion leading to the second opening, the inlet portion, the curved wall portion, the channel and the outlet portion all being axisymmetrical relative to the general longitudinal axis of the duct, whereby a substantial majority of the particulate matter carried in the fluid-carrying medium is forced to travel through the duct including the outlet portion of the duct and whereby a majority of the fluid-carrying medium exits from the duct through the channel in a state substantially free of particulate matter.

9. The system of claim 8 wherein the inlet nozzle portion of the duct of each element has substantially conically-shaped inner walls narrowing towards the curved wall portion whereby the flow of the fluid-carrying medium and the particulate are accelerated as the fluid-carrying medium passes through the inlet nozzle portion.

10. The system of claim 8 wherein the channel is approximately at a 135°

angle relative to the longitudinal axis of the duct as measured from the downstream side of the axis.

11. The system of claim 8 wherein each collection element is adapted for separating particulate matter from a gaseous carrying medium, wherein the walls of the inlet nozzle portion of the duct have an angle α

relative to the longitudinal axis of the duct, wherein the curved cross-section of the curved wall portion of the duct has an effective radius R, wherein the diameter of the duct in the curved wall portion is D*, wherein the channel has an angle β

relative to the longitudinal axis of the duct as measured from the downstream side of the axis, wherein the diameter of the outlet portion is D₂, wherein R is approximately between 0.04 to 0.20 inches, the sum of angles α and

β

is approximately between 130°

to 165°

, and the ratio of D₂ to D* is approximately between 1.085 to 1.52.

12. The system of claim 11 wherein D* is approximately between 0.15 to 0.75 inches, and D₂ is approximately between 0.30 to 1.025 inches.

13. The system of claim 11 comprising a multitude of additional collection elements, each additional collection element being as defined in claim 11, and wherein the inlet nozzle portion of the duct of each additional collection element is coupled to the outlet portion of the duct of one of the first collection elements.

14. The system of claim 8 comprising a multitude of additional collection elements, each additional collection element being as defined in claim 8, and wherein the inlet nozzle portion of the duct of each additional collection element is coupled to the outlet portion of the duct of one of the first collection elements.

15. The system of claim 13 or 14 wherein each additional collection element is dimensioned so that a flow velocity of the carrier gas in the curved wall portion of the duct of the additional collection element is substantially equal to the flow velocity of the carrier gas in the curved wall portion of the duct of the first collection element to which the additional collection element is coupled.

16. The system of claim 8 wherein the solid body incorporates at least one additional channel in fluid communication with the duct, the additional channel comprising injection means for injecting a purging medium into the duct for removing particulate matter adhered to the walls of the duct.

17. A system adapted for separating particulate matter carried in a carrier gas, from the carrier gas, the system comprising an array of separating elements mounted parallel relative to one another in the flow of the carrier gas, each element comprising:

a solid body and axisymmetrical duct means incorporated in the solid body for accelerating the flow of the carrier gas toward the longitudinal axis to a maximum velocity within the range of approximately 0.04 to 0.02 Mach;

axisymmetrical curved walls means adjacent to the duct means and downstream therefrom;

axisymmetrical outlet means disposed in the solid body adjacent to the curved wall means and downstream therefrom for directing a majority of the carrier gas through a turning angle within approximately the range of 130°

to 165°

, whereby the curved wall means and the outlet means subject the carrier gas and the particulate matter to a centrifugal force which causes a majority of the particulate matter to flow in a substantially cylindrical path without rotation along the longitudinal axis of the duct means and the carrier gas in a state substantially free of particulate matter to escape from the duct means by flowing outwardly relative to the longitudinal axis of the duct means and into the outlet means; and

axisymmetrical discharge means disposed in the solid body adjacent to the outlet means and downstream therefrom for discharging the majority of a particulate matter and a minor portion of the carrier gas from the solid body, the duct means, curved wall means, outlet means and discharge means all being axisymmetrical relative to the longitudinal axis.

18. The system of claim 17 wherein the duct means, curved wall means, outlet means and discharge means are formed by the internal walls of the solid body.

19. The system of claim 18 wherein the duct means comprise a substantially conically-shaped nozzle narrowing towards the curved wall means.

20. The system of claim 18 wherein the outlet means comprise an opening adjacent to the curved wall means and a channel in the solid body.

21. The system of claim 20 wherein the discharge means comprise a discharge duct.

22. In a separator for separating particulate matter from a fluid-carrying medium the combination comprising:

a duct having a longitudinal axis and the following components arranged serially and axisymmetrically with respect to the longitudinal axis, an inlet nozzle for accelerating the medium toward the longitudinal axis, a curved wall section, an annular opening in the periphery of the duct and a particulate outlet portion; and

means defining an outlet channel for the fluid-carrying medium connected to the annular opening, the outlet channel being disposed at an angle β

with respect to the longitudinal axis as measured from the downstream side of the axis, the angle β

being equal to or greater than 90°

, the curved wall section forming a smooth transition between the wall of the inlet nozzle and the adjacent outlet channel wall to prevent turbulence of the fluid-carrying medium and separation of the boundary layer as the medium flows from the inlet nozzle into the outlet channel;

the inlet nozzle, being constructed and arranged to accelerate the flow of the fluid-carrying medium to a maximum velocity within the duct of between 0.04 and 1.0 Mach, whereby the fluid-carrying medium and the particulate matter carried therein is subjected to a centrifugal force as the medium is directed through the nozzle along the curved wall section and into the outlet channel to cause a substantial majority of the particulate matter to follow the longitudinal axis into the outlet portion of the duct while a substantial majority of the fluid-carrying medium is directed through the outlet channel.

23. The separator of claim 22 wherein the inlet nozzle has substantially conically-shaped walls which are positioned at an angle α

relative to the longitudinal axis as measured from the upstream side of the longitudinal axis, the sum of the angles α and

β

being within the range of about 130°

to 165°

.

24. The separator of claim 23 wherein the curved wall section has an effective radius of curvature R, where R is within the range of about 0.04 to 0.20 inches.

25. The separator of claim 24 wherein the smallest diameter of the nozzle and curved wall section is D*, the diameter of the outlet portion is D₂ and the ratio of D* to D₂ is approximately between 1.085 to 1.52.

26. The separator of claim 25 wherein D* is approximately between 0.15 to 0.75 inches, and D₂ is approximately between 0.30 to 1.025 inches.

27. The separator of claim 22 where the nozzle is constructed and arranged to accelerate the flow of the fluid-carrying medium to a maximum flow velocity within the duct of between 0.04 and 0.2 Mach.

28. The separator of claim 27 wherein the annular opening for receiving the substantial majority of the fluid-carrying medium has a width of approximately 0.03 to 0.165 inches.

29. The separator of claim 27 wherein the duct and the outlet channel are arranged to direct approximately 95% of the fluid-carrying medium into the outlet channel.