EP0262568A2 - Cyclone - Google Patents
Cyclone Download PDFInfo
- Publication number
- EP0262568A2 EP0262568A2 EP87113876A EP87113876A EP0262568A2 EP 0262568 A2 EP0262568 A2 EP 0262568A2 EP 87113876 A EP87113876 A EP 87113876A EP 87113876 A EP87113876 A EP 87113876A EP 0262568 A2 EP0262568 A2 EP 0262568A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- cleaner according
- vortex cleaner
- conical
- main body
- diameter
- 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.)
- Granted
Links
Images
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D5/00—Purification of the pulp suspension by mechanical means; Apparatus therefor
- D21D5/18—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force
- D21D5/24—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force in cyclones
Definitions
- the invention relates to a vortex cleaner according to the preamble of claim 1.
- a vortex cleaner is known from European patent application 0058484.
- a central guide body is provided in the upper region of the essentially conical main body, but only one has approximately conical shape.
- An outlet chamber adjoins the conical part with the smaller diameter arranged at the bottom and has an essentially much larger diameter than the outlet end of the conical part and is penetrated centrally by the central separator tube for the light particles.
- the remaining variants according to this publication also show this discharge chamber.
- the cone angle of the conical part of the main body is between 2 ° and 5 °, i.e. the cone opening angle between 4 ° and 10 °, preferably the cone angle between 2.5 ° and 4 °, i.e. the cone opening angle is between 5 ° and 8 °.
- these angles of inclination are already known from the previous designs of the vortex cleaners.
- the cyclone which is used here preferably for separating solid contaminant particles from fiber suspensions, is shown here in the preferred installation position.
- the end with the larger diameter, which has the inlet part 3, is in the lower position and the part with the smaller diameter to which the outlet part 6 is connected is in the upper position, because here a fraction enriched with light soiling is present to be subtracted, which has specifically lighter components than the specific weight of the suspension (liquid)
- the reverse or a horizontal installation position is also possible.
- the middle part 2 is conical, while the inlet end 3 and outlet end 6 are essentially cylindrical.
- the length of the cylindrical inlet part 3 is approximately 0.6 times the conical part 2.
- a separator tube 5 for the light particles preferably light impurities such as polystyrene or light adhesive impurities and light dirt of another kind, also air and gases, runs centrally in its outlet part 6.
- the outlet part 6 is initially straight as far as it passes through the central separator tube 5 and then kinks with its outlet end 7 essentially at a right angle.
- the specifically relatively heavier suspension which is essentially freed from the light impurities, is then drawn off through the discharge opening 8 of the outlet part.
- the suspension is fed tangentially to the inlet part 3 via the inlet pipe 1, as a result of which it flows around the guide body 4 in a spiral-helical manner.
- the straight, cylindrical outlet part 6 settles without transitions, edges or jumps immediately as an extension of the conical part 2 of the main body.
- the central separator tube 5 extends a very small dimension into the conical part 2 of the main body, which can be between almost zero and approximately 5 or 10 mm.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Cyclones (AREA)
- Gas Separation By Absorption (AREA)
- Paper (AREA)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT87113876T ATE54477T1 (de) | 1986-09-30 | 1987-09-23 | Wirbelreiniger. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19863633150 DE3633150A1 (de) | 1986-09-30 | 1986-09-30 | Wirbelreiniger |
| DE3633150 | 1986-09-30 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP0262568A2 true EP0262568A2 (fr) | 1988-04-06 |
| EP0262568A3 EP0262568A3 (en) | 1989-02-08 |
| EP0262568B1 EP0262568B1 (fr) | 1990-07-11 |
Family
ID=6310646
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP87113876A Expired - Lifetime EP0262568B1 (fr) | 1986-09-30 | 1987-09-23 | Cyclone |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP0262568B1 (fr) |
| AT (1) | ATE54477T1 (fr) |
| DE (2) | DE3633150A1 (fr) |
| ES (1) | ES2016829B3 (fr) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1990000646A1 (fr) * | 1988-07-08 | 1990-01-25 | Wikdahl Nils Anders Lennart | Procede et dispositif d'epuration d'une suspension fibreuse par elimination de produits de contamination legers |
| WO2001022059A3 (fr) * | 1999-09-18 | 2001-10-18 | John Ernest Foster Holley | Procede de separation |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2787374A (en) * | 1951-09-20 | 1957-04-02 | Centriclone Corp | Centrifugal classifier |
| FR1257689A (fr) * | 1960-02-20 | 1961-04-07 | Cyclone retardateur | |
| CA1212648A (fr) * | 1981-02-14 | 1986-10-14 | John D. Peel | Cyclone separateur a decharge axiale descendante pour fractions legeres |
-
1986
- 1986-09-30 DE DE19863633150 patent/DE3633150A1/de active Granted
-
1987
- 1987-09-23 ES ES87113876T patent/ES2016829B3/es not_active Expired - Lifetime
- 1987-09-23 EP EP87113876A patent/EP0262568B1/fr not_active Expired - Lifetime
- 1987-09-23 AT AT87113876T patent/ATE54477T1/de active
- 1987-09-23 DE DE8787113876T patent/DE3763641D1/de not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1990000646A1 (fr) * | 1988-07-08 | 1990-01-25 | Wikdahl Nils Anders Lennart | Procede et dispositif d'epuration d'une suspension fibreuse par elimination de produits de contamination legers |
| AU627754B2 (en) * | 1988-07-08 | 1992-09-03 | N. A. Lennart Wikdahl | Hydrocyclone |
| WO2001022059A3 (fr) * | 1999-09-18 | 2001-10-18 | John Ernest Foster Holley | Procede de separation |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0262568B1 (fr) | 1990-07-11 |
| DE3763641D1 (de) | 1990-08-16 |
| DE3633150A1 (de) | 1988-04-07 |
| DE3633150C2 (fr) | 1991-02-28 |
| EP0262568A3 (en) | 1989-02-08 |
| ATE54477T1 (de) | 1990-07-15 |
| ES2016829B3 (es) | 1990-12-01 |
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