CA1210167A - Column froth flotation - Google Patents
Column froth flotationInfo
- Publication number
- CA1210167A CA1210167A CA000455766A CA455766A CA1210167A CA 1210167 A CA1210167 A CA 1210167A CA 000455766 A CA000455766 A CA 000455766A CA 455766 A CA455766 A CA 455766A CA 1210167 A CA1210167 A CA 1210167A
- Authority
- CA
- Canada
- Prior art keywords
- column
- pulp
- flow passages
- plates
- particles
- 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
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
- B03D1/02—Froth-flotation processes
-
- 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
- B03D1/08—Subsequent treatment of concentrated product
- B03D1/082—Subsequent treatment of concentrated product of the froth product, e.g. washing
-
- 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
- B03D1/1481—Flotation machines with a plurality of parallel plates
-
- 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
- B03D1/24—Pneumatic
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biotechnology (AREA)
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Paper (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
The froth flotation device includes a flotation column partially filled with a packing which defines a large number of small flow passages extending in a circuitous pattern between the upper and lower portions of the column. A conditioned aqueous pulp of a mineral ore, such as iron ore. is introduced into the midzone of the column. A
pressurized inert gas, such as air, is introduced into the bottom of the column and is forced upwardly through the flow passages in the packing. As the air flows upwardly through these flow passages, it is broken into fine bubbles which intimately contact the floatable particles (e.g., iron oxide) in the aqueous pulp and forms a froth concentrate or float fraction which overflows from the top of the column. Wash water is introduced into the top of the column and flows through the flow passages in the packing countercurrently to the float fraction to scrub entrained non-floatable particles (e.g., gangue) from the froth concentrate. A tailing fraction containing the non-floatable particles is withdrawn from the bottom of the column.
The froth flotation device includes a flotation column partially filled with a packing which defines a large number of small flow passages extending in a circuitous pattern between the upper and lower portions of the column. A conditioned aqueous pulp of a mineral ore, such as iron ore. is introduced into the midzone of the column. A
pressurized inert gas, such as air, is introduced into the bottom of the column and is forced upwardly through the flow passages in the packing. As the air flows upwardly through these flow passages, it is broken into fine bubbles which intimately contact the floatable particles (e.g., iron oxide) in the aqueous pulp and forms a froth concentrate or float fraction which overflows from the top of the column. Wash water is introduced into the top of the column and flows through the flow passages in the packing countercurrently to the float fraction to scrub entrained non-floatable particles (e.g., gangue) from the froth concentrate. A tailing fraction containing the non-floatable particles is withdrawn from the bottom of the column.
Description
COLUMN FROTH FLOTATION
BACKGROUND OF THE INVENTION
This invention relates to froth flotation and, more particularl~, to column froth flotation for beneficiating mineral ores and the like.
Froth flotation has been used to beneficiate a variety of mineral o~es and to effect separation of various other materials for many years. Froth flotation involve~ the separation of particles from each other in a liquid pulp based on differences in hydrophobicity. The pulp is aerated by introducing a plurality of minute air bubble~ into it. The air bubble~ tend to attach to the floatable (hydrophobic) particles and cause those particles ~o rise to the surface as a froth product which overflows from the flotation device, leaving behind the non-floatable thydrophilic) par~icles.
An article entitled "Flotation Machines" in Mininq Maqazine, January, 1982, page 35, describes several different types of flotation devices and proces~es u~ed for benefieiating minerals. In so-called column flotation, a conditioned pulp i8 introduced into the midzone of a rela~ively tall column, pressurized air is introduced through a diffuser in the bottom of the column, and wash water is fed into the top of ~he column.
fraction containing the floatable pa~ticles, usually the mineral values, overflows from the top of the column and a fraction containing the non-floatable particles, usually the gangue, is discharged from the bottom of the column by gravity or a pump. Examples of p~ior column flotation devices and processes are described in Canadian Patents 680,576 and 694,547, Canadian Chemical Processinq. February, 1965, pages 55-58, and E & MW, Volumn 66 No. 1, pages 76-78, 83.
Tha air diffusers in flotation columns have a tendency to become plugged, particularly when a lime depressant is used. causing an uneven distribution of air throughout the pulp. Also, the small air bubbles generated at the bottom of the column tend to enlarge as they rise toward the top due to a change in static pressure within the column, resulting in a reduced surface contact between the air and particles. SeveIal differen~ approaches have been used to alleviate this problem, including the u~e of hydrophobic materials and, instead of using a diffuser, introducing the air as a fine `dispersion in water. The latter approach is disclosed in U.S.
Patent 3,371,779.
SUMMARY OF T~E INVENTION
An ob9ect of the invention is ~o provide a simple, economical froth flotation device and process capable of separating floatable particles from an aqueous pulp of a mixture of floatable and non-floatable particles with a minimum number of flotation stages.
Another object o~ the inven~ion i8 to provide a f~oth flotation device and process which produces increased air-to-particle contact.
A further object of the invention is to provide a froth flotation device and process which reguires mi~imal amounts of water and energy.
A still further object of the inv~ntion is to provide a froth flotation column which does not require an air diffuser having a tendency to become plugged during operation.
~ . .
Other objects, aspects and advantages of the invention will become apparent to those skilled in art upon reviewing the following detailed description, the drawing and the appended claims.
The invention provide6 a froth flotation dsvice including a tubular flotation column, packing means disposed in the column defining a large number of small flow passages extending in a circuitous pattern between the upper and lower portions o~ the column, pulp feed means for introducing an aqueous pulp into the column a~ an intermediate location for flow through the flow passages, means for introducing wash water into the upper portion of the column for downward flow through the flow passages, means for introducing a pressurized inert gas into the lower portion of the column for upward flow throu~h the flow passages0 means for discharging a froth fraction containing floated particles of the aqueous pulp from the upper portion o~ the co}umn, and means for discharging a tailing fraction containing unfloated particles of the agueous pulp from the lower portion of the column.
An aqueous pulp containing a mixtuLe of floatable and non-floatable particles is introduced into a column. The iner~ gas, preferably air, is broken into fine bubbles as it is forced upwardly through the flow passages in the packing. These bubbles intimately contact the floatable particles and form a froth concentrate or float fraction which contains the floatable particle~ and ovsrflows from the top portion of the column. The wash water, flowing through the flow pa~sages in the packing Gountercurren~ly to the float fraction, removes entrained non-floatable particles from the float .
~2~67 fraction and a tailing fraction containing the non-floatable particles is withdrawn from the bottom of the column.
In one embodiment, ~he packing comprises a plurality of vertically spaced plates and spacer means for laterally spacing the plates apact to define a plurality of small ~low passages between adjacent plates. The spacer means can comprise rows of corrugations on each of the plates, preferably extending diagonally relative ~o the horizontal.
In one embodimen~, separate, vertically adjacent sections of the plates are provided. These sections preferably are oriented so that the vertical planes of the plates in one ~ec~ion are angularly related ~o the ~ertical planes of She plates in the adjacent section.
BRIEF DESCRIPTION OF THE DRAWINGS
Fig. l is a schematic represen~ation o~
a froth flotation column embodying the invention.
Fig. 2 is an exploded, perspective view of a portion of the corrugated plates making up one section of packing for the column illustrated in Fig.
1.
DESCRIPTION OF THE PREFERRED EMBODIMENT
The column flotation device and process of the invention can be used to separate a wide variety of materials in a broad range of particle sizes. It is particularly adapta~le for separation of mineral values from the ganyue i~ fine-grained ores, such as low-grade, oxidized taconite ores from the Lake Superior area. T~e invention will be described in connectior, with that applicatisn.
~2~
The flotation device 10 provided by the invention includes a tubular column 12 having an upper portion 14 and a lower portiop 160 a pulp inlet 18 for introducing a conditioned aqueous slurry or pulp of an oxidized taconite ore into the column at an intermediate location. a water inlet 20 for introducing wash water into the upper portion of the column 12, and a gas inlet 22 for introduGing a pressurized gas, such as air, into ~he lower portion 16 of the column 12.
The column 12 can be generally upright or vertical as illustrated in Fig. 1 or inclined at angle to the vertical. The column 12 is partially filled with a packing 24 which defines a large number of small flow passages extending in a circuitous or tortuous pattern between the upper and lower portions 14 and 16. Wash water introduced into the upper portion 14 of the column 12 through the water inlet 20 flows downwardly through these flow passages.
Pressurized air introduced into the lower portion ?6 of the column 12 through the gas inlet 22 is forced upwardly through these flow passages, countercurrently to the wash water and the portion of the aqueous pulp descending through these flow passages.
A~ ~he air passes upwardly through these flow passages, it is broken into fine bubbles of relatively,uniform size, These rising bubbles intimately contact the particl2s of the aqueous pulp in the flow pa6sages of the packing 24 to produce a froth concentrat0 or float fraction containing primarily the floatable particles and a minor amount of essen~ially non-floatable particles entrained in the froth. The air bubbles cacry the froth concentrate 25 upwardly into a froth compartment 26 ~o~
in the upper portion of the column 12. The froth concentrate 25 is discharged from the froth chamber 26 by overflowing therefrom through an outlet 28.
Wash water descending through the flow passages in the packing 24 induces entrained non-floatable particles to separate ~rom the froth concentrate and drop by gravity (i.e.. sink) through these flow passages. While the wash water can be introduced into the column 12 in any convenient manner, it preferably is introduced into the froth chamber 26 and above the top surface of the froth concentrate 26 through a spray nozzle 32 centrally disposed in the top of the column 12. The spray nozzle 32 distributes multiple streams of wa~e{ over the froth in the froth chamber 26, thereby insuring a more uniform contact of the wash water with non-floatable particles in the froth concentrate 25 and also a more uniform distribution of the wash water through the flow passage~ in the packing Z4.
A tailing fraction 33 containing the non-floatable particles in the agueous pulp collects in a tailing chamber 32 at the bottom of the column 12 and is discharged therefrom through an outlet 34.
Although not particularly critical, the tailing chambar 32 preferably is conically shaped as illustrated in Fig. 1 to promote discharge of the tailing fraction. The tailing fraction preferably is withdrawn through the outlet 34 by a conventional variable flow pump 36.
While the colu~n 12 can have various cross-sectional con~iguratio~s, in the specific construction illus~rated. it has a square cross section. The cro s sectional dimensions and length of the column 12 are governed by the type of aqueous ~.2~0~
pulp being treated, the particular type of packing used, the desired throughput, and other variables familiar to those skilled in the art.
The packing 24 can be in a variety of S different forms capable of providing a substantially plugged flow condition and defining a large number of flow passages extending in a circuitous or tortuous pattern between the upper and lower portions of the column 12. These flow passages cause the air bubbles to break up and combine into fine bubble6 of relatively uniform size, thereby maximizlng intimate surface area contact with the floatable particles.
Sui~able packiny includes con~entional packing materials used in ~acked tower for vapor-liquid trans~er operations, such as Raschig rings, Berl saddles, partition rings, and the like.
In the preferred embodiment illustrated, the packing 24 consists of a plurality of sections 38a-38f of ve~tical extending plates 40.
Each section includes a plurality of the plates ~O
and spacer means for laterally spacing the plates 40 apar~ to define a plurality of relatively small flow passages between adjacent plates 40. In the specific construction illustrated, such spacer means comprises uniformly spaced rows of corLugations 42 on each plate 40. The corrugations 42 preferably extend diagonally, e.g., at an angle of approximately 45 to the hoLizontal, to eliminate vertical flow passages of subsSantial length. The angular orienSation of She coIrugations can be varied to control flow through the flow passage. For instance, this flow can be increased by increasing the angle of the corrugations 42 to the horizontal.
In order to further enhance the circuitou~ or toLtuous pattern of the flow passages defined between adjacent plates 40, the corrugations 42 of alternate plates 40 preferably extend in the opposite direction as illustrated in Fig. 2. That is, the corrugations on one plate extend at an angle to the corrugations on the next plate. Also, alternate sections are positioned so that the ver~ical planes of the plates in one section are angularly related (e.g., at about 9O) to the vertical planes of the plates in the adjacent section. Referring to Fig. 1, the vertical planes of the plate~ 40 in sections 38a, 38c, and 38e extend perpendicularly to the plane of the page and the vertical planes of the plates in sections 38b, 3~d and 38~ extend parallel to the plane of the page.
~ he packing ~ections 38c and 38d in the vicinity of the pulp inlet 38 preferably are spaced apart to provide a substantially unobstructed feed compartment OL chamber 44. The packing sections 38a, 38b, and 38c above the feed chamber 44 make up the primary cleaning section of the column 12 and ~he packing sections 38d, 38e and 38f below the feed chamber 44 make up a scavenging section wheLein the floatable particles are separated from the descending tailings.
In a typical operation, an iron ore, such as oxidized taconite~ is comminuted into a particle size suitable ~or liberation of the mineral values and for froth flotation. An aqueous slurry or pulp of the particles i8 intloduced into a stirred conditioning ve6~el 46 for the addition and admixing of suitable flo~ation reagents. If silica or gangue is to be floated (reverse flotation), a cationic ~.2~ 7 _9_ collector or an anionic collec~or (for calcium activated silica) is added to and mixed with the aqueous pulp in the conditioning vessel 4&. If iron oxide is ~o be floated, a suitable anionic collector, such as a fatty acid type collector, is added to and thoroug~ly mixed with the aqueous pulp in the conditioning vessel 46.
~ arious suitable conditioning reagents can be used depending primarily on the material being treated and the type of flota~ion. The conditioning reagent disclosed in U.S. Patent ~,132,535, is particularly effective for iron ore6 ~hen ~n anionic collect~r is used. That conditioning reaqe~t is formed by mixing a polyvalent metal salt with an alkali ~etal silicate. The conditioning reagen.~ is usually added to and thoroughly mixed with ~he pulp pr;or to the addition of the collector. After the collector has been added to the conditioning ~essel 46, the pulp is mixed for a suffic;ent time to lnsure uniform dispersi~n of the collector throughout the pulp . ~
In some cases, it may be necessary to add a small amount of fuel oil and/or a conventional frothing agant to the pulp. When used, the fro~hing agent can be incorporated into the pulp before, after, or togethec with the collector. If the frothing agent is added separa~ely, the pulp is mixed for a sufficient time to insure uniform dispersion of the frothing agent throughout the pulp.
Following conditioning, the pulp is withdrawn ~rom the conditioning vessel 46 by a pump 4~ and introduced into the column through the pulp inlet 18.
~`
~2~
The flow rates of the ore pulp, the air and the wash water can be adjusted to ob~ain a material balance which provides the most effective separation of the floatable particles (e.g., iron oxide) from the non-floatable particles (e.g., gangue).
The device and proces6 of the invention have several advantages over conventional flotation devices and processes. They provide all the advantages of conventional flotation columnc and further provide increased air-to-particle contact, eliminate the need for a pecial device in the bottom of the column for generating fine air bubbles, and require less water and energy. More importantly, floatable particles, such as iron oxide, can be more effectively separated from non-floatable particles, such as yangue, with single stage flo~ation. That is, a conventional Plotation column usually requires at least two flotation stages to recover the same amount of iron oxide from a low grade iron ore.
In addition ~o being used for single stage flotation, the device of ~he in~ention can be used in combination with conven~ional flotation machines and two or more can be used in series.
The following examples are presented to illustrate the invention and are not ~o be construed as limitations thereof.
EXAMPLE l A series of laboratory tests were run on an experimental column consisSing of a 2-inch I.D.
tube, 8 feet long and almost entirel~ packed with
BACKGROUND OF THE INVENTION
This invention relates to froth flotation and, more particularl~, to column froth flotation for beneficiating mineral ores and the like.
Froth flotation has been used to beneficiate a variety of mineral o~es and to effect separation of various other materials for many years. Froth flotation involve~ the separation of particles from each other in a liquid pulp based on differences in hydrophobicity. The pulp is aerated by introducing a plurality of minute air bubble~ into it. The air bubble~ tend to attach to the floatable (hydrophobic) particles and cause those particles ~o rise to the surface as a froth product which overflows from the flotation device, leaving behind the non-floatable thydrophilic) par~icles.
An article entitled "Flotation Machines" in Mininq Maqazine, January, 1982, page 35, describes several different types of flotation devices and proces~es u~ed for benefieiating minerals. In so-called column flotation, a conditioned pulp i8 introduced into the midzone of a rela~ively tall column, pressurized air is introduced through a diffuser in the bottom of the column, and wash water is fed into the top of ~he column.
fraction containing the floatable pa~ticles, usually the mineral values, overflows from the top of the column and a fraction containing the non-floatable particles, usually the gangue, is discharged from the bottom of the column by gravity or a pump. Examples of p~ior column flotation devices and processes are described in Canadian Patents 680,576 and 694,547, Canadian Chemical Processinq. February, 1965, pages 55-58, and E & MW, Volumn 66 No. 1, pages 76-78, 83.
Tha air diffusers in flotation columns have a tendency to become plugged, particularly when a lime depressant is used. causing an uneven distribution of air throughout the pulp. Also, the small air bubbles generated at the bottom of the column tend to enlarge as they rise toward the top due to a change in static pressure within the column, resulting in a reduced surface contact between the air and particles. SeveIal differen~ approaches have been used to alleviate this problem, including the u~e of hydrophobic materials and, instead of using a diffuser, introducing the air as a fine `dispersion in water. The latter approach is disclosed in U.S.
Patent 3,371,779.
SUMMARY OF T~E INVENTION
An ob9ect of the invention is ~o provide a simple, economical froth flotation device and process capable of separating floatable particles from an aqueous pulp of a mixture of floatable and non-floatable particles with a minimum number of flotation stages.
Another object o~ the inven~ion i8 to provide a f~oth flotation device and process which produces increased air-to-particle contact.
A further object of the invention is to provide a froth flotation device and process which reguires mi~imal amounts of water and energy.
A still further object of the inv~ntion is to provide a froth flotation column which does not require an air diffuser having a tendency to become plugged during operation.
~ . .
Other objects, aspects and advantages of the invention will become apparent to those skilled in art upon reviewing the following detailed description, the drawing and the appended claims.
The invention provide6 a froth flotation dsvice including a tubular flotation column, packing means disposed in the column defining a large number of small flow passages extending in a circuitous pattern between the upper and lower portions o~ the column, pulp feed means for introducing an aqueous pulp into the column a~ an intermediate location for flow through the flow passages, means for introducing wash water into the upper portion of the column for downward flow through the flow passages, means for introducing a pressurized inert gas into the lower portion of the column for upward flow throu~h the flow passages0 means for discharging a froth fraction containing floated particles of the aqueous pulp from the upper portion o~ the co}umn, and means for discharging a tailing fraction containing unfloated particles of the agueous pulp from the lower portion of the column.
An aqueous pulp containing a mixtuLe of floatable and non-floatable particles is introduced into a column. The iner~ gas, preferably air, is broken into fine bubbles as it is forced upwardly through the flow passages in the packing. These bubbles intimately contact the floatable particles and form a froth concentrate or float fraction which contains the floatable particle~ and ovsrflows from the top portion of the column. The wash water, flowing through the flow pa~sages in the packing Gountercurren~ly to the float fraction, removes entrained non-floatable particles from the float .
~2~67 fraction and a tailing fraction containing the non-floatable particles is withdrawn from the bottom of the column.
In one embodiment, ~he packing comprises a plurality of vertically spaced plates and spacer means for laterally spacing the plates apact to define a plurality of small ~low passages between adjacent plates. The spacer means can comprise rows of corrugations on each of the plates, preferably extending diagonally relative ~o the horizontal.
In one embodimen~, separate, vertically adjacent sections of the plates are provided. These sections preferably are oriented so that the vertical planes of the plates in one ~ec~ion are angularly related ~o the ~ertical planes of She plates in the adjacent section.
BRIEF DESCRIPTION OF THE DRAWINGS
Fig. l is a schematic represen~ation o~
a froth flotation column embodying the invention.
Fig. 2 is an exploded, perspective view of a portion of the corrugated plates making up one section of packing for the column illustrated in Fig.
1.
DESCRIPTION OF THE PREFERRED EMBODIMENT
The column flotation device and process of the invention can be used to separate a wide variety of materials in a broad range of particle sizes. It is particularly adapta~le for separation of mineral values from the ganyue i~ fine-grained ores, such as low-grade, oxidized taconite ores from the Lake Superior area. T~e invention will be described in connectior, with that applicatisn.
~2~
The flotation device 10 provided by the invention includes a tubular column 12 having an upper portion 14 and a lower portiop 160 a pulp inlet 18 for introducing a conditioned aqueous slurry or pulp of an oxidized taconite ore into the column at an intermediate location. a water inlet 20 for introducing wash water into the upper portion of the column 12, and a gas inlet 22 for introduGing a pressurized gas, such as air, into ~he lower portion 16 of the column 12.
The column 12 can be generally upright or vertical as illustrated in Fig. 1 or inclined at angle to the vertical. The column 12 is partially filled with a packing 24 which defines a large number of small flow passages extending in a circuitous or tortuous pattern between the upper and lower portions 14 and 16. Wash water introduced into the upper portion 14 of the column 12 through the water inlet 20 flows downwardly through these flow passages.
Pressurized air introduced into the lower portion ?6 of the column 12 through the gas inlet 22 is forced upwardly through these flow passages, countercurrently to the wash water and the portion of the aqueous pulp descending through these flow passages.
A~ ~he air passes upwardly through these flow passages, it is broken into fine bubbles of relatively,uniform size, These rising bubbles intimately contact the particl2s of the aqueous pulp in the flow pa6sages of the packing 24 to produce a froth concentrat0 or float fraction containing primarily the floatable particles and a minor amount of essen~ially non-floatable particles entrained in the froth. The air bubbles cacry the froth concentrate 25 upwardly into a froth compartment 26 ~o~
in the upper portion of the column 12. The froth concentrate 25 is discharged from the froth chamber 26 by overflowing therefrom through an outlet 28.
Wash water descending through the flow passages in the packing 24 induces entrained non-floatable particles to separate ~rom the froth concentrate and drop by gravity (i.e.. sink) through these flow passages. While the wash water can be introduced into the column 12 in any convenient manner, it preferably is introduced into the froth chamber 26 and above the top surface of the froth concentrate 26 through a spray nozzle 32 centrally disposed in the top of the column 12. The spray nozzle 32 distributes multiple streams of wa~e{ over the froth in the froth chamber 26, thereby insuring a more uniform contact of the wash water with non-floatable particles in the froth concentrate 25 and also a more uniform distribution of the wash water through the flow passage~ in the packing Z4.
A tailing fraction 33 containing the non-floatable particles in the agueous pulp collects in a tailing chamber 32 at the bottom of the column 12 and is discharged therefrom through an outlet 34.
Although not particularly critical, the tailing chambar 32 preferably is conically shaped as illustrated in Fig. 1 to promote discharge of the tailing fraction. The tailing fraction preferably is withdrawn through the outlet 34 by a conventional variable flow pump 36.
While the colu~n 12 can have various cross-sectional con~iguratio~s, in the specific construction illus~rated. it has a square cross section. The cro s sectional dimensions and length of the column 12 are governed by the type of aqueous ~.2~0~
pulp being treated, the particular type of packing used, the desired throughput, and other variables familiar to those skilled in the art.
The packing 24 can be in a variety of S different forms capable of providing a substantially plugged flow condition and defining a large number of flow passages extending in a circuitous or tortuous pattern between the upper and lower portions of the column 12. These flow passages cause the air bubbles to break up and combine into fine bubble6 of relatively uniform size, thereby maximizlng intimate surface area contact with the floatable particles.
Sui~able packiny includes con~entional packing materials used in ~acked tower for vapor-liquid trans~er operations, such as Raschig rings, Berl saddles, partition rings, and the like.
In the preferred embodiment illustrated, the packing 24 consists of a plurality of sections 38a-38f of ve~tical extending plates 40.
Each section includes a plurality of the plates ~O
and spacer means for laterally spacing the plates 40 apar~ to define a plurality of relatively small flow passages between adjacent plates 40. In the specific construction illustrated, such spacer means comprises uniformly spaced rows of corLugations 42 on each plate 40. The corrugations 42 preferably extend diagonally, e.g., at an angle of approximately 45 to the hoLizontal, to eliminate vertical flow passages of subsSantial length. The angular orienSation of She coIrugations can be varied to control flow through the flow passage. For instance, this flow can be increased by increasing the angle of the corrugations 42 to the horizontal.
In order to further enhance the circuitou~ or toLtuous pattern of the flow passages defined between adjacent plates 40, the corrugations 42 of alternate plates 40 preferably extend in the opposite direction as illustrated in Fig. 2. That is, the corrugations on one plate extend at an angle to the corrugations on the next plate. Also, alternate sections are positioned so that the ver~ical planes of the plates in one section are angularly related (e.g., at about 9O) to the vertical planes of the plates in the adjacent section. Referring to Fig. 1, the vertical planes of the plate~ 40 in sections 38a, 38c, and 38e extend perpendicularly to the plane of the page and the vertical planes of the plates in sections 38b, 3~d and 38~ extend parallel to the plane of the page.
~ he packing ~ections 38c and 38d in the vicinity of the pulp inlet 38 preferably are spaced apart to provide a substantially unobstructed feed compartment OL chamber 44. The packing sections 38a, 38b, and 38c above the feed chamber 44 make up the primary cleaning section of the column 12 and ~he packing sections 38d, 38e and 38f below the feed chamber 44 make up a scavenging section wheLein the floatable particles are separated from the descending tailings.
In a typical operation, an iron ore, such as oxidized taconite~ is comminuted into a particle size suitable ~or liberation of the mineral values and for froth flotation. An aqueous slurry or pulp of the particles i8 intloduced into a stirred conditioning ve6~el 46 for the addition and admixing of suitable flo~ation reagents. If silica or gangue is to be floated (reverse flotation), a cationic ~.2~ 7 _9_ collector or an anionic collec~or (for calcium activated silica) is added to and mixed with the aqueous pulp in the conditioning vessel 4&. If iron oxide is ~o be floated, a suitable anionic collector, such as a fatty acid type collector, is added to and thoroug~ly mixed with the aqueous pulp in the conditioning vessel 46.
~ arious suitable conditioning reagents can be used depending primarily on the material being treated and the type of flota~ion. The conditioning reagent disclosed in U.S. Patent ~,132,535, is particularly effective for iron ore6 ~hen ~n anionic collect~r is used. That conditioning reaqe~t is formed by mixing a polyvalent metal salt with an alkali ~etal silicate. The conditioning reagen.~ is usually added to and thoroughly mixed with ~he pulp pr;or to the addition of the collector. After the collector has been added to the conditioning ~essel 46, the pulp is mixed for a suffic;ent time to lnsure uniform dispersi~n of the collector throughout the pulp . ~
In some cases, it may be necessary to add a small amount of fuel oil and/or a conventional frothing agant to the pulp. When used, the fro~hing agent can be incorporated into the pulp before, after, or togethec with the collector. If the frothing agent is added separa~ely, the pulp is mixed for a sufficient time to insure uniform dispersion of the frothing agent throughout the pulp.
Following conditioning, the pulp is withdrawn ~rom the conditioning vessel 46 by a pump 4~ and introduced into the column through the pulp inlet 18.
~`
~2~
The flow rates of the ore pulp, the air and the wash water can be adjusted to ob~ain a material balance which provides the most effective separation of the floatable particles (e.g., iron oxide) from the non-floatable particles (e.g., gangue).
The device and proces6 of the invention have several advantages over conventional flotation devices and processes. They provide all the advantages of conventional flotation columnc and further provide increased air-to-particle contact, eliminate the need for a pecial device in the bottom of the column for generating fine air bubbles, and require less water and energy. More importantly, floatable particles, such as iron oxide, can be more effectively separated from non-floatable particles, such as yangue, with single stage flo~ation. That is, a conventional Plotation column usually requires at least two flotation stages to recover the same amount of iron oxide from a low grade iron ore.
In addition ~o being used for single stage flotation, the device of ~he in~ention can be used in combination with conven~ional flotation machines and two or more can be used in series.
The following examples are presented to illustrate the invention and are not ~o be construed as limitations thereof.
EXAMPLE l A series of laboratory tests were run on an experimental column consisSing of a 2-inch I.D.
tube, 8 feet long and almost entirel~ packed with
2-inch long conventional brass tower packing cylinders.
~2~ 6~ .
Samples of -10 mesh oxidized taconite ore (obtained from the Cascade deposit owned by Clevel2nd-Cliffs Iron Company) were ground batchwise at 60 weight % solids in a rod mill in the presence of water for about 20 minutes to produce a slurry or pulp o~ about 80 weight % passing 500 mesh. The pulp was co~ditioned with a conditioning ceagent prepared in acc~rdance with U.S. Patent 4,132,635 and the pH
was ad~usted to 8.8 by adding soda or sulfuri~ acid.
The resulting pulp samples were separately introduced - into a stirred container where a fatty acid collector (PAMAK*~, No. 2 fuel oil, and a frothing agent were added and mixed into the pulp.
The conditioned pulp samples containing 20% so~ids were continuously pumped from the stirred contai~er into the mid-section of the column a~ a rate o~ about 130 cc/min. Water was introduced near the top of the column at a flow rate of about 50 - cc~min_ and air was introduced near the bottom of the column at a flow rate of about 8 l/min.
Samples of the concentrate and tailings, respectively ta~en from the top and bottom of the column~ were collected and analyzed for iron conten~. Results from the representative tests are ~ummarized in Table I.
These results demonstrate the superior separa~ion e~ficiency of a flotation column arranyed and operated in accordance with the invention, even though only a single flotation stage is employed.
A series of pilot plant tests were run on a column arrangPd generally in the manner illustrated in Fig. 1 and a conventional 8-stage * trade mark ,~
i ~``
. . .
WEM`CG Fagergren flotation machine. The column was 20 feet ~all, had a 7 l/q in. ~ 7 1/~ in. square cross section, and included six 3-foot sections of packing plates. Each packing section was packed with 5 layers of corrugated plates. The plate corrugations were 1/8 inch high and extended a~ about 45 to the horizontal, and alternate layers or sec~ions were oriented at 90 to each other.
An oxidized taconite ore was ground to about 75% -500 mesh and formed into a pulp. A
conditioning reagent prepared in accordance with U.S.
Patent 4,132,635, an anionic collector (PAM~-4), and No. 2 fuel oil were mixed into the pulp. One stream of the conditioned pulp containing about 20 weight %
solids was pumped into the ~eed compartment of the column at a feed rate of about 150 lbsfhr and another stream of the same pulp was processed in the conventional flotation machineO Air at a pressure of about 10-12 psig was introduced into a column through ~0 the gas inlet at a rate of about 300-500 ft3~hr and wash water was s~rayed into the froth chamher a~ a rate of about 30-50 gal/hr.
Samples of the froth concentrate and tailings from the column and the conventional flotation machine were collected and analyzed for iIon content. The results from these tests are summarized in Table II. Under the "Mach7ne Used"
heading in Table II, "A" designates the device of the invention and "B" designates the conventional flotation machine.
From these results, it can be seen that single stage flotation with a column and process of the invention produces higher grade concentrates and~or higher recove~ies than eight stages o a conventional flotation machine.
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~0~67 From the foregoing description. one .
skilled in the art can easily ascertain the essential characteristics of the invention, and without departing from the spirit and scope thereof, make 5 various modif ications and changes to adapt it ~o variou~ usages and conditions.
~2~ 6~ .
Samples of -10 mesh oxidized taconite ore (obtained from the Cascade deposit owned by Clevel2nd-Cliffs Iron Company) were ground batchwise at 60 weight % solids in a rod mill in the presence of water for about 20 minutes to produce a slurry or pulp o~ about 80 weight % passing 500 mesh. The pulp was co~ditioned with a conditioning ceagent prepared in acc~rdance with U.S. Patent 4,132,635 and the pH
was ad~usted to 8.8 by adding soda or sulfuri~ acid.
The resulting pulp samples were separately introduced - into a stirred container where a fatty acid collector (PAMAK*~, No. 2 fuel oil, and a frothing agent were added and mixed into the pulp.
The conditioned pulp samples containing 20% so~ids were continuously pumped from the stirred contai~er into the mid-section of the column a~ a rate o~ about 130 cc/min. Water was introduced near the top of the column at a flow rate of about 50 - cc~min_ and air was introduced near the bottom of the column at a flow rate of about 8 l/min.
Samples of the concentrate and tailings, respectively ta~en from the top and bottom of the column~ were collected and analyzed for iron conten~. Results from the representative tests are ~ummarized in Table I.
These results demonstrate the superior separa~ion e~ficiency of a flotation column arranyed and operated in accordance with the invention, even though only a single flotation stage is employed.
A series of pilot plant tests were run on a column arrangPd generally in the manner illustrated in Fig. 1 and a conventional 8-stage * trade mark ,~
i ~``
. . .
WEM`CG Fagergren flotation machine. The column was 20 feet ~all, had a 7 l/q in. ~ 7 1/~ in. square cross section, and included six 3-foot sections of packing plates. Each packing section was packed with 5 layers of corrugated plates. The plate corrugations were 1/8 inch high and extended a~ about 45 to the horizontal, and alternate layers or sec~ions were oriented at 90 to each other.
An oxidized taconite ore was ground to about 75% -500 mesh and formed into a pulp. A
conditioning reagent prepared in accordance with U.S.
Patent 4,132,635, an anionic collector (PAM~-4), and No. 2 fuel oil were mixed into the pulp. One stream of the conditioned pulp containing about 20 weight %
solids was pumped into the ~eed compartment of the column at a feed rate of about 150 lbsfhr and another stream of the same pulp was processed in the conventional flotation machineO Air at a pressure of about 10-12 psig was introduced into a column through ~0 the gas inlet at a rate of about 300-500 ft3~hr and wash water was s~rayed into the froth chamher a~ a rate of about 30-50 gal/hr.
Samples of the froth concentrate and tailings from the column and the conventional flotation machine were collected and analyzed for iIon content. The results from these tests are summarized in Table II. Under the "Mach7ne Used"
heading in Table II, "A" designates the device of the invention and "B" designates the conventional flotation machine.
From these results, it can be seen that single stage flotation with a column and process of the invention produces higher grade concentrates and~or higher recove~ies than eight stages o a conventional flotation machine.
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~0~67 From the foregoing description. one .
skilled in the art can easily ascertain the essential characteristics of the invention, and without departing from the spirit and scope thereof, make 5 various modif ications and changes to adapt it ~o variou~ usages and conditions.
Claims (13)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A device for concentrating by froth flotation a floatable material in an aqueous pulp containing a mixture of floatable and non-floatable particles, said device comprising a tubular flotation column having an upper portion including a primary cleaning zone, a lower portion including a scavenging zone, and an intermediate portion including a pulp inlet zone between said cleaning and scavenging zones;
packing means disposed in only said cleaning and scavenging zones and defining a large number of small flow passages extending in a circuitous pattern through the respective zone;
pulp feed means for introducing an aqueous pulp into said pulp inlet zone for flow through said flow passages;
means for introducing wash water into said upper portion of said column above said cleaning zone for downward flow through said flow passages;
means for introducing a pressurized inert gas into said lower portion of said column below said scavenging zone for upward flow through said flow passages, whereby the gas, as it flows upwardly through said flow passages, is broken into fine bubbles which intimately contact the particles of the aqueous pulp in said flow passages;
means for discharging a float overflow fraction containing floated particles of the aqueous pulp from the upper portion of said column above said cleaning zone; and means for discharging a tailing fraction containing non-floated particles of the aqueous pulp from the lower portion of said column below said scavenging zone.
packing means disposed in only said cleaning and scavenging zones and defining a large number of small flow passages extending in a circuitous pattern through the respective zone;
pulp feed means for introducing an aqueous pulp into said pulp inlet zone for flow through said flow passages;
means for introducing wash water into said upper portion of said column above said cleaning zone for downward flow through said flow passages;
means for introducing a pressurized inert gas into said lower portion of said column below said scavenging zone for upward flow through said flow passages, whereby the gas, as it flows upwardly through said flow passages, is broken into fine bubbles which intimately contact the particles of the aqueous pulp in said flow passages;
means for discharging a float overflow fraction containing floated particles of the aqueous pulp from the upper portion of said column above said cleaning zone; and means for discharging a tailing fraction containing non-floated particles of the aqueous pulp from the lower portion of said column below said scavenging zone.
2. A device according to Claim 1 wherein said packing means comprises a plurality of vertically extending plates; and spacer means for laterally spacing said plates apart to define a plurality of flow passages between adjacent plates.
3. A device according to Claim 2 including a plurality of vertically adjacent, separate sections of said plates.
4. A device according to Claim 3 wherein said sections are oriented so that the vertical planes of the plates in each of said section are angularly related to the vertical planes of the plates in the adjacent section.
5. A device according to Claim 3 wherein said spacer means comprises rows of corrugations on each of said plates extending diagonally relative to the horizontal.
6. A device according to Claim 5 wherein the corrugations of adjacent plates extend in opposite directions.
7. A process for concentrating by froth flotation a floatable material in an aqueous pulp containing a mixture of floatable and non-floatable particles, said process including the steps of providing a generally tubular flotation column having an upper portion including a cleaning zone, a lower portion including a scavenging zone, an intermediate portion including a pulp inlet zone between said cleaning and scavenging zones;
providing in only said cleaning and scavenging zones packing means defining a large number of flow passages extending in a circuitous pattern through the respective zone;
preparing the aqueous pulp for flotation separation of the particles of the aqueous pulp;
introducing the resulting pulp into the pulp inlet zone for flow through the flow passages of the packing means;
introducing wash water into the upper portion of the column for downward flow through the flow passages of the packing means;
introducing a pressurized inert gas into the lower portion of the column for upward flow through the flow pas-sages of the packing means, whereby the gas is broken into fine bubbles which intimately contact the particles of the aqueous pulp in the flow passages of the packing means;
withdrawing a float fraction containing the floated particles of the aqueous pulp from the upper portion of said column above the cleaning zone; and withdrawing a tailing fraction containing non-floated particles of the aqueous pulp from the lower portion of the column below the scavenging zone.
providing in only said cleaning and scavenging zones packing means defining a large number of flow passages extending in a circuitous pattern through the respective zone;
preparing the aqueous pulp for flotation separation of the particles of the aqueous pulp;
introducing the resulting pulp into the pulp inlet zone for flow through the flow passages of the packing means;
introducing wash water into the upper portion of the column for downward flow through the flow passages of the packing means;
introducing a pressurized inert gas into the lower portion of the column for upward flow through the flow pas-sages of the packing means, whereby the gas is broken into fine bubbles which intimately contact the particles of the aqueous pulp in the flow passages of the packing means;
withdrawing a float fraction containing the floated particles of the aqueous pulp from the upper portion of said column above the cleaning zone; and withdrawing a tailing fraction containing non-floated particles of the aqueous pulp from the lower portion of the column below the scavenging zone.
8. A process according to Claim 7 wherein the pulp contains a mineral ore including a mixture of mineral value particles and gangue particles; and the pulp is prepared for flotation by treating with flotation reagents which are effective for promoting separation of the mineral value and the gangue by flotation.
9. A process according to Claim 8 wherein said mineral ore is a low-grade iron ore.
10. A process according to Claim 7 wherein the packing comprises a plurality of separate, vertically adjacent sections of vertically extending plates; and spacer means for laterally spacing said plates apart to define a plurality of flow passages between adjacent plates.
11. A process according to Claim 10 wherein said sections are oriented so that the vertical planes of the plates in one section is angularly related to the vertical planes of the plates in the adjacent section.
12. A process according to Claim 10 wherein the spacer means comprises rows of corrugations on each of the plates extending diagonally relative to the horizontal
13. A process according to Claim 12 wherein the corrugations of adjacent plates extend in opposite directions.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US50479383A | 1983-06-16 | 1983-06-16 | |
| US504,793 | 1983-06-16 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1210167A true CA1210167A (en) | 1986-08-19 |
Family
ID=24007759
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000455766A Expired CA1210167A (en) | 1983-06-16 | 1984-06-04 | Column froth flotation |
Country Status (6)
| Country | Link |
|---|---|
| EP (1) | EP0144421B1 (en) |
| AU (2) | AU561931B2 (en) |
| CA (1) | CA1210167A (en) |
| DE (1) | DE3485641D1 (en) |
| FI (1) | FI75280C (en) |
| WO (1) | WO1985000021A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7914670B2 (en) | 2004-01-09 | 2011-03-29 | Suncor Energy Inc. | Bituminous froth inline steam injection processing |
| WO2014188232A1 (en) | 2013-05-23 | 2014-11-27 | Dpsms Tecnologia E Inovação Em Mineração Ltda | Automated system of froth flotation columns with aerators injection nozzles and process |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4966687A (en) * | 1985-12-19 | 1990-10-30 | The Standard Oil Company | Method and apparatus for column flotation of mineral matter |
| US4964576A (en) * | 1988-04-04 | 1990-10-23 | Datta Rabinder S | Method and apparatus for mineral matter separation |
| GB8925833D0 (en) * | 1989-11-15 | 1990-01-04 | Robertet Sa | Derivatives of aromatic benzoates as inhibitors of esterase-producing micro-organisms |
| AU629965B2 (en) * | 1990-07-30 | 1992-10-15 | Rabinder S. Datta | Method and apparatus for mineral matter separation |
| DE19611864C1 (en) * | 1996-03-26 | 1997-12-11 | Voith Sulzer Stoffaufbereitung | Flotation process and device for separating solids from a suspension containing paper fibers |
| US7510083B2 (en) | 2004-06-28 | 2009-03-31 | The Mosaic Company | Column flotation cell for enhanced recovery of minerals such as phosphates by froth flotation |
| ITUB20156822A1 (en) * | 2015-12-11 | 2017-06-11 | Paolo Bozzato | SYSTEM AND PROCEDURE FOR SEPARATION WITH FOAM |
| KR102442975B1 (en) | 2020-04-17 | 2022-09-15 | 한국원자력연구원 | Float sorting device for selective separation of non-metallic minerals |
| CN113275132B (en) * | 2021-05-08 | 2023-03-07 | 武汉工程大学 | Flotation column for reverse flotation of phosphorus ore |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1809646A (en) * | 1926-01-29 | 1931-06-09 | Koppers Co Inc | Apparatus for treating gases |
| US2416066A (en) * | 1944-05-19 | 1947-02-18 | Donald S Phelps | Froth flotation cell |
| US3339730A (en) * | 1962-07-14 | 1967-09-05 | Column Flotation Co Of Canada | Froth flotation method with counter-current separation |
| SE318587B (en) * | 1964-07-10 | 1969-12-15 | C Munters | |
| AU546684B2 (en) * | 1981-01-29 | 1985-09-12 | Gulf & Western Industries Inc. | Froth flotation |
-
1984
- 1984-05-17 AU AU28329/84A patent/AU561931B2/en not_active Ceased
- 1984-06-04 CA CA000455766A patent/CA1210167A/en not_active Expired
- 1984-06-08 FI FI842340A patent/FI75280C/en not_active IP Right Cessation
- 1984-06-13 AU AU31004/84A patent/AU3100484A/en not_active Abandoned
- 1984-06-13 EP EP84902567A patent/EP0144421B1/en not_active Expired - Lifetime
- 1984-06-13 WO PCT/US1984/000926 patent/WO1985000021A1/en active IP Right Grant
- 1984-06-13 DE DE8484902567T patent/DE3485641D1/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7914670B2 (en) | 2004-01-09 | 2011-03-29 | Suncor Energy Inc. | Bituminous froth inline steam injection processing |
| US8685210B2 (en) | 2004-01-09 | 2014-04-01 | Suncor Energy Inc. | Bituminous froth inline steam injection processing |
| WO2014188232A1 (en) | 2013-05-23 | 2014-11-27 | Dpsms Tecnologia E Inovação Em Mineração Ltda | Automated system of froth flotation columns with aerators injection nozzles and process |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0144421A4 (en) | 1988-04-26 |
| AU2832984A (en) | 1984-12-20 |
| FI842340A0 (en) | 1984-06-08 |
| FI75280B (en) | 1988-02-29 |
| DE3485641D1 (en) | 1992-05-14 |
| EP0144421B1 (en) | 1992-04-08 |
| AU561931B2 (en) | 1987-05-21 |
| WO1985000021A1 (en) | 1985-01-03 |
| FI842340A (en) | 1984-12-17 |
| FI75280C (en) | 1988-06-09 |
| AU3100484A (en) | 1985-01-11 |
| EP0144421A1 (en) | 1985-06-19 |
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