US2015464A - Separator - Google Patents
Separator Download PDFInfo
- Publication number
- US2015464A US2015464A US737033A US73703334A US2015464A US 2015464 A US2015464 A US 2015464A US 737033 A US737033 A US 737033A US 73703334 A US73703334 A US 73703334A US 2015464 A US2015464 A US 2015464A
- Authority
- US
- United States
- Prior art keywords
- mixture
- cone
- gas
- vanes
- cylindrical body
- 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.)
- Expired - Lifetime
Links
Images
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
- B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
- B04C5/13—Construction of the overflow ducting, e.g. diffusing or spiral exits formed as a vortex finder and extending into the vortex chamber; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow
-
- 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
-
- 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
- B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
Definitions
- the gas and the material with which it is loaded and from which it is to be separated are introduced tangentially and under pressure into the apparatus; they fall 5 together following a spiral circuit to the base of the apparatus which is airtight or connected to.
- this device consists essentially in a cone placed inside the cylindrical body of the cyclone or other device, the apex of the cone comprising an opening which serves for the removal of the gaseous fluid at the upper part of the apparatus while its base is connected to the wall of the cylindrical body by the intermediary of vanes preferably curved, and between which the material and the air are compelled to. pass.
- Figure 1 is a view in axial section of a cyclone provided with a distribution device set up according to the invention.
- Figure 2 is a plan view of the device shown in Figure 1. I w
- the cyclone-or separator comprises'in the ordinary manner a cylindrical body I, terminating at its lower part in a conical inverted portion 2 which is air-tight or connected to an air-tight receptacle (not shown).
- the mixture of gas and material is introduced tangentially into this cylindrical body by a pipe 3.
- the distribution of the mixture of gas and material in the interior of the cylindrical body I is ensured by a right '6 and the envelope I.
- vanes 1 are preferably curved towards the axis of the body I, and are 5 preferably uniformly distributed over the whole circumference.
- the gas containing in suspension the matter 10 to be separated is introduced tangentially into the space between the cone 6 and the cylindrical envelope I and assumes a spiraldescending movement in this space. During this movement the material distributes itself uniformly around the 15 cone 6 so that all the circumference of this cone is equally covered.
- the speeding up of the mixture of gas and material takes places progressively by reason of the progressive narrowing of the section of the space a between the cone 20
- the mixture speeds up more and more as it descends, and when it reaches the very narrow annular space b occupied by the vanes 1 it is automatically entrained and d1- rected into, the interior of the cyclone separator 25 proper across these vanes which are preferably curved so as better to direct the mixture by removing it from the wall of the body I.
- the motive force necessary for the injection ofthe mixture into the apparatus 30 may be substantially reduced due to the. phenomenon of the automatic and progressive increase of the speed of the mixture which is produced as has been seenabove by the progressive narrowing of the space a. 35
- Distribution device for cyclones, separators, 50 turbulence furnaces, and like apparatus, comprising in combination a cylindrical chamber, a conduit opening tangentially into said chamber adjacent the top thereof for the introduction of the mixture into the apparatus, an inverted cone dis- 55 right cone, an outlet conduit connected to said opening through which the gaseous fluid of the mixture may be discharged, and vanes between a the base of the right cone and the wall of the cylindrical chamber, said vanes being curved downwardly and inwardly towards the axis of the cylindrical body in the same direction of rotation as that of the incoming mixture.
Description
Sept. 24, 1935.
E. c. SAINT-JACQUES 2,015,464.
SEPARATOR Filed July 26. 1934 Patented Sept. 24, 1935 UNITED. STATES PATENT, OFFICE Application July 26,1934, Serial No. 737,033
In France August 10, 1933 1 Claim.
In an ordinary cyclone, the gas and the material with which it is loaded and from which it is to be separated are introduced tangentially and under pressure into the apparatus; they fall 5 together following a spiral circuit to the base of the apparatus which is airtight or connected to.
an airtight receptacle in which the material, after having been centrifuged against the wall of the apparatus during the turbulent movement of the descent, is precipitated, while the gas rises with little powder to be removed through the orifice arranged in the upper part of the cyclone separator.
In apparatus of this kind, in order to obtain a suificient rotation of the mixture of gas and material, it is necessary to provide at the point of injection of the mixture 2. pressure sufiiciently high and which increases with the diameter of the cyclone. Moreover, the friction of the mixture of the gas and material upon the wall of the apparatus absorbs a considerable part of the power used for its injection. Then with certain materials this friction produces a, considerable effect of abrasion. The present invention has for its object a dis .tribution device applicable not only to cyclones but even to all air separators, to turbulence furnaces and similar devices, and which permits these disadvantages to be minimized.
For this purpose this device consists essentially in a cone placed inside the cylindrical body of the cyclone or other device, the apex of the cone comprising an opening which serves for the removal of the gaseous fluid at the upper part of the apparatus while its base is connected to the wall of the cylindrical body by the intermediary of vanes preferably curved, and between which the material and the air are compelled to. pass.
The invention is illustrated by way of example in the accompanying drawing in which:
Figure 1 is a view in axial section of a cyclone provided with a distribution device set up according to the invention, and
Figure 2 is a plan view of the device shown in Figure 1. I w
The cyclone-or separator comprises'in the ordinary manner a cylindrical body I, terminating at its lower part in a conical inverted portion 2 which is air-tight or connected to an air-tight receptacle (not shown). The mixture of gas and material is introduced tangentially into this cylindrical body by a pipe 3.
According to the invention the distribution of the mixture of gas and material in the interior of the cylindrical body I is ensured by a right '6 and the envelope I.
cone 6 at the apex of which is attached the pipe 5 forv outlet of the gas and of which the base is connected to the wall of the bodyl by the intermediarylof vanes I. The vanes 1 are preferably curved towards the axis of the body I, and are 5 preferably uniformly distributed over the whole circumference.
The operation of the cyclone provided with such a device is as follows:
The gas containing in suspension the matter 10 to be separated is introduced tangentially into the space between the cone 6 and the cylindrical envelope I and assumes a spiraldescending movement in this space. During this movement the material distributes itself uniformly around the 15 cone 6 so that all the circumference of this cone is equally covered. The speeding up of the mixture of gas and material takes places progressively by reason of the progressive narrowing of the section of the space a between the cone 20 The mixture speeds up more and more as it descends, and when it reaches the very narrow annular space b occupied by the vanes 1 it is automatically entrained and d1- rected into, the interior of the cyclone separator 25 proper across these vanes which are preferably curved so as better to direct the mixture by removing it from the wall of the body I.
Thus at first the motive force necessary for the injection ofthe mixture into the apparatus 30 may be substantially reduced due to the. phenomenon of the automatic and progressive increase of the speed of the mixture which is produced as has been seenabove by the progressive narrowing of the space a. 35
Then, the matter is better distributed as has been seen over the whole of the circumference of the apparatus and instead of arriving at a lump at a single point, it has a greater tendency to remove itself from the wall of the cylindrical body 40 due to the action of the vanes. The abrasive effect is thus substantially reduced.
Finally, it will be observed that the conditions of operation of the apparatus are always constant since for a definite angle of the cone 6 45 the height of this latter is always proportional to the maximum diameter of the cylindrical body I.
What is claimed is:--
Distribution device for cyclones, separators, 50 turbulence furnaces, and like apparatus, comprising in combination a cylindrical chamber, a conduit opening tangentially into said chamber adjacent the top thereof for the introduction of the mixture into the apparatus, an inverted cone dis- 55 right cone, an outlet conduit connected to said opening through which the gaseous fluid of the mixture may be discharged, and vanes between a the base of the right cone and the wall of the cylindrical chamber, said vanes being curved downwardly and inwardly towards the axis of the cylindrical body in the same direction of rotation as that of the incoming mixture.
EUGENE CAMILLE SAINT-JACQUES-
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR613087X | 1933-08-10 |
Publications (1)
Publication Number | Publication Date |
---|---|
US2015464A true US2015464A (en) | 1935-09-24 |
Family
ID=8979273
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US737033A Expired - Lifetime US2015464A (en) | 1933-08-10 | 1934-07-26 | Separator |
Country Status (5)
Country | Link |
---|---|
US (1) | US2015464A (en) |
BE (1) | BE406007A (en) |
DE (1) | DE613087C (en) |
FR (1) | FR792335A (en) |
GB (1) | GB424608A (en) |
Cited By (57)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2813404A (en) * | 1955-08-26 | 1957-11-19 | Worthington Corp | Refrigeration system |
DE1081424B (en) * | 1958-01-21 | 1960-05-12 | Thomas Fischer Dipl Ing | Method and device for separating liquid or solid substances from gases or liquids |
US2943698A (en) * | 1960-07-05 | Cyclone-type separator | ||
US2952330A (en) * | 1958-03-12 | 1960-09-13 | Charles A Winslow | Centrifugal-type fluid purifier |
US3339350A (en) * | 1965-05-28 | 1967-09-05 | Monsanto Co | Gas-liquid separator |
US4572727A (en) * | 1983-04-14 | 1986-02-25 | Ube Industries, Ltd. | Cyclone |
US4687492A (en) * | 1984-04-16 | 1987-08-18 | Ashland Oil, Inc. | Cyclone for lessening formation of carbonaceous deposits |
US4824449A (en) * | 1985-06-04 | 1989-04-25 | Istvan Majoros | Device for transforming a fluid flow |
US5961701A (en) * | 1997-03-24 | 1999-10-05 | Vision Almet Limited | Moisture separator for digester gases and landfill gases and raw natural gases |
US6221134B1 (en) | 1999-07-27 | 2001-04-24 | G.B.D. Corp. | Apparatus and method for separating particles from a cyclonic fluid flow |
US6228260B1 (en) | 1999-07-27 | 2001-05-08 | G. B. D. Corp. | Apparatus for separating particles from a cyclonic fluid flow |
US6228151B1 (en) | 1999-08-18 | 2001-05-08 | G.B.D. Corp. | Apparatus and method for separating particles from a cyclonic fluid flow |
US6231645B1 (en) | 1999-07-27 | 2001-05-15 | G.B.D. Corp. | Apparatus and method for separating particles from a cyclonic fluid flow utilizing a movable access member associated with a cyclonic separator |
US6251296B1 (en) | 1999-07-27 | 2001-06-26 | G.B.D. Corp. | Apparatus and method for separating particles from a cyclonic fluid flow |
US6440197B1 (en) | 1999-07-27 | 2002-08-27 | G.B.D. Corp. | Apparatus and method separating particles from a cyclonic fluid flow including an apertured particle separation member within a cyclonic flow region |
BE1017746A3 (en) * | 2007-08-29 | 2009-05-05 | Atlas Copco Airpower Nv | LIQUID SEPARATOR. |
US20090300874A1 (en) * | 2008-06-05 | 2009-12-10 | Bissell Homecare, Inc. | Cyclonic vacuum cleaner with improved collection chamber |
US9027198B2 (en) | 2013-02-27 | 2015-05-12 | G.B.D. Corp. | Surface cleaning apparatus |
US9227201B2 (en) | 2013-02-28 | 2016-01-05 | Omachron Intellectual Property Inc. | Cyclone such as for use in a surface cleaning apparatus |
US9227151B2 (en) | 2013-02-28 | 2016-01-05 | Omachron Intellectual Property Inc. | Cyclone such as for use in a surface cleaning apparatus |
US9238235B2 (en) | 2013-02-28 | 2016-01-19 | Omachron Intellectual Property Inc. | Cyclone such as for use in a surface cleaning apparatus |
US9295995B2 (en) | 2013-02-28 | 2016-03-29 | Omachron Intellectual Property Inc. | Cyclone such as for use in a surface cleaning apparatus |
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US9693666B2 (en) | 2011-03-04 | 2017-07-04 | Omachron Intellectual Property Inc. | Compact surface cleaning apparatus |
US9820621B2 (en) | 2013-02-28 | 2017-11-21 | Omachron Intellectual Property Inc. | Surface cleaning apparatus |
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US9949601B2 (en) | 2007-08-29 | 2018-04-24 | Omachron Intellectual Property Inc. | Cyclonic surface cleaning apparatus |
US10080472B2 (en) | 2010-03-12 | 2018-09-25 | Omachron Intellectual Property Inc. | Hand carriable surface cleaning apparatus |
US10136778B2 (en) | 2014-12-17 | 2018-11-27 | Omachron Intellectual Property Inc. | Surface cleaning apparatus |
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Families Citing this family (7)
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---|---|---|---|---|
DE876029C (en) * | 1941-05-13 | 1953-05-07 | Intensiv Filter Gmbh | Centrifugal dust collector |
DE921347C (en) * | 1950-05-17 | 1954-12-16 | Bernhard Telgmann | Airborne dust separator for chimneys |
DE965744C (en) * | 1950-10-26 | 1957-06-19 | Hartmann A G Maschf | Sifter with tangential feeding of the well-loaded carrier |
DE936180C (en) * | 1952-12-31 | 1955-12-07 | Alfred Knecht | Centrifugal air cleaner, especially for internal combustion engines |
DE3540259C2 (en) * | 1985-11-13 | 1995-05-11 | Truetzschler Gmbh & Co Kg | Device for separating from fiber spinning machines, in particular blow room machines and cards, extracted fiber waste and the like. Like impurities |
DE3615416A1 (en) * | 1986-05-07 | 1987-11-12 | Truetzschler & Co | DEVICE FOR CLEANING TEXTILE FIBER FLAKES |
IT1284925B1 (en) * | 1995-11-30 | 1998-05-28 | Rieter Ag Maschf | SUCTION DEVICE ON A TEXTILE MACHINE |
-
0
- BE BE406007D patent/BE406007A/xx unknown
-
1933
- 1933-08-10 FR FR792335D patent/FR792335A/en not_active Expired
-
1934
- 1934-06-19 DE DES114413D patent/DE613087C/en not_active Expired
- 1934-07-10 GB GB20240/34A patent/GB424608A/en not_active Expired
- 1934-07-26 US US737033A patent/US2015464A/en not_active Expired - Lifetime
Cited By (87)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2943698A (en) * | 1960-07-05 | Cyclone-type separator | ||
US2813404A (en) * | 1955-08-26 | 1957-11-19 | Worthington Corp | Refrigeration system |
DE1081424B (en) * | 1958-01-21 | 1960-05-12 | Thomas Fischer Dipl Ing | Method and device for separating liquid or solid substances from gases or liquids |
US2952330A (en) * | 1958-03-12 | 1960-09-13 | Charles A Winslow | Centrifugal-type fluid purifier |
US3339350A (en) * | 1965-05-28 | 1967-09-05 | Monsanto Co | Gas-liquid separator |
US4572727A (en) * | 1983-04-14 | 1986-02-25 | Ube Industries, Ltd. | Cyclone |
US4687492A (en) * | 1984-04-16 | 1987-08-18 | Ashland Oil, Inc. | Cyclone for lessening formation of carbonaceous deposits |
US4824449A (en) * | 1985-06-04 | 1989-04-25 | Istvan Majoros | Device for transforming a fluid flow |
US5961701A (en) * | 1997-03-24 | 1999-10-05 | Vision Almet Limited | Moisture separator for digester gases and landfill gases and raw natural gases |
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Also Published As
Publication number | Publication date |
---|---|
BE406007A (en) | |
GB424608A (en) | 1935-02-25 |
FR792335A (en) | 1935-12-28 |
DE613087C (en) | 1935-05-11 |
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