US1871121A - Separation of particles of different densities by means of liquids - Google Patents
Separation of particles of different densities by means of liquids Download PDFInfo
- Publication number
- US1871121A US1871121A US433812A US43381230A US1871121A US 1871121 A US1871121 A US 1871121A US 433812 A US433812 A US 433812A US 43381230 A US43381230 A US 43381230A US 1871121 A US1871121 A US 1871121A
- Authority
- US
- United States
- Prior art keywords
- particles
- coal
- liquid
- liquids
- separation
- 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
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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
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
- B03B5/28—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
- B03B5/30—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using heavy liquids or suspensions
- B03B5/44—Application of particular media therefor
- B03B5/442—Application of particular media therefor composition of heavy media
Definitions
- This invention relates to the separationof particles of different densities by Ineansof liquids.
- the invention will principally be described with reference to the cleaning of coal,.this usually being effected by pneumatic separation on tables which may be stationary or moving.
- the object of the present invention is to provide an improved or modified method.
- the invention consists in a method for the separation of particles of difierent densities 5 by means of liquids particularly for the clean ing of coal according to which the mixture is first treated with a protecting liquid comprising oil or other substances which will minimize the wetting of the solidmaterialby the high density liquid and the thustreated material then submitted to the action of a liquid of density intermediatebetween that of the coal or other material to be concentrated and the associated refuse or material to be separated therefrom.
- the invention also consists in methodsfor the separation of particles of different densities by means of liquids substantially as herein described. i
- I In carrying the invention into effect intone form by way of example applied to the-cleaning of coal, I first treat the material with oil or'the like in-the form of a finespray or 'mist and next submit it to the action of a solution having a density greater than coal but less than stone, and preferably having high surface tension so that the pretreated particles are not unduly wetted when immersed in the solution.
- Suitable separating liquids are solutions of calcium chloride or zinc chloride.
- paraflin oil forms a convenient substance which may be applied by spraying, this being preferably carried out while the material is being fed to the tanks containing the liquids, on a bar screen, so that the whole of the surface can be covered with the spray.
- any suitable apparatus may be used, the following by way of example j
- the raw product is delivered by means of a travelling bar'screen, or the like,so that the'whole of the surface of the particle is available for spraying past the oil sprays, and into the tank containing the separating liquid.
- the light particles float andthe heavy ones sink, whence they may be removed by any suitable mechanical means whereby the high density liquid is not removed along with the solid particles.
- any suitable means may be provided whereby accumulations of sludge may be tapped off from the bottom of the tanks as oocasion demands. If necessary, the treated particles may be sprayed with water to remove traces of adhering heavy density liquid. 7
- the invention is particularly useful in connection with particles from the size of 1 cube upwards.
- coal hasjaspecific gravity less than about 1.35.
- density between about 1 .35 and about 1.75 and some heavy high ash refuse maybe presenthaving a densityhigher-than about 1.75.
- V e w 1 ,A an alternative to the spray'treatment of thecoalby paraifin' oil, a layer'of paraffin oil, or the like may'be fioated on the, surface ofthe high density liquid so thatv the coal must pass through, the paraffin, or the 7 like, beigreit r ach sth high d n ty iq d-j As quantities of liquidylarge quantities being objectionable as they would spoil the ap pearance of the coal and have several other objections.
- V I an alternative to the spray'treatment of thecoalby paraifin' oil, a layer'of paraffin oil, or the like may'be fioated on the, surface ofthe high density liquid so thatv the coal must pass through, the paraffin, or the 7 like, beigreit r ach sth high d n ty iq d-j As quantities of liquidylarge quantities being objectionable as they would spoil the ap pearance of the coal and have several other objections.
- the invention therefore,is particularly suitable for the separation of large particles of stone from large particles of coal, that is to say, material which is usually separated by hand-picking.
- T he invention provides a mechanical process for the treatment of large coal whereby the labor normally employed in hand-pick ing the refuse is eliminated.
- two liquid media of difierent densities may be employed, and one of the products from the first tank re-treated in the second liquid.
- a second treatment with oil or other substances which will minimize the wetting of the solid material by the high density liquid may be applied after the coal or other material to be concentrated has been subjected to the first liquid medium and before it is subjected to the action of the second liquid medium.
- a coal may contain by weight of its particles lighter than 1. 1 specific gravity with an ash content of 5%, 20% by weight of its particles with a'density between 14 and 1.7' and having an ash content of 30%; and 10% by weight of its particles having densities; higher than1.7 and having anash content of 70%,that is to say, consisting practically of pure shale.
- the first treatment in a liquid medium may be in the liquid of 1.4: density, so that only 30% of the input to the first stage need be re-treated in the second stage at 1.7 density.
- the resulting products containing 5, 80, and 70% of ash respectively may be marketed as regards the first two as first class coal and second class coal, and the third product discarded as worthless.
- the second product may be broken down to a smaller size to liberate the intergrown layers of coal and stone, and such crushed product may be treated by this or any other process.
- i i 1 A process of separating a material having solid constituents of different specific gravities; comprising water-proofing by means of oily substances of the material containing a high proportion ofivaluable'constituents and being highly adsorptive of water and aqueous saline solutions, floating off said valuable constituents on a saline solution of specific gravity intermediate that of the valuable'fand waste constituents, and draining the water-proofed valuable constituents to yield :a dry concentrate free from water and saline solution.
- a process of separating a material having solid constituents of different specific gravities comprising water-proofing by means of'oily substances of the material containing a high proportion of valuable constituents and being highly adsorptive of water and aqueous saline solutions, floating 0E said valuable constituents on a saline solution of specific gravity intermediate that of the valuable and waste constituents, and drainingthe water-proofe'd-valuable constituents to yield a dry concentrate free from water and saline solution, the size of the particles treated being from about 1-inch cube upwards; 1 In testimony'whereof I have signed my name to this specification. f
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Description
Patented Aug. 9, 1932 UNITED s-T Arss ooLIn WILLIAM I-IIGHAM CQLMES, or IiO W FELL, ENGLAND, ASSIGNOR or onE-HALE TO THE EIET EY molt ,QOIMJEANY, LnvrrrEnoE BIRTLEY, ENGLAND Y SEPARATION or PARTICLES or DIEEE ENT DEnsrrIEsEY MEANS F mourns No Drawing. Application filed March 6, 1930, Serial No. 133312, and in Great Britain March 8, 1929.
This invention relates to the separationof particles of different densities by Ineansof liquids.
It is particularly directed to thecleaning 5 of coal but it is not limited thereto.,
The invention will principally be described with reference to the cleaning of coal,.this usually being effected by pneumatic separation on tables which may be stationary or moving.
The object of the present invention is to provide an improved or modified method.
The invention consists in a method for the separation of particles of difierent densities 5 by means of liquids particularly for the clean ing of coal according to which the mixture is first treated with a protecting liquid comprising oil or other substances which will minimize the wetting of the solidmaterialby the high density liquid and the thustreated material then submitted to the action of a liquid of density intermediatebetween that of the coal or other material to be concentrated and the associated refuse or material to be separated therefrom. a v
The invention also consists in methodsfor the separation of particles of different densities by means of liquids substantially as herein described. i
In carrying the invention into effect intone form by way of example applied to the-cleaning of coal, I first treat the material with oil or'the like in-the form of a finespray or 'mist and next submit it to the action of a solution having a density greater than coal but less than stone, and preferably having high surface tension so that the pretreated particles are not unduly wetted when immersed in the solution.
Suitable separating liquids are solutions of calcium chloride or zinc chloride.
As to the pretreatment of the mixture to be separated, paraflin oil forms a convenient substance which may be applied by spraying, this being preferably carried out while the material is being fed to the tanks containing the liquids, on a bar screen, so that the whole of the surface can be covered with the spray.
In carrying this process into efieot any suitable apparatus may be used, the following by way of example j The raw product is delivered by means of a travelling bar'screen, or the like,so that the'whole of the surface of the particle is available for spraying past the oil sprays, and into the tank containing the separating liquid. Here the light particles float andthe heavy ones sink, whence they may be removed by any suitable mechanical means whereby the high density liquid is not removed along with the solid particles.
Any suitable means may be provided whereby accumulations of sludge may be tapped off from the bottom of the tanks as oocasion demands. If necessary, the treated particles may be sprayed with water to remove traces of adhering heavy density liquid. 7
General.
By means of the present invention a simple method is provided for the cleaning of coal and the like enabling larger pieces of material to be treated than those which are usually treated with the pneumatic separating processes or with such processes as the ore froth flotation processes.
The invention is particularly useful in connection with particles from the size of 1 cube upwards.
It is preferred to work with a liquid of density not less than about 11 when the cleaning of coal comes into question, but the densities of the particles to be separatedmust be borne in mind. Generally speaking coal hasjaspecific gravity less than about 1.35. There is usually a certain amount of intergrown material with density between about 1 .35 and about 1.75 and some heavy high ash refuse maybe presenthaving a densityhigher-than about 1.75. In the case of anthracite the density of the reasonably pure material may be as high as about1.9.; V e w 1 ,As an alternative to the spray'treatment of thecoalby paraifin' oil, a layer'of paraffin oil, or the like may'be fioated on the, surface ofthe high density liquid so thatv the coal must pass through, the paraffin, or the 7 like, beigreit r ach sth high d n ty iq d-j As quantities of liquidylarge quantities being objectionable as they would spoil the ap pearance of the coal and have several other objections. V I
The smaller the particles treated, the greater the amount of surface per unit-weight there will be which mustbe covered .in the first place by the oil reagent, and the greater theloss of high density liquid.
The invention, therefore,is particularly suitable for the separation of large particles of stone from large particles of coal, that is to say, material which is usually separated by hand-picking. I
T he invention provides a mechanical process for the treatment of large coal whereby the labor normally employed in hand-pick ing the refuse is eliminated.
In a form of the invention, which is par' ticularly applicable to coals containing a high percentage of material of intermediate density, two liquid media of difierent densities may be employed, and one of the products from the first tank re-treated in the second liquid.
Before the coal is subjected to the action of the first liquid it is treated with oil or other substances which will minimize the wetting of the solid material by the high density liquid. I
In addition to the treatment with oil or other substances which will minimize the wetting of the solid material by the high density liquid before the coal or other material to be concentrated is subjected'to the first liquid medium a second treatment with oil or other substances which will minimize the wetting of the solid material by the high density liquid may be applied after the coal or other material to be concentrated has been subjected to the first liquid medium and before it is subjected to the action of the second liquid medium. 1
F orexample, a coal may contain by weight of its particles lighter than 1. 1 specific gravity with an ash content of 5%, 20% by weight of its particles with a'density between 14 and 1.7' and having an ash content of 30%; and 10% by weight of its particles having densities; higher than1.7 and having anash content of 70%,that is to say, consisting practically of pure shale.
With such a coal, after the coal-has been subjected to the action of oil "or other sub stances which will minimize the Wetting of the solid material by the high density liquid the first treatment in a liquid medium may be in the liquid of 1.4: density, so that only 30% of the input to the first stage need be re-treated in the second stage at 1.7 density. The resulting products containing 5, 80, and 70% of ash respectively may be marketed as regards the first two as first class coal and second class coal, and the third product discarded as worthless. I
In such cases as offer economical advantages, the second product may be broken down to a smaller size to liberate the intergrown layers of coal and stone, and such crushed product may be treated by this or any other process. l i s Having now described my invention, what I claim as new and desire to secure by Letters Patent is i i 1; A process of separating a material having solid constituents of different specific gravities; comprising water-proofing by means of oily substances of the material containing a high proportion ofivaluable'constituents and being highly adsorptive of water and aqueous saline solutions, floating off said valuable constituents on a saline solution of specific gravity intermediate that of the valuable'fand waste constituents, and draining the water-proofed valuable constituents to yield :a dry concentrate free from water and saline solution.
2. A process of separating a material having solid constituents of different specific gravities; comprising water-proofing by means of'oily substances of the material containing a high proportion of valuable constituents and being highly adsorptive of water and aqueous saline solutions, floating 0E said valuable constituents on a saline solution of specific gravity intermediate that of the valuable and waste constituents, and drainingthe water-proofe'd-valuable constituents to yield a dry concentrate free from water and saline solution, the size of the particles treated being from about 1-inch cube upwards; 1 In testimony'whereof I have signed my name to this specification. f
' VCOLINWILLIAM HIGHAM HOLMES.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB7638/29A GB331841A (en) | 1929-03-08 | 1929-03-08 | Improvements in or relating to the separation of particles of different densities by means of liquids |
Publications (1)
Publication Number | Publication Date |
---|---|
US1871121A true US1871121A (en) | 1932-08-09 |
Family
ID=9836939
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US433812A Expired - Lifetime US1871121A (en) | 1929-03-08 | 1930-03-06 | Separation of particles of different densities by means of liquids |
Country Status (4)
Country | Link |
---|---|
US (1) | US1871121A (en) |
DE (1) | DE606652C (en) |
FR (1) | FR691309A (en) |
GB (1) | GB331841A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2483372A (en) * | 1947-10-29 | 1949-09-27 | Socony Vacuum Oil Co Inc | Heavy gravity liquid separation of porous catalyst |
US2556496A (en) * | 1947-12-09 | 1951-06-12 | Great Lakes Carbon Corp | Purification of coal |
US2643215A (en) * | 1947-03-01 | 1953-06-23 | Houdry Process Corp | Treatment and use of porous contact masses |
US2832470A (en) * | 1954-06-30 | 1958-04-29 | Shell Dev | Process for fractionating mixtures of solid particles of different porosities |
US11135596B2 (en) | 2016-11-18 | 2021-10-05 | Feelgood Metals B.V. | Separation process with separation media loss reduction |
CN116713103A (en) * | 2023-08-02 | 2023-09-08 | 江苏时代新能源科技有限公司 | Separation method and detection method for impurity metal particles in cathode powder |
-
1929
- 1929-03-08 GB GB7638/29A patent/GB331841A/en not_active Expired
-
1930
- 1930-03-06 FR FR691309D patent/FR691309A/en not_active Expired
- 1930-03-06 DE DE1930606652D patent/DE606652C/en not_active Expired
- 1930-03-06 US US433812A patent/US1871121A/en not_active Expired - Lifetime
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2643215A (en) * | 1947-03-01 | 1953-06-23 | Houdry Process Corp | Treatment and use of porous contact masses |
US2483372A (en) * | 1947-10-29 | 1949-09-27 | Socony Vacuum Oil Co Inc | Heavy gravity liquid separation of porous catalyst |
US2556496A (en) * | 1947-12-09 | 1951-06-12 | Great Lakes Carbon Corp | Purification of coal |
US2832470A (en) * | 1954-06-30 | 1958-04-29 | Shell Dev | Process for fractionating mixtures of solid particles of different porosities |
US11135596B2 (en) | 2016-11-18 | 2021-10-05 | Feelgood Metals B.V. | Separation process with separation media loss reduction |
CN116713103A (en) * | 2023-08-02 | 2023-09-08 | 江苏时代新能源科技有限公司 | Separation method and detection method for impurity metal particles in cathode powder |
CN116713103B (en) * | 2023-08-02 | 2024-01-02 | 江苏时代新能源科技有限公司 | Separation method and detection method for impurity metal particles in cathode powder |
Also Published As
Publication number | Publication date |
---|---|
DE606652C (en) | 1934-12-07 |
GB331841A (en) | 1930-07-08 |
FR691309A (en) | 1930-10-20 |
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