AU3531300A - Cyclone - Google Patents
Cyclone Download PDFInfo
- Publication number
- AU3531300A AU3531300A AU35313/00A AU3531300A AU3531300A AU 3531300 A AU3531300 A AU 3531300A AU 35313/00 A AU35313/00 A AU 35313/00A AU 3531300 A AU3531300 A AU 3531300A AU 3531300 A AU3531300 A AU 3531300A
- Authority
- AU
- Australia
- Prior art keywords
- cyclone according
- separating chamber
- cyclone
- metal sheet
- base material
- 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.)
- Abandoned
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
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
-
- 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
- B04C5/08—Vortex chamber constructions
Description
AUSTRALIA
Patents Act 1990 COMPLETE SPECIFICATION STANDARD PATENT Applicant(s): VOEST-ALPINE INDUSTRIEANLAGENBAU GmbH Invention Title:
CYCLONE
The following statement is a full description of this invention, including the best method of performing it known to me/us:
IA
Cyclone The invention relates to a cyclone for separating solids particles out of a gas flow, having a separating chamber, a dust-laden-gas feed which opens into the separating chamber, a clean-gas discharge line leading away from the separating chamber, and a solids discharge line leading away from the separating chamber.
Cyclones are widely used in industry for cleaning off-gases from, for example, ore-reduction plants, sintering plants or in the cement-producing sector, and are also employed in fluidized-bed reactors for separating out fine material which has been discharged with the fluidizing gas.
o00 The important criteria for the operation of a cyclone are, firstly, the degree of separation achieved and, in addition, the energy required to operate the cyclone, which for a specific cyclone and a given 20 amount of gas and solids loading, is dependent on the pressure loss between dust-laden-gas feed and clean-gas discharge line.
Therefore, the aim of cyclone manufacturers and operators is to achieve degrees of separation which are as high as possible and pressure losses which are as low as possible. While the degree of separation which can be achieved is dependent upon a large number of factors, such as the geometry of the cyclone, the grain-size range of the solids to be separated out, and the amount and velocity of gas, for a given geometry the pressure loss can only be varied by a change in the gas velocity. However, this also changes the degree of separation, which at least in general should remain constant.
Therefore, the object of the present invention is to provide a cyclone which exhibits a considerably reduced pressure loss compared to the prior art, while the degree of separation, however, is to remain substantially constant.
2 The object which is set according to the invention is achieved by the fact that at least part of the inner surface of the separating chamber is provided with a structure which increases the wall roughness of the surface and is formed by a multiplicity of structure elements which are at short distances from one another.
Surprisingly, it has been found that this measure enables the pressure loss between dust-laden- 10 gas feed and clean-gas discharge line to be reduced by S•up to 37%, while the degree of separation remains entirely constant or decreases only to an insignificant S• extent.
Advantageously, the entire inner surface of the 15 separating chamber is provided with the structure which increases the wall roughness of the surface, so that the effect of the reduction in the pressure loss is **.particularly strongly emphasized.
According to one advantageous embodiment, in addition the inner surfaces of the dust-laden-gas feed and/or the clean-gas discharge line and/or the solids discharge line are provided with the structure. This further enhances the effect of the reduction in pressure loss.
According to a preferred embodiment, a metal sheet, which bears substantially flat against the length of the corresponding surface or is arranged at a short distance from and parallel to the corresponding surface, is provided with the structure. This embodiment is particularly simple to achieve in design terms. Such a metal sheet is easy to replace during maintenance of the cyclone.
According to a further embodiment, the base material of the corresponding inner surface is provided with the structure.
For this purpose, the individual structure elements are rolled into the base material of the corresponding component, for example the separating chamber or the metal sheet, prior to final assembly. Of 3 course, it is also possible for the structure to be applied by manufacturing steps other than rolling, for example by milling or by welding on individual structure elements.
Individual structure elements may be formed by grooves, webs, polygonal or rounded plates or platelets or depressions or recesses.
According to a further embodiment, the structure is formed by a metal mesh, i.e. the 10 individual structure elements are formed by holes and webs, i.e. the individual perforations in the metal mesh.
According to a further preferred embodiment, the structure is formed by expanded metal. Expanded D 15 metal is initially formed by a metal sheet into which rows of slots are cut or punched, the individual rows being offset from one another by approximately half a slot length. Stretching of the metal sheet imparts the typical mesh-like structure to the latter.
20 Advantageously, the dimensions of individual structure elements are selected in such a way that their dimensions with the separating chamber having a substantially circular horizontal cross section measured parallel to the surface and in the circumferential direction of the cross section of the separating chamber amount to up to 5 cm.
The novel effect of the reduction in the pressure drop brought about by the increased wall roughness occurs up to a level of 5 cm.
According to a further advantageous feature, the dimensions of individual structure elements perpendicular to the surface of the separating chamber, i.e. their height or depth, are up to 1 cm.
A cyclone according to the invention is explained in more detail below with reference to the drawing, Fig. 1.
Fig. 1 diagrammatically depicts a cyclone according to the invention in cross section, having a separating chamber i, having a dust-laden-gas feed 2 4 opening substantially tangentially into the separating chamber i, having a clean-gas discharge line 3 leading away from the separating chamber 1, and having a solids discharge line 4 leading away from the separating chamber i.
The inner surface 5 of the separating chamber is provided with a structure 6 which increases its wall roughness and in this case is formed by a metal mesh.
For the purposes of this specification it will be clearly understood that the word "comprising" means "including but not limited to", and that the word "comprises" has a corresponding meaning.
o *o o* *o
Claims (10)
- 2. Cyclone according to Claim 1, characterized in that substantially the entire inner surface of the *.":separating chamber is provided with the structure
- 3. Cyclone according to one of Claims 1 and 2, 20 characterized in that in addition the inner surfaces of the dust-laden-gas feed and/or the clean-gas discharge line and/or the solids discharge line (4) are provided with the structure (6)
- 4. Cyclone according to one of Claims 1 to 3, characterized in that a metal sheet, which bears substantially flat against the length of the corresponding surface or is arranged at a short distance from and parallel to the corresponding surface, is provided with the structure (6)
- 5. Cyclone according to one of Claims 1 to 3, characterized in that the base material of the corresponding inner surface is provided with the structure (6)
- 6. Cyclone according to one of Claims 1 to characterized in that the structure is formed by structure elements which are made, preferably by rolling or milling, in the base material of the corresponding surface or of the metal sheet. 6
- 7. Cyclone according to one of Claims 1 to 6, characterized in that the structure is formed by structure elements which are applied, preferably by welding, to the base material of the corresponding surface or of the metal sheet.
- 8. Cyclone according to one of Claims 1 to 4, characterized in that the structure is formed by a metal mesh.
- 9. Cyclone according to one of Claims 1 to 4, 10 characterized in that the structure is formed by 0 expanded metal.
- 10. Cyclone according to one of Claims 1 to 9, in which the separating chamber has a substantially circular horizontal cross section, characterized in Q.O 15 that the dimensions of individual structure elements, e*SS measured parallel to the surface and in the circumferential direction of the cross section of the separating chamber are up to 5 cm.
- 11. Cyclone according to one of Claims 1 to 20 characterized in that the dimensions of individual structure elements, measured perpendicular to the surface of the separating chamber are up to 1 cm. Dated this 15th day of May 2000 VOEST-ALPINE INDUSTRIEANLAGENBAU GMBH By their Patent Attorneys GRIFFITH HACK Fellows Institute of Patent and Trade Mark Attorneys of Australia
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT98899A AT406831B (en) | 1999-06-02 | 1999-06-02 | Cyclone |
AT988/99 | 1999-06-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
AU3531300A true AU3531300A (en) | 2000-12-07 |
Family
ID=3504370
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU35313/00A Abandoned AU3531300A (en) | 1999-06-02 | 2000-05-15 | Cyclone |
Country Status (3)
Country | Link |
---|---|
AT (1) | AT406831B (en) |
AU (1) | AU3531300A (en) |
DE (1) | DE10023009A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7377960B2 (en) * | 2004-04-07 | 2008-05-27 | Engineered Support Systems, Inc. | Cyclonic separator with secondary vortex break |
PL2792646T3 (en) * | 2013-04-16 | 2015-11-30 | Demon Gmbh | Method and system for treating waste water containing ammonium |
-
1999
- 1999-06-02 AT AT98899A patent/AT406831B/en not_active IP Right Cessation
-
2000
- 2000-05-11 DE DE2000123009 patent/DE10023009A1/en active Pending
- 2000-05-15 AU AU35313/00A patent/AU3531300A/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
DE10023009A1 (en) | 2000-12-07 |
ATA98899A (en) | 2000-02-15 |
AT406831B (en) | 2000-09-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU593977B2 (en) | Cyclone | |
MX2012011373A (en) | Wear-resistant separator for separating sand and rock particles. | |
CA2404800A1 (en) | Method and apparatus for separating particles from hot gases | |
KR101922067B1 (en) | Method for separating gas in a fluidized gas/solid mixture | |
EP0800359A1 (en) | Shroud and cyclonic cleaning apparatus incorporating same | |
EP2431096B1 (en) | Cyclone separator | |
EP3703863B1 (en) | Vortex mill and method of vortex milling for obtaining powder with customizable particle size distribution | |
AU3531300A (en) | Cyclone | |
US6257415B1 (en) | Multi-outlet diffuser system for classifier cones | |
WO2001008781A2 (en) | Cellulose based filter media and cartridge apparatus | |
US5657877A (en) | Rotary classifier for a roller mill | |
JP2003505244A5 (en) | ||
US4224145A (en) | Vortex cleaner | |
CA2016865A1 (en) | Cone wear detection | |
US3854902A (en) | Method of filtering gas | |
US20020014707A1 (en) | Method of flue gas conditioning and a flue gas conditioning device | |
US10258923B2 (en) | Systems and methods for catalyst screens in selective catalytic reduction reactors | |
Kumar et al. | Study of the fluid dynamic performance of distributor type in torbed type reactors | |
RU2006116262A (en) | ARMOR OF A CONE CRUSHER AND METHOD FOR ITS MANUFACTURE | |
CN215879135U (en) | Boiling air tap for boiling dust-removing hopper | |
JP6640262B2 (en) | Ceramic filter dust collector | |
RU2233706C1 (en) | Dressing device | |
RU2813178C1 (en) | Centrifugal disc grinder | |
SU673565A1 (en) | Apparatus for varying the direction of gas-suspended particle flow | |
EP3000525A1 (en) | Fluidized bed reactor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
DA3 | Amendments made section 104 |
Free format text: THE NATURE OF THE AMENDMENT IS: AMEND THE PRIORITY DETAILS TO CORRECT THE DATE TO 1999 |
|
MK1 | Application lapsed section 142(2)(a) - no request for examination in relevant period |