WO2003026800A2 - Flotation machine rotor and method of operation - Google Patents
Flotation machine rotor and method of operation Download PDFInfo
- Publication number
- WO2003026800A2 WO2003026800A2 PCT/US2002/029764 US0229764W WO03026800A2 WO 2003026800 A2 WO2003026800 A2 WO 2003026800A2 US 0229764 W US0229764 W US 0229764W WO 03026800 A2 WO03026800 A2 WO 03026800A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- rotor
- flotation machine
- body portion
- aperture
- peripheral edge
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/16—Flotation machines with impellers; Subaeration machines
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/234—Surface aerating
- B01F23/2342—Surface aerating with stirrers near to the liquid surface, e.g. partially immersed, for spraying the liquid in the gas or for sucking gas into the liquid, e.g. using stirrers rotating around a horizontal axis or using centrifugal force
- B01F23/23421—Surface aerating with stirrers near to the liquid surface, e.g. partially immersed, for spraying the liquid in the gas or for sucking gas into the liquid, e.g. using stirrers rotating around a horizontal axis or using centrifugal force the stirrers rotating about a vertical axis
- B01F23/234211—Stirrers thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1493—Flotation machines with means for establishing a specified flow pattern
Definitions
- Flotation machines are commonly employed to separate solid material from a slurry typically composed of liquids and solids in varying proportions.
- An impeller located in the flotation machine agitates the slurry dispersing entrapped gas, thereby causing the formation of gas bubbles.
- Particulate solid material adheres to the surface of the gas bubbles and rises therewith to the slurry surface forming a froth that has a higher concentration of adhered solid material, than does the slurry.
- the froth which is a combination of liquid, solid particles, and gas is removed from the flotation machine for further processing.
- the gas bubble /particle interaction is important to the flotation process as, without it, there can be no separation via the above-described method.
- gas is usually introduced through an opening in the impeller or rotor of the flotation machine.
- a prior art method of introducing the gas is shown in FIGS. 1, 2, and 3.
- Gas is introduced through apertures 12 in the rotor. These apertures tend to be large and located between successive pairs of rotor blades 14.
- the apertures 12 extend, in part through an upper surface 16 of the rotor 10, with the remainder of each aperture extending into a body portion 18 of the rotor.
- each aperture 12 follows the smooth contours of the rotor body portion 18.
- a problem associated with rotors configured in the above-described manner is that there is a tendency for solid particles, to enter the rotor body portion 18, through the apertures 12.
- Another problem attributed to these prior art rotors is that the distribution of gas bubbles attributable to the air entering through an aperture is not optimal due to the apertures configuration. This in turn minimizes the gas bubble /particle interaction and thereby the solid /liquid separation.
- the present invention resides in one aspect to a flotation machine rotor that includes a body portion which defines an interior area and is adapted to communicate with a gas source. At least one rotor blade projects radially outwardly from the body portion with at least one aperture being defined by the body portion.
- the aperture is in gaseous communication with the interior area and is adjacent the at least one rotor blade. During operation, gas flowing from the gas source is expelled through the aperture causing bubbles to be generated in a liquid /solid slurry in which the flotation machine rotor is immersed.
- the aperture is defined at least in-part by a lower peripheral edge. At least one lip projects outwardly from the lower peripheral edge.
- solid particles forming part of the liquid solid slurry travel upwardly along the body portion and encounter the lip.
- the solid particles are then projected away from the body portion and into approximate alignment with the aperture.
- the gas bubbles generated by gas being expelled from the aperture entrain the solid particles thereby forming a froth of gas bubbles and entrapped particles on the slurry surface which is then skimmed off, clarifying the slurry.
- the aperture is in the form of a slot and extends in a longitudinal direction approximately perpendicular to a central axis defined by the rotor.
- the body portion can be contoured with a diameter defined thereby progressively increasing from a lower to an upper section of the body portion. The slots are positioned in the upper section of the body portion.
- the present invention resides in another aspect in a method for operating a flotation machine rotor of the above-described type wherein a liquid/ solid slurry is introduce into a flotation machine and the rotor is caused to spin about the central axis so that the solid particles forming part of the slurry move upwardly along the body portion and contact the lips associated with the apertures in the body portion. At least a portion of the solid particles are projected radially away from the rotor by the lip and become approximately aligned with the associated aperture. Gas from the gas source is caused to flow from the aperture thereby forming bubbles in the slurry that define a surface upon which a portion of the solid particles projected from the lip contact and are entrain thereon. These bubbles and entrained solids cause a froth to form on the surface of the liquid solid slurry which can then be removed from the flotation machine.
- FIG. 1 is a perspective view of a prior art flotation machine rotor.
- FIG. 2 is a partial, top view of the rotor of FIG. 1.
- FIG. 3 is a partial, cross-sectional view of the rotor of FIG. 1.
- FIG. 4 is a perspective view of a flotation machine rotor embodying the present invention.
- FIG. 5 is a top plan view of the rotor of FIG. 4.
- FIG. 6 is a partial, cross-sectional view of the rotor of FIG. 4.
- FIG. 7 is a partial, cross-sectional view of the rotor of FIG. 4.
- FIG. 8 is an enlarged view of a portion of the rotor of FIG. 7.
- FIG. 9 is a partial plan view and side elevational view of an alternate embodiment of the present invention.
- a flotation machine rotor embodying the present invention and generally designated by the reference number 40 includes a plurality of rotor blades 42, each extending radially from a rotor body portion 44.
- the rotor body portion 44 defines a plurality of approximately horizontal slots 46 extending therethrough part-way between an upper and lower portion of the rotor 40.
- Each slot is defined in part by an upper and a lower peripheral edge, 43 and 45 respectively.
- the upper peripheral edge of each slot 46 being closer to an upper surface 47 of the rotor 40.
- the terms upper, lower, horizontal, vertical, and the like are intended to apply only to the particular orientation of the rotor as shown in the figures. Since other rotor orientations are possible, these terms should be broadly construed, and not interpreted in a limiting sense.
- the slots 46 each open into an interior area 48 defined by the rotor 40, and as will be explained in detail below are used to supply gas, usually air, into the rotor and thereby into the slurry introduced therein.
- the rotor defines an opening 49 in gaseous communication with the interior area 48.
- the rotor body portion 44 includes a plurality of lips 50 each projecting radially outward from a lower peripheral edge 52 defined by each slot 46. The lips each cause a break in the otherwise smooth contour defined by the rotor body portion.
- a suitable drive such as, but not limited to a motor.
- a liquid/ solid particle slurry is introduced into the housing and the rotation of the rotor 40 causes the solid particles entrained in the slurry to travel up the rotor body portion 44 over the lip 50 which acts to project the particles away for the rotor where gas flowing through each slot 46 causes the formation of air bubbles 52 that contact and entrain the solid particles.
- the rotor 40 in order to introduce gas bubbles into the slurry is coupled to a gas source that is in gaseous communication with the aperture 49 and thereby the interior area 48, see Fig. 5.
- the gas bubbles having the particles entrained thereon are shown in the illustrated embodiment as element 54. These gas bubbles having solid particles entrained thereon are carried to a point where they can be removed from the flotation machine.
- An advantage of the present invention is that the lips 50 will aid in the prevention of particles entering the interior of the rotor as well as in placing the particles in the gas stream flowing from the slots 46.
- the slots provide large gas bubble /particle contact areas.
- the combination of the slots and lips can cause a venturi-like effect pulling greater quantities of gas through the slots. While approximately horizontal slots have been shown and described, the present invention is not limited in this regard as other orientations such as, but not limited to vertical slots can be substituted without departing from the broader aspects of the present invention.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biotechnology (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Crushing And Pulverization Processes (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2461279A CA2461279C (en) | 2001-09-21 | 2002-09-19 | Flotation machine rotor and method of operation |
AU2002326989A AU2002326989B2 (en) | 2001-09-21 | 2002-09-19 | Flotation machine rotor and method of operation |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US32403101P | 2001-09-21 | 2001-09-21 | |
US60/324,031 | 2001-09-21 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2003026800A2 true WO2003026800A2 (en) | 2003-04-03 |
WO2003026800A3 WO2003026800A3 (en) | 2004-02-26 |
Family
ID=23261771
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2002/029764 WO2003026800A2 (en) | 2001-09-21 | 2002-09-19 | Flotation machine rotor and method of operation |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU2002326989B2 (en) |
CA (1) | CA2461279C (en) |
WO (1) | WO2003026800A2 (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4800017A (en) * | 1987-04-16 | 1989-01-24 | Dorr-Oliver Incorporated | Flotation mechanism |
WO1997006892A1 (en) * | 1995-08-17 | 1997-02-27 | Svedala Limited | Flotation tank impeller |
-
2002
- 2002-09-19 WO PCT/US2002/029764 patent/WO2003026800A2/en not_active Application Discontinuation
- 2002-09-19 AU AU2002326989A patent/AU2002326989B2/en not_active Ceased
- 2002-09-19 CA CA2461279A patent/CA2461279C/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4800017A (en) * | 1987-04-16 | 1989-01-24 | Dorr-Oliver Incorporated | Flotation mechanism |
WO1997006892A1 (en) * | 1995-08-17 | 1997-02-27 | Svedala Limited | Flotation tank impeller |
Also Published As
Publication number | Publication date |
---|---|
CA2461279A1 (en) | 2003-04-03 |
AU2002326989B2 (en) | 2006-06-22 |
WO2003026800A3 (en) | 2004-02-26 |
CA2461279C (en) | 2011-01-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6805243B1 (en) | Flotation machine rotor and method of operation | |
CA1337774C (en) | Flotation machine | |
EP0272107B1 (en) | Aeration apparatus | |
US3993563A (en) | Gas ingestion and mixing device | |
US2243309A (en) | Flotation apparatus | |
CA1066437A (en) | Flotation cell | |
JPH0483545A (en) | Granular material classifier | |
US3409130A (en) | Flotation apparatus | |
US20040084354A1 (en) | Flotation machine | |
CA2461279C (en) | Flotation machine rotor and method of operation | |
US4940534A (en) | Froth flotation column | |
US7980824B2 (en) | Rotor for a flotation machine | |
US6413366B1 (en) | Method and device for flotation of pollutants from an aqueous fibrous material suspension | |
AU2002326989A1 (en) | Flotation machine rotor and method of operation | |
ZA200401922B (en) | Flotation machine rotor and method of operation | |
JPH11514925A (en) | Complete reactor for liquid purification | |
US5591327A (en) | Flotation equipment | |
JP3142880B2 (en) | Reactor baffle for liquid purification | |
JP7021553B2 (en) | Coolant tank | |
JP6992953B2 (en) | Raw seaweed foreign matter separation device (raw seaweed foreign matter separation and removal device) co-rotation prevention device for raw seaweed (including raw seaweed lumps, foreign matter, foreign matter lumps) and co-rotation prevention method | |
US2969879A (en) | Liquid and gas mixing machine | |
JPH0711597A (en) | Paper-making screen | |
SU1438841A1 (en) | Flotation machine | |
US6276936B1 (en) | Dental separator for solids from a solids/liquid mixture | |
RU2213624C1 (en) | Flotation machine for coarse particle flotation |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A2 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BY BZ CA CH CN CO CR CU CZ DE DM DZ EC EE ES FI GB GD GE GH HR HU ID IL IN IS JP KE KG KP KR LC LK LR LS LT LU LV MA MD MG MN MW MX MZ NO NZ OM PH PL PT RU SD SE SG SI SK SL TJ TM TN TR TZ UA UG UZ VN YU ZA ZM |
|
AL | Designated countries for regional patents |
Kind code of ref document: A2 Designated state(s): GH GM KE LS MW MZ SD SL SZ UG ZM ZW AM AZ BY KG KZ RU TJ TM AT BE BG CH CY CZ DK EE ES FI FR GB GR IE IT LU MC PT SE SK TR BF BJ CF CG CI GA GN GQ GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2002326989 Country of ref document: AU |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2461279 Country of ref document: CA |
|
122 | Ep: pct application non-entry in european phase | ||
NENP | Non-entry into the national phase |
Ref country code: JP |
|
WWW | Wipo information: withdrawn in national office |
Country of ref document: JP |