GB2287667A - Cyclone inlet - Google Patents
Cyclone inlet Download PDFInfo
- Publication number
- GB2287667A GB2287667A GB9505166A GB9505166A GB2287667A GB 2287667 A GB2287667 A GB 2287667A GB 9505166 A GB9505166 A GB 9505166A GB 9505166 A GB9505166 A GB 9505166A GB 2287667 A GB2287667 A GB 2287667A
- Authority
- GB
- United Kingdom
- Prior art keywords
- cyclone
- inlet unit
- cyclone inlet
- unit according
- vanes
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C11/00—Accessories, e.g. safety or control devices, not otherwise provided for, e.g. regulators, valves in inlet or overflow ducting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/02—Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
- B04C5/04—Tangential inlets
Abstract
A cyclone inlet unit comprising three vanes (21) defining three inlet orifices (33). The vanes are shaped so that the orifices are each of gradually decreasing cross-sectional area towards the interior of the unit. The vanes may be integrally formed with a plate-like end portion. Alternatively the vanes are detachably secured and their positions adjustable. <IMAGE>
Description
CYCLONE INLET UNIT
This invention relates to a cyclone inlet unit, particularly to an inlet unit of a cyclone for use in separating oil and water mixtures e.g. the oil being in droplet form dispersed in water or vice versa.
When using a cyclone for separating oil from a mixture of oil and water containing relatively small quantities of oil e.g. up to 20% oil, the separating efficiency may be significantly dependent on the geometrical features thereof.
One such important feature is the construction and arrangement of the inlet or inlets through which the mixture to be separated enters the cyclone so as to promote the formation of a vortex. For example, the shape and/or configuration of the inlet or inlets may limit the separating efficiency because of effects such as turbulence causing break-up of the oil droplets in the mixture being fed to the cyclone.
It is an object of the present invention to provide a cyclone inlet unit wherein the aforementioned disadvantages are reduced or overcome.
In accordance with the invention a cyclone inlet unit comprises three vanes between which are three inlet orifices, each orifice having a rectangular cross-sectional area and lying between two sidewalls, one on one vane and the other on another adjacent vane, each orifice being of gradually decreasing cross-sectional area towards the interior of the unit, at least one of the sidewall surfaces having a convex profile.
Both sidewall surfaces may have convex profiles or one may be convex and the other planar.
The rectangular orifices may be such that the length in an axial direction with respect to the cyclone is much greater than the length in a radial direction.
Each orifice may have a portion of unchanging cross-sectional area, said portion being directed along a tangent to the cyclone. The orifices are preferably equi-spaced around the near-cylindrically shaped interior of the unit.
The three vanes, may each be adjustable in position to vary the radial widths of the orifices and to change the rate of decreasing cross-sectional area of each of the openings leading to the orifices.
Two embodiments of the invention will now be described by way of example only with respect to the accompanying drawings of which:
Figure 1 shows a radial cross-section through an inlet unit in
accordance with the first embodiment;
Figure 2 shows an axial cross-section on line ll-ll of Figure 1; and
Figure 3 shows a radial cross-section through an inlet unit in
accordance with the second embodiment of the
invention.
In general a cyclone separator comprises a tapered tube (not shown) into which a mixture of material e.g. oil and water, to be separated is fed tangentially through an inlet or inlets at or adjacent the wide end of the tube.
A vortex is formed and the more dense material e.g water migrates to the outer parts of the tube and out through the narrow end of the tapered tube (known as the underflow outlet) and the less dense material e.g. oil migrates to the central core of the vortex in the tube, and out through an outlet on the axis, usually at the wide end (known as the overflow outlet). A separator tube is described in GB Patent No. 1583742.
The inlet unit of either embodiment is, in use, attached by bolts or other means to an end flange situated at the wide end of the tapered cyclone separator tube.
The unit 1 of the first embodiment shown in Figures 1 and 2 is made from a single piece of metal e.g. stainless steel, by suitable known techniques e.g. casting and machining, so as to have an end plate-like portion 2 which extends perpendicularly to the axis 0-0 of the cyclone and three vanes 3,4,5 extending in overlapping arrangement around the edge of the portion 2. A central circular bore 6 is formed in the plate-like portion and retains e.g. by force fitting, a cylindrical overflow outlet unit 7.
The three vanes define and separate three rectangular orifices 8,9,10 through which material to be separated is introduced at an appropriate velocity into the cyclone to form a vortex. Typically the axial length of each orifice is 20 mm. The radially inner side 11 of each vane is smoothly concavely curved from a very narrow portion 12, typically 1 mm wide, lying alongside the radially inner side of an orifice, and having a diameter D1 of 60 mm (which matches the maximum diameter of the tapered separator tube) towards the radially outer side of the next orifice spaced apart therefrom by 120 with respect to the axis of the separator. The diameter D2 of this radially inner surface at the next orifice is 67 mm, the increasing radius between one orifice and the next being directly proportional to the angular change.Thus, for example, the diameter D3 at a position 6Oa from one orifice is 63.5mm.
The entrance 13 to each orifice 8 has a constant rectangular crosssectional shape, the radial width being 2.5 mm for a tangential distance d of 3.0 mm. The radially outer surface 14 of a vane defining the inner surface of an orifice is convex, having a radius of curvature, beyond the initial 3.0 mm at the orifice entrance, of 144 mm. The radially inner surface 15 of a vane, defining the radially outer surface of an orifice is also convexly curved having a radius of curvature, beyond the initial 3.00 mm at the orifice entrance, of 13 mm decreasing to 2mm. The entrance to an orifice is therefore generally funnel-shaped, as can be seen in Figure 1.
The radially outer surface of each vane may be provided with recesses such as 16 to allow space for external attachment means such as a bolt, which is used to hold the various components of the separator together.
The unit 20 of the second embodiment shown in Figure 3 also comprises three overlapping vanes 21,22,23 of metal e.g. stainless steel, but in this instance the vanes are not integrally formed with the plate-like end portion 35. The vanes define inlet orifices 31, 32, 33. Each vane has a radially inner surface 24 having a curved profile which is the same as the radially inner surface of each vane of the first embodiment. However the radially outer surface 25 of each vane, defining the inner surface of an orifice entrance, is planar in this embodiment.
The three vanes are each provided with two bores 26,27, each parallel to the cyclone axis, one bore 26 being circular, and the other 27 being in the form of an elongated slot. This enables each vane to be bolted to the plate like portion 35 and the positions of each vane to be adjusted slightly to provide the optimum separating efficiency. Thus the narrow tips of each vane may remain positioned on an imaginary circle of 60mm diameter, while the position of the curved radially inner face defining the radially outer extremity of an orifice may be adjusted radially outwardly or inwardly so as to widen or narrow an orifice.
The use of a unit according to the invention having three inlet orifices provides reduced area wetted by the mixture inside the tapered tube compared to a unit having fewer inlets of the same radial width, larger surface areas causing greater frictional losses leading to reduced vortex velocities.
Claims (12)
1. A cyclone inlet unit comprising three vanes between which are three inlet orifices, each orifice having a rectangular cross-sectional area aligned between two sidewalls, one on one vane and the other on another, adjacent vane, each orifice being of gradually decreasing cross-sectional area towards the interior of the unit, at least one of the sidewall surfaces having a convex profile.
2. A cyclone inlet unit according to Claim 1 wherein both sidewalls have convex profiles.
3. A cyclone inlet unit according to Claim 1 wherein one sidewall has a convex profile and the other sidewall is planar.
4. A cyclone inlet unit according to any one of the preceding claims wherein the rectangular orifices are such that the length in an axial direction with respect to the cyclone is much greater than the length in a radial direction.
5. A cyclone inlet unit according to any one of the preceding claims wherein each orifice has a portion of unchanging cross-sectional area, said portion being directed along a tangent to the cyclone.
6. A cyclone inlet unit according to any one of the preceding claims wherein the orifices are equi-spaced around the interior of the unit.
7. A cyclone inlet unit according to any one of the preceding claims having a near-cylindrically-shaped interior.
8. A cyclone inlet unit according to any one of the preceding claims wherein the three vanes are adjustable in position to vary the radial width of the orifices.
9. A cyclone inlet unit according to any one of the preceding claims wherein the three vanes are adjustable in position to change the rate of decreasing cross-sectional area of each of the openings leading to the orifices.
10. A cyclone inlet unit according to any one of the preceding claims wherein the three vanes are connected to a plate-like end portion forming an end of the cyclone.
11. A cyclone inlet unit substantially as described herein with reference to and as illustrated in Figures 1 and 2 of the accompanying drawings.
12. A cyclone inlet unit substantially as described herein with reference to and as shown in Figure 3 of the accompanying drawings.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9406077A GB9406077D0 (en) | 1994-03-26 | 1994-03-26 | Cyclone inlet unit |
Publications (2)
Publication Number | Publication Date |
---|---|
GB9505166D0 GB9505166D0 (en) | 1995-05-03 |
GB2287667A true GB2287667A (en) | 1995-09-27 |
Family
ID=10752603
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9406077A Pending GB9406077D0 (en) | 1994-03-26 | 1994-03-26 | Cyclone inlet unit |
GB9505166A Withdrawn GB2287667A (en) | 1994-03-26 | 1995-03-15 | Cyclone inlet |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9406077A Pending GB9406077D0 (en) | 1994-03-26 | 1994-03-26 | Cyclone inlet unit |
Country Status (2)
Country | Link |
---|---|
GB (2) | GB9406077D0 (en) |
WO (1) | WO1995026233A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997049862A1 (en) * | 1996-06-21 | 1997-12-31 | Alfa Laval Ab | Method and apparatus for removing neutral buoyancy contaminants from a cellulosic pulp |
US8973215B2 (en) | 2012-07-18 | 2015-03-10 | Techtronic Floor Care Technology Limited | Cyclonic vacuum cleaner and dirt separator |
US20210323003A1 (en) * | 2018-09-06 | 2021-10-21 | Sand Separation Technologies Inc. | Counterflow vortex breaker |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4486207A (en) * | 1981-06-22 | 1984-12-04 | Atlantic Richfield Company | Apparatus for reducing attrition of particulate matter in a chemical conversion process |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1753972A (en) * | 1924-02-05 | 1930-04-08 | Centrifix Corp | Centrifugal apparatus |
DE756646C (en) * | 1941-09-05 | 1953-06-15 | Willy Neumann | Centrifugal dust separator for internal combustion engines |
US3969096A (en) * | 1974-10-16 | 1976-07-13 | E. I. Du Pont De Nemours And Company | Cyclone separator having multiple-vaned gas inlets |
FR2629371B1 (en) * | 1988-03-29 | 1991-05-17 | Stumm Eric | DEVICE FOR DUST COLLECTION OF INDUSTRIAL GASES BY MECHANICAL - PNEUMATIC SEPARATORS |
-
1994
- 1994-03-26 GB GB9406077A patent/GB9406077D0/en active Pending
-
1995
- 1995-03-15 WO PCT/GB1995/000551 patent/WO1995026233A1/en active Application Filing
- 1995-03-15 GB GB9505166A patent/GB2287667A/en not_active Withdrawn
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4486207A (en) * | 1981-06-22 | 1984-12-04 | Atlantic Richfield Company | Apparatus for reducing attrition of particulate matter in a chemical conversion process |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997049862A1 (en) * | 1996-06-21 | 1997-12-31 | Alfa Laval Ab | Method and apparatus for removing neutral buoyancy contaminants from a cellulosic pulp |
US8973215B2 (en) | 2012-07-18 | 2015-03-10 | Techtronic Floor Care Technology Limited | Cyclonic vacuum cleaner and dirt separator |
US10016110B2 (en) | 2012-07-18 | 2018-07-10 | Techtronic Floor Care Technology Limited | Cyclonic vacuum cleaner and dirt separator |
US20210323003A1 (en) * | 2018-09-06 | 2021-10-21 | Sand Separation Technologies Inc. | Counterflow vortex breaker |
US11839884B2 (en) * | 2018-09-06 | 2023-12-12 | Sand Separation Technologies Inc. | Counterflow vortex breaker |
Also Published As
Publication number | Publication date |
---|---|
WO1995026233A1 (en) | 1995-10-05 |
GB9406077D0 (en) | 1994-05-18 |
GB9505166D0 (en) | 1995-05-03 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
WAP | Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1) |