US3356211A - Separation of ore particles preferentially coated with liquid fluorescent material - Google Patents

Separation of ore particles preferentially coated with liquid fluorescent material Download PDF

Info

Publication number
US3356211A
US3356211A US416293A US41629364A US3356211A US 3356211 A US3356211 A US 3356211A US 416293 A US416293 A US 416293A US 41629364 A US41629364 A US 41629364A US 3356211 A US3356211 A US 3356211A
Authority
US
United States
Prior art keywords
ore
particles
fluorescent material
coated
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
Application number
US416293A
Inventor
Ted C Mathews
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US416293A priority Critical patent/US3356211A/en
Priority to GB50118/65A priority patent/GB1078430A/en
Priority to DEM67544A priority patent/DE1237512B/en
Priority to SE15736/65A priority patent/SE311501B/xx
Priority to OA52273A priority patent/OA02048A/en
Priority to FR41290A priority patent/FR1475692A/en
Application granted granted Critical
Publication of US3356211A publication Critical patent/US3356211A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B1/00Conditioning for facilitating separation by altering physical properties of the matter to be treated
    • B03B1/04Conditioning for facilitating separation by altering physical properties of the matter to be treated by additives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B1/00Conditioning for facilitating separation by altering physical properties of the matter to be treated
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07CPOSTAL SORTING; SORTING INDIVIDUAL ARTICLES, OR BULK MATERIAL FIT TO BE SORTED PIECE-MEAL, e.g. BY PICKING
    • B07C5/00Sorting according to a characteristic or feature of the articles or material being sorted, e.g. by control effected by devices which detect or measure such characteristic or feature; Sorting by manually actuated devices, e.g. switches
    • B07C5/34Sorting according to other particular properties
    • B07C5/342Sorting according to other particular properties according to optical properties, e.g. colour
    • B07C5/3425Sorting according to other particular properties according to optical properties, e.g. colour of granular material, e.g. ore particles, grain
    • B07C5/3427Sorting according to other particular properties according to optical properties, e.g. colour of granular material, e.g. ore particles, grain by changing or intensifying the optical properties prior to scanning, e.g. by inducing fluorescence under UV or x-radiation, subjecting the material to a chemical reaction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07CPOSTAL SORTING; SORTING INDIVIDUAL ARTICLES, OR BULK MATERIAL FIT TO BE SORTED PIECE-MEAL, e.g. BY PICKING
    • B07C5/00Sorting according to a characteristic or feature of the articles or material being sorted, e.g. by control effected by devices which detect or measure such characteristic or feature; Sorting by manually actuated devices, e.g. switches
    • B07C5/36Sorting apparatus characterised by the means used for distribution
    • B07C5/363Sorting apparatus characterised by the means used for distribution by means of air
    • B07C5/365Sorting apparatus characterised by the means used for distribution by means of air using a single separation means
    • B07C5/366Sorting apparatus characterised by the means used for distribution by means of air using a single separation means during free fall of the articles

Definitions

  • ABSTRACT OF THE DISCLOSURE The patent describes a method for the concentration of ore by subjecting a quantity of crushed ore containing various types of minerals to electromagnetic radiation to cause at least a portion thereof to fluoroesce at a characteristic wavelength distinct from that of the rest of the ore mass, and sensing the characteristic wavelength emitted by the radiated particles.
  • the fluorescence of at least one portion of the ore at characteristic wavelength distinct from that of the rest of the ore is achieved by the preferential coating of some of the ore particles with a liquid fluorescent material.
  • the desired mineral may be separated from the worthless portion by radiating the ore to cause a portion of it to emit at a characteristic wavelength and sensing the emitted rays.
  • the sensed rays are used to operate means for separating the ore into a desired and an undesired portion.
  • the desired separation may be achieved by first treating a quantity of the ore with a liquid which preferentially coats the particles of one of the portions of the ore and is also capable of emitting at a characteristic wavelength upon exposure to ultraviolet light, X-rays, or other suitable type of electromagnetic radiation.
  • the treated ore is then passed to a separation zone where an electromagnetic wave means sensitive to the characteristic wavelength detects which particles are coated and which particles are not.
  • the sensing means then functions to actuate a deflecting means which physically removes the coated particles from the body of ore particles.
  • a desired or undesired type of mineral may be removed from the mass of ore.
  • a portion of a body of ore is caused to emit a characteristic wavelength, which wavelength is unlike that emitted by the rest of the ore.
  • the ore particles are then separated according to whether they emit the characeristic wavelength.
  • This is preferably accomplished in the following manner.
  • a quantity of ore containing at least one valuable mineral portion is first treated with a liquid which preferentially coats the particles of one of the minerals in the ore.
  • the coating liquid in adition to being specific to particles of one of the minerals in the ore, is also capable of fluoroescing at a characteristic Wavelength after exposure to ultraviolet, X-rays, or any other suitable type of radiation. For this reason, the coating liquid is sometimes referred to as the fiuoroscent material.
  • the ore which in the preferred embodiment has been treated with the fluorescent material to provide both coated and uncoated particles, is placed on a conveyor 1 and caused to drop from the end of conveyor in a downward path past a radiation source 2, into a zone where the characteristic radiation emitted by the radiated particles is received in an electromagnetic wave-sensing means 3.
  • the wave energy received by means 3 produces a small current which is amplified by an amplifier 4.
  • the output of the amplifier then triggers a rectifier switch 5 which, in turn, energizes deflecting means 6, normally a solenoidoperated air jet, water jet, or mechanical gate.
  • the deflecting means knocks the particle emitting at the characteristic wavelength out of the stream of ore particles. These particles are received in collector 7, with the balance of the particles falling into collector 8.
  • the coating may be dispensed with in the case of natural iluorescing ores. These ores, upon excitation, emit at a characteristic wavelength which can be used to activate separation. Typical materials that can be recovered from ore mixtures without coating or other pretreatment are willemite, hydrozincite, uranite, calcite and sheelite. Other ores separated by the technique of this invention are first pretreated to provide a preferential coating capable of emitting at a charactersitic wavelength upon exposure to one of the many forms of electromagnetic radiation.
  • fluorescence refers to the property of absorbing radiation at one particular Wavelength and re-emitting it as light of a different wavelength so long as the stimulus is active.
  • fluorescence is used generically herein to include the limited definitions of both fluorescence and phosphorescence, and envisions the emission of a characteristic wavelength whether or not visible.
  • a wire variety of organic materials which fiuoresce at a characteristic wavelength upon excitation by ultraviolet light, X-rays, or other radiation may be used to preferentially coat either the desired or the undesired portion of the ore.
  • organic fluorescent substances are anthracene, fluorescein, chrysene, aminoacetal picrate, petroleum base lubricating oil, allylamine picrate, aluminum palmitate, ammonium mandelate, calcium triethanolamine theobroinine, ferrous stearate, glyceryl monooleate, glyceryl monostearate, hydrastine, hydrastine chloride, lead naphthenate, lead linoleate, lead stearate, manganous stearate and benzene. Certain of these materials are solids at ordinary temperatures and hence are used in solution. For example, anthracene may be dissolved in benzene.
  • collectors are usually long chain molecules with an atomic group which orients on the particle surface and another group which orients on the fluorescent substance. While not bound by any theory, it is believed that the collector is preferentially absorbed on the mineral surface and displaces the water film normally present thereon.
  • Collectors may be of any one of several types and are generally classified on the basis of their surface attachment into three groups-anionic, cationic and neutral.
  • Anionic collectors usch as xanthates adhere to minerals with a positive surface potential such as metals and sulfides.
  • Cationic collectors usch as amines adhere to surfaces having a negative charge such as silicates.
  • the neutral collectors such as petroleum derivatives adhere to surfaces more positive than the neutral hydrocarbon.
  • the use of a collector is not always require-d.
  • many petroleum base lubricating oils will both preferentially adhere to certain minerals and also fluoresce when excited by electromagnetic radiation.
  • the following list is merely illustrative of some of the anionic collectors which may be employed in this invention: the alkali alkyl xanthates, such as sodium sec-butyl xanthate, potassium ethyl xanthate, sodium ethyl xanthate and potassium amyl xanthate; aryl dithiophosphoric acids such as phenyl dithiophosphoric acid; fatty acids such as stearic acid; thio carbanilide; saponified fatty acids such as sodium stearate and potassium stearate; sulfonated oils; glycerides such as tripalmitin and tristearin; and alcohols.
  • the alkali alkyl xanthates such as sodium sec-butyl xanthate, potassium
  • the cationic collectors include the alkyl ammonium halides such as amyl trimethyl ammonium bromide and cetyl trimethyl ammonium bromide; the alkali metal and alkaline earth metal alkyl aryl sulfonates such as sodium dodecyl benzene sulfonate and calcium dodecyl benzene sulfonate; the alkyl ammonium acetates such as dodecylammonium acetate; long-chain alcohols such as dodecyl alcohol; ethylenically unsaturated monocarboxylic acids and their soaps such as oleic acid, linoleic acid, sodium oleate and sodium linoleate; fatty amine acetates; and benzene.
  • alkyl ammonium halides such as amyl trimethyl ammonium bromide and cetyl trimethyl ammonium bromide
  • the fluorescent material and the collector may be applied to the ore in a variety of ways, including spraying and dipping.
  • the fluorescent material is added to the collector prior to ore treatment.
  • the ore may be treated with the collector and the fluorescent material sequentially. Any excess of the fluorescent material or collector may be readily removed by washing with water.
  • a fluorescent ore, or the fluorescent material preferentially absorbed on some of the ore particles can be caused to fluoresce at a characteristic wavelength by radiation from the full spectrum of electromagnetic energy, varying from radio waves through infrared, visible, ultraviolet, gamma rays, and ionic bombardment.
  • the specific type of radiation employed in any given situation will depend upon the particular fluorescent material being used. For example, anthracene and petroleum base lubricating oils upon exposure to ultraviolet light (25003700 angstroms) will fluoresce strongly at about 4000 angstroms.
  • any ore portion whether naturally fluorescent or not, may be readily separated from any other portion. It will, therefore, be recognized that the following examples are presented solely to illustrate the invention and should not be regarded as limitative in any way.
  • Example I A quantity of crushed ore containing primarily quartz and calcite is coated with a petroleum base lubricating oil (sold by the Standard Oil Co. under the name Penn Motor Oil SAE 30). The excess lubricating oil is removed by flushing with water. Microscopic examination of the particles reveals that the quartz rejects the lubricating oil while coating the calcite.
  • the apparatus used to separate the ore includes a conveyor having an ultraviolet light source stationed at its discharge end. Below the ultraviolet source is positioned a 931-A photo multiplier tube sensitive to 4000 A. emissions. A Wratten filter is interposed in the optical path of the tube to eliminate stray ultraviolet.
  • the output of the tube leads to an amplifier which triggers a silicon controlled rectifier switch which, in turn, energizes a solenoid-operated air jet located below the ultraviolet source.
  • the treated ore is placed on the moving conveyor belt at a rate which provides a single layer of ore particles.
  • the ore particles are exposed to ultraviolet light as they leave the end of the conveyor and'are in free fall.
  • the 4000 A. emissions from the coated particles are sensed by the photo multiplier tube. It is found that the air jet deflector actuated by the tube produces a high degree of separation of the coated calcite from the quartz.
  • Example II A quantity of crushed ore containing quartz, sandstone, argillite, schist, quartzite and calcite is first washed to remove adhered particles. The ore is then sprayed with an aqueous mixture of dodecylammonium acetate and anthracene dissolved in benzene. The ore is then washed with water to remove the coating solution from the unwanted portions and to leave a coating of anthracene only on the quartz particles. The quartz is then separated from the rest of the ore according to the procedure and employing the apparatus described in Example I.
  • Example III A quantity of crushed ore containing sulfide minerals, sandstone, argillite, schist and calcite are washed with water to remove adhered particles. The ore is then washed with an aqueous solution of anthracene and phenyl dithiophosphoric acid. The excess is removed by washing with water. It is found that the anthracene preferentially adheres to the surface of the sulfide minerals. The sulfide mineral is then effectively separated from the bulk of the ore in the manner set forth in Example I.
  • the wave sensing means 3 is typically a photo multiplier tube having a sensitivity to specific wavelength bands.
  • the bands received at the sensing means are narrowed, as required, by the use of filters.
  • Tubes are cornmercially available having sensitivities from the infrared to the ultraviolet. Thus, it is a simple matter to select a tube which is sensitive to the characteristic wavelength emitted upon electromagnetic excitation of any given fluorescent ore or material.
  • photo multiplier tubes photons which result from fluorescence are received in a first stage and converted to electrons which are deflected to succeeding states by electrostatic fields and multiplied by secondary emission from each stage.
  • the weak current emerging from the photo multiplier tube may be amplified in a conventional solid state amplifier. Since the current from the amplifier is used to operate deflection means 6, it is usually necessary to incorporate an adjustable delay network in the amplifier in order to achieve register between the position of the particle at the time of detection by the sensing means and the time of deflection.
  • the particles are passed before the sensing means at a high velocity.
  • the sensing means is normally placed so that the ore particles passing before it are in free fall and thus have a high velocity and a fixed path.
  • the sensing means is conveniently located so that the sensing means detects the particles soon after they leave the end of the conveyor. To assure a high degree of separation, the ore particles are fed to the conveyor at arate which provides a single layer. While only one sensing means is shown in the drawing, it will be understood that the number of sensing means used is dependent upon the tonnage of ore particles to be handled, the width of the conveyor, and the size of the particles. The field of detection for each sensing means is limited to an area approximately equal to the area of an individual ore particle.
  • deflecting means 6 has been found to depend on the individual size of the ore particles.
  • An air jet is useful on sizes below /2 inch.
  • a water jet is used on sizes between /2 inch and 4 inches, while a mechanical gate is used for even larger sizes.
  • the method for the concentration of ore which comprises treating a quantity of crushed ore containing various types of minerals with a liquid fluorescent material capable of preferentially coating some of the particles in the ore, radiating the treated quantity of ore to excite the liquid on the coated particles to fluoresce at a characteristic wavelength, and separating the coated particles from the uncoated particles on the basis of the difference in their emitted wavelengths.
  • the method for the concentration of ore which comprises treating a quantity of crushed ore containing various types of minerals with a liquid fluorescent material capable of preferentially coating some of the particles in the ore, radiating the treated quantity of ore to excite the liquid on the coated particles, passing the radiated treated quantity of ore through a zone where the characteristic wavelength emitted by the radiated coated particles is received in an electromagnetic wavesensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic Wave-sensitive element to the characteristic wavelength received therein.
  • the method for the concentration of calcite-containing ore which comprises treating a quantity of calcitecontaining ore containing various types of minerals with a liquid fluorescent material capable of preferentially coating some of the particles in the ore, radiating the treated quantity of ore to excite the liquid on the coated particles, passing the radiated treated quantity of ore through a zone where the characteristic wavelength emitted by the radiated coated particles is received in an electromagnetic wave-sensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic wavesensitive element to the characteristic wavelength received therein.
  • the method for the concentration of quartz-containing ore which comprises treating a quantity of quartzcontaining ore containing various types of minerals with a liquid fluorescent material capable of preferentially coating some of the particles in the ore, radiating the treated quantity of ore to excite the liquid on the coated particles, passing the radiated treated quantity of ore through a zone where the characteristic wavelength emitted by the radiated coated particles is received in an electromagnetic wave-sensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic wave-sensitive element to the characteristic wavelength received therein.
  • the method for the concentration of sulfide-containing ore which comprises treating a quantity of sulfidecontaining ore containing various types of minerals with a liquid fluorescent material capable of preferentially coating some of the particles in the ore, radiating the treated quantity of ore to excite the liquid on the coated particles, passing the radiated treated quantity of ore through a zone where the characteristic Wavelength emitted by the radiated coated particles is received in an electromagnetic wave-sensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic wavesensitive element to the characteristic wavelength received therein.
  • the method for the concentration of ore which comprises treating a quantity of ore containing various types of minerals with anthracene to preferentially coat some of the particles in the ore, radiating the treated quantity of ore to cause the anthracene on the coated particles to fiuoresce, passing the radiated treated quantity of ore through a zone where the characteristic wavelength emitted by the radiated coated particles is received in an electromagnetic Wave-sensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic wavesensitive element to the characteristic wavelength received therein.
  • the method for the concentration of ore which comprises treating a quantity of ore containing various types of minerals with a petroleum base lubricating oil to preferentially coat some of the particles in the ore, radiating the treated quantity of ore to cause the lubricating oil on the coated particles to fiuoresce, passing the radiated treated quantity of ore through a zone Where the characteristic wavelength emitted by the radiated coated parti- 8 cles is received in an electromagnetic wave-sensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic wave-sensitive element to the characteristic wavelength received therein.

Landscapes

  • Silver Salt Photography Or Processing Solution Therefor (AREA)
  • Investigating, Analyzing Materials By Fluorescence Or Luminescence (AREA)
  • Luminescent Compositions (AREA)
  • Photosensitive Polymer And Photoresist Processing (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

Dec. 5, 1967 T. c. MATHEWS 3, SEPARATION OF ORE PARTICLES PREFERENTIALLY COATED WITH LIQUID FLUORESCENT MATERIAL Filed Dec. 7, 1964 O 4=9e9 coeaaavw @O INVENTOR. 750 CI M4 Iva 5W5 United States Patent 3,356,211 SEPARATION OF ORE PARTICLES PREFEREN- TIALLY COATED WITH LIQUID FLUORES- CENT MATERIAL Ted C. Mathews, P.0. Box 2061, Fairbanks, Alaska 99701 Filed Dec. 7, 1964, Ser. No. 416,293 7 Claims. (Cl. 209-9) ABSTRACT OF THE DISCLOSURE The patent describes a method for the concentration of ore by subjecting a quantity of crushed ore containing various types of minerals to electromagnetic radiation to cause at least a portion thereof to fluoroesce at a characteristic wavelength distinct from that of the rest of the ore mass, and sensing the characteristic wavelength emitted by the radiated particles. The fluorescence of at least one portion of the ore at characteristic wavelength distinct from that of the rest of the ore is achieved by the preferential coating of some of the ore particles with a liquid fluorescent material.
A common condition in many mining operations requires the mining of large quantities of worthless rock and the like to permit the recovery of the valuable mineral portion. The mill must then crush, grind and treat all of this material to extract the desired mineral.
To reduce the mill load it is desirable to reject at the mine the worthless material. In the instance where strong visual contrast exists between the mineral and the worthless portion, the mineral is often picked by hand to up grade the feed for the subsequent crushing and grinding operations. Heretofore, it has also been proposed to automatically separate the mineral from the worthless portion by means which detect the difference in the natural color or radioactivity of the mineral and the worthless portion. However, these techniques have limited utility since at many mines visual or radioactive contrast does not exist and hence, these ores may not be treated economically in this way.
According to the present invention, it has now been found that the desired mineral may be separated from the worthless portion by radiating the ore to cause a portion of it to emit at a characteristic wavelength and sensing the emitted rays. The sensed rays are used to operate means for separating the ore into a desired and an undesired portion. In a preferred embodiment, it has been found that the desired separation may be achieved by first treating a quantity of the ore with a liquid which preferentially coats the particles of one of the portions of the ore and is also capable of emitting at a characteristic wavelength upon exposure to ultraviolet light, X-rays, or other suitable type of electromagnetic radiation. The treated ore is then passed to a separation zone where an electromagnetic wave means sensitive to the characteristic wavelength detects which particles are coated and which particles are not. The sensing means then functions to actuate a deflecting means which physically removes the coated particles from the body of ore particles. Thus, a desired or undesired type of mineral may be removed from the mass of ore.
3,356,2ll Patented Dec. 5, 1967 It is an object of this invention to provide a method for the treatment and concentration of ores.
It is another object of this invention to provide a process of preferentially coating one portion of a mass of ore-bearing rock with a liquid material which, when excited by exposure to electromagnetic radiation, emits radiation of a wavelength distinct from that of the rest of the mass.
It is another object of this invention to pass radiated Ore through a zone where the radiation emitted by the particles is received in an electromagnetic wave-sensitive element and certain of the radiated particles are automatically rejected in accordance with the selective response of the electromagnetic wave-sensitive element to the characteristic emissions therefrom.
These and other objects of this invention will become apparent from the detailed description which follows.
According to this invention, a portion of a body of ore is caused to emit a characteristic wavelength, which wavelength is unlike that emitted by the rest of the ore. The ore particles are then separated according to whether they emit the characeristic wavelength. This is preferably accomplished in the following manner. A quantity of ore containing at least one valuable mineral portion is first treated with a liquid which preferentially coats the particles of one of the minerals in the ore. The coating liquid, in adition to being specific to particles of one of the minerals in the ore, is also capable of fluoroescing at a characteristic Wavelength after exposure to ultraviolet, X-rays, or any other suitable type of radiation. For this reason, the coating liquid is sometimes referred to as the fiuoroscent material. I
The radiation and separation of the ore will be better understood by reference to the accompanying schematic drawing depicting these aspects of the process of this invention. The ore, which in the preferred embodiment has been treated with the fluorescent material to provide both coated and uncoated particles, is placed on a conveyor 1 and caused to drop from the end of conveyor in a downward path past a radiation source 2, into a zone where the characteristic radiation emitted by the radiated particles is received in an electromagnetic wave-sensing means 3. The wave energy received by means 3 produces a small current which is amplified by an amplifier 4. The output of the amplifier then triggers a rectifier switch 5 which, in turn, energizes deflecting means 6, normally a solenoidoperated air jet, water jet, or mechanical gate. The deflecting means knocks the particle emitting at the characteristic wavelength out of the stream of ore particles. These particles are received in collector 7, with the balance of the particles falling into collector 8.
While in the preferred method, a portion of the ore particles is preferentially coated to provide the characteristic emissions upon excitation, the coating may be dispensed with in the case of natural iluorescing ores. These ores, upon excitation, emit at a characteristic wavelength which can be used to activate separation. Typical materials that can be recovered from ore mixtures without coating or other pretreatment are willemite, hydrozincite, uranite, calcite and sheelite. Other ores separated by the technique of this invention are first pretreated to provide a preferential coating capable of emitting at a charactersitic wavelength upon exposure to one of the many forms of electromagnetic radiation.
In this specification, the ore particles which emit at a characteristic wavelength upon excitation will sometimes be referred to as being fluorescent. Likewise, the coating materials used in many cases to provide this property will be referred to as fluorescent materials. In a narrow sense, fluorescence refers to the property of absorbing radiation at one particular Wavelength and re-emitting it as light of a different wavelength so long as the stimulus is active. However, I intend by fluorescence to indicate that property of absorbing radiation at one particular wavelength and re-emitting it as a different wavelength, whether or not visible, during exposure to the active stimulus, or after exposure, or during both of these time periods. Thus, fluorescence is used generically herein to include the limited definitions of both fluorescence and phosphorescence, and envisions the emission of a characteristic wavelength whether or not visible.
In the preferred process, a wire variety of organic materials which fiuoresce at a characteristic wavelength upon excitation by ultraviolet light, X-rays, or other radiation may be used to preferentially coat either the desired or the undesired portion of the ore. Illustrative of these organic fluorescent substances are anthracene, fluorescein, chrysene, aminoacetal picrate, petroleum base lubricating oil, allylamine picrate, aluminum palmitate, ammonium mandelate, calcium triethanolamine theobroinine, ferrous stearate, glyceryl monooleate, glyceryl monostearate, hydrastine, hydrastine chloride, lead naphthenate, lead linoleate, lead stearate, manganous stearate and benzene. Certain of these materials are solids at ordinary temperatures and hence are used in solution. For example, anthracene may be dissolved in benzene.
To assist in adhering the fluorescent substances to the particles to be coated, there may be optionally employed any one of a number of bonding agents, hereinafter referred to as collectors. The collectors are usually long chain molecules with an atomic group which orients on the particle surface and another group which orients on the fluorescent substance. While not bound by any theory, it is believed that the collector is preferentially absorbed on the mineral surface and displaces the water film normally present thereon.
Collectors may be of any one of several types and are generally classified on the basis of their surface attachment into three groups-anionic, cationic and neutral. Anionic collectors usch as xanthates adhere to minerals with a positive surface potential such as metals and sulfides. Cationic collectors usch as amines adhere to surfaces having a negative charge such as silicates. The neutral collectors such as petroleum derivatives adhere to surfaces more positive than the neutral hydrocarbon.
As has been already indicated, the use of a collector is not always require-d. For example, many petroleum base lubricating oils will both preferentially adhere to certain minerals and also fluoresce when excited by electromagnetic radiation. The following list is merely illustrative of some of the anionic collectors which may be employed in this invention: the alkali alkyl xanthates, such as sodium sec-butyl xanthate, potassium ethyl xanthate, sodium ethyl xanthate and potassium amyl xanthate; aryl dithiophosphoric acids such as phenyl dithiophosphoric acid; fatty acids such as stearic acid; thio carbanilide; saponified fatty acids such as sodium stearate and potassium stearate; sulfonated oils; glycerides such as tripalmitin and tristearin; and alcohols.
The cationic collectors include the alkyl ammonium halides such as amyl trimethyl ammonium bromide and cetyl trimethyl ammonium bromide; the alkali metal and alkaline earth metal alkyl aryl sulfonates such as sodium dodecyl benzene sulfonate and calcium dodecyl benzene sulfonate; the alkyl ammonium acetates such as dodecylammonium acetate; long-chain alcohols such as dodecyl alcohol; ethylenically unsaturated monocarboxylic acids and their soaps such as oleic acid, linoleic acid, sodium oleate and sodium linoleate; fatty amine acetates; and benzene.
The fluorescent material and the collector, if present, may be applied to the ore in a variety of ways, including spraying and dipping. In practice, the fluorescent material is added to the collector prior to ore treatment. However, the ore may be treated with the collector and the fluorescent material sequentially. Any excess of the fluorescent material or collector may be readily removed by washing with water.
A fluorescent ore, or the fluorescent material preferentially absorbed on some of the ore particles can be caused to fluoresce at a characteristic wavelength by radiation from the full spectrum of electromagnetic energy, varying from radio waves through infrared, visible, ultraviolet, gamma rays, and ionic bombardment. The specific type of radiation employed in any given situation will depend upon the particular fluorescent material being used. For example, anthracene and petroleum base lubricating oils upon exposure to ultraviolet light (25003700 angstroms) will fluoresce strongly at about 4000 angstroms.
By appropriately selecting the fluorescent material and collector, it is possible to coat almost any mineral in preference to any other material present. Thus, by my invention, any ore portion, whether naturally fluorescent or not, may be readily separated from any other portion. It will, therefore, be recognized that the following examples are presented solely to illustrate the invention and should not be regarded as limitative in any way.
Example I A quantity of crushed ore containing primarily quartz and calcite is coated with a petroleum base lubricating oil (sold by the Standard Oil Co. under the name Penn Motor Oil SAE 30). The excess lubricating oil is removed by flushing with water. Microscopic examination of the particles reveals that the quartz rejects the lubricating oil while coating the calcite. The apparatus used to separate the ore includes a conveyor having an ultraviolet light source stationed at its discharge end. Below the ultraviolet source is positioned a 931-A photo multiplier tube sensitive to 4000 A. emissions. A Wratten filter is interposed in the optical path of the tube to eliminate stray ultraviolet. The output of the tube leads to an amplifier which triggers a silicon controlled rectifier switch which, in turn, energizes a solenoid-operated air jet located below the ultraviolet source. The treated ore is placed on the moving conveyor belt at a rate which provides a single layer of ore particles. The ore particles are exposed to ultraviolet light as they leave the end of the conveyor and'are in free fall. The 4000 A. emissions from the coated particles are sensed by the photo multiplier tube. It is found that the air jet deflector actuated by the tube produces a high degree of separation of the coated calcite from the quartz.
Example II A quantity of crushed ore containing quartz, sandstone, argillite, schist, quartzite and calcite is first washed to remove adhered particles. The ore is then sprayed with an aqueous mixture of dodecylammonium acetate and anthracene dissolved in benzene. The ore is then washed with water to remove the coating solution from the unwanted portions and to leave a coating of anthracene only on the quartz particles. The quartz is then separated from the rest of the ore according to the procedure and employing the apparatus described in Example I.
Example III A quantity of crushed ore containing sulfide minerals, sandstone, argillite, schist and calcite are washed with water to remove adhered particles. The ore is then washed with an aqueous solution of anthracene and phenyl dithiophosphoric acid. The excess is removed by washing with water. It is found that the anthracene preferentially adheres to the surface of the sulfide minerals. The sulfide mineral is then effectively separated from the bulk of the ore in the manner set forth in Example I.
In the practice of the process of this invention, separations of 90% of efficiency have been achieved, using a variety of ores including the following:
Quartz from Quartzite Sandstone Argillite Calcite Mica schist Calcareous schist Hornblend schist Limestone from- Quartz Sandstone Argillite Calcite Mica schist Calcareous schist Hornblend schist As can be seen from the foregoing, the process of this invention is particularly well suited to the concentration of quartz, calcite and limestone-containing ores.
The wave sensing means 3 is typically a photo multiplier tube having a sensitivity to specific wavelength bands. The bands received at the sensing means are narrowed, as required, by the use of filters. Tubes are cornmercially available having sensitivities from the infrared to the ultraviolet. Thus, it is a simple matter to select a tube which is sensitive to the characteristic wavelength emitted upon electromagnetic excitation of any given fluorescent ore or material.
In these photo multiplier tubes, photons which result from fluorescence are received in a first stage and converted to electrons which are deflected to succeeding states by electrostatic fields and multiplied by secondary emission from each stage. The weak current emerging from the photo multiplier tube may be amplified in a conventional solid state amplifier. Since the current from the amplifier is used to operate deflection means 6, it is usually necessary to incorporate an adjustable delay network in the amplifier in order to achieve register between the position of the particle at the time of detection by the sensing means and the time of deflection.
Since the throughput of ore particles in the process of this invention must be as high as possible, the particles are passed before the sensing means at a high velocity. The sensing means is normally placed so that the ore particles passing before it are in free fall and thus have a high velocity and a fixed path.
As can be seen in the drawing, the sensing means is conveniently located so that the sensing means detects the particles soon after they leave the end of the conveyor. To assure a high degree of separation, the ore particles are fed to the conveyor at arate which provides a single layer. While only one sensing means is shown in the drawing, it will be understood that the number of sensing means used is dependent upon the tonnage of ore particles to be handled, the width of the conveyor, and the size of the particles. The field of detection for each sensing means is limited to an area approximately equal to the area of an individual ore particle.
The particular deflecting means 6 chosen has been found to depend on the individual size of the ore particles. An air jet is useful on sizes below /2 inch. A water jet is used on sizes between /2 inch and 4 inches, while a mechanical gate is used for even larger sizes.
While the process of this invention has been described with particular reference to the separation of ore particles while in free fall from the end of a conveyor, it will be evident to anyone skilled in the art that my invention may be practiced in many other ways and with the aid of many different types of apparatus. For example, the particles may be mechanically separated while moving in any desired plane including the horizontal. In the case of small batches, it may be expedient to perform the actual separation manually.
Having fully described the invention, it is intended that it be limited only by the lawful scope of the appended claims.
I claim:
1. The method for the concentration of ore which comprises treating a quantity of crushed ore containing various types of minerals with a liquid fluorescent material capable of preferentially coating some of the particles in the ore, radiating the treated quantity of ore to excite the liquid on the coated particles to fluoresce at a characteristic wavelength, and separating the coated particles from the uncoated particles on the basis of the difference in their emitted wavelengths.
2. The method for the concentration of ore which comprises treating a quantity of crushed ore containing various types of minerals with a liquid fluorescent material capable of preferentially coating some of the particles in the ore, radiating the treated quantity of ore to excite the liquid on the coated particles, passing the radiated treated quantity of ore through a zone where the characteristic wavelength emitted by the radiated coated particles is received in an electromagnetic wavesensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic Wave-sensitive element to the characteristic wavelength received therein.
3. The method for the concentration of calcite-containing ore which comprises treating a quantity of calcitecontaining ore containing various types of minerals with a liquid fluorescent material capable of preferentially coating some of the particles in the ore, radiating the treated quantity of ore to excite the liquid on the coated particles, passing the radiated treated quantity of ore through a zone where the characteristic wavelength emitted by the radiated coated particles is received in an electromagnetic wave-sensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic wavesensitive element to the characteristic wavelength received therein.
4. The method for the concentration of quartz-containing ore which comprises treating a quantity of quartzcontaining ore containing various types of minerals with a liquid fluorescent material capable of preferentially coating some of the particles in the ore, radiating the treated quantity of ore to excite the liquid on the coated particles, passing the radiated treated quantity of ore through a zone where the characteristic wavelength emitted by the radiated coated particles is received in an electromagnetic wave-sensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic wave-sensitive element to the characteristic wavelength received therein.
5. The method for the concentration of sulfide-containing ore which comprises treating a quantity of sulfidecontaining ore containing various types of minerals with a liquid fluorescent material capable of preferentially coating some of the particles in the ore, radiating the treated quantity of ore to excite the liquid on the coated particles, passing the radiated treated quantity of ore through a zone where the characteristic Wavelength emitted by the radiated coated particles is received in an electromagnetic wave-sensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic wavesensitive element to the characteristic wavelength received therein.
6. The method for the concentration of ore which comprises treating a quantity of ore containing various types of minerals with anthracene to preferentially coat some of the particles in the ore, radiating the treated quantity of ore to cause the anthracene on the coated particles to fiuoresce, passing the radiated treated quantity of ore through a zone where the characteristic wavelength emitted by the radiated coated particles is received in an electromagnetic Wave-sensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic wavesensitive element to the characteristic wavelength received therein.
7. The method for the concentration of ore which comprises treating a quantity of ore containing various types of minerals with a petroleum base lubricating oil to preferentially coat some of the particles in the ore, radiating the treated quantity of ore to cause the lubricating oil on the coated particles to fiuoresce, passing the radiated treated quantity of ore through a zone Where the characteristic wavelength emitted by the radiated coated parti- 8 cles is received in an electromagnetic wave-sensitive element, and automatically displacing the coated particles in accordance with the selective response of the electromagnetic wave-sensitive element to the characteristic wavelength received therein.
References Cited UNITED STATES PATENTS 1,577,328 3/1926 Lewis 209 -167 2,096,099 10/1937 Gaugler 250--71 2,267,999 12/19'41 Switzer 250-71 2,717,693 9/1955 Holmes 209-1115 2,878,392 3/1959 Polito 25071 3,011,634 12/1961 Hutter 209111.5 X 3,016,143 1/1962 Trachta 209-167 X 3,061,723 10/1962 Kaptf 250-71 3,118,060 1/1964 Klein 25071 3,255,881 6/1966 Holderreed 209--164 X FRANK W. LUTTER, Primary Examiner.

Claims (1)

1. THE METHOD FOR THE CONCENTRATION OF ORE WHICH COMPRISES TREATING A QUANTITY OF CRUSHED ORE CONTAINING VARIOUS TYPES OF MINERALS WITH A LIQUID FLOURSCENT MATERIAL CAPABLE OF PREFERNTIALLY COATING SOME OF THE PARTCLES IN THE ORE, RADIATING THE TREATED QUANTITY OF ORE TO
US416293A 1964-12-07 1964-12-07 Separation of ore particles preferentially coated with liquid fluorescent material Expired - Lifetime US3356211A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
US416293A US3356211A (en) 1964-12-07 1964-12-07 Separation of ore particles preferentially coated with liquid fluorescent material
GB50118/65A GB1078430A (en) 1964-12-07 1965-11-25 Ore concentration process
DEM67544A DE1237512B (en) 1964-12-07 1965-12-06 Method of sorting ores
SE15736/65A SE311501B (en) 1964-12-07 1965-12-06
OA52273A OA02048A (en) 1964-12-07 1965-12-06 Process of concentrating an ore.
FR41290A FR1475692A (en) 1964-12-07 1965-12-07 Process for the treatment and concentration of poor minerals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US416293A US3356211A (en) 1964-12-07 1964-12-07 Separation of ore particles preferentially coated with liquid fluorescent material

Publications (1)

Publication Number Publication Date
US3356211A true US3356211A (en) 1967-12-05

Family

ID=23649384

Family Applications (1)

Application Number Title Priority Date Filing Date
US416293A Expired - Lifetime US3356211A (en) 1964-12-07 1964-12-07 Separation of ore particles preferentially coated with liquid fluorescent material

Country Status (6)

Country Link
US (1) US3356211A (en)
DE (1) DE1237512B (en)
FR (1) FR1475692A (en)
GB (1) GB1078430A (en)
OA (1) OA02048A (en)
SE (1) SE311501B (en)

Cited By (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3795310A (en) * 1971-11-10 1974-03-05 Rech Geol Minieres Bureau De Process and apparatus for carrying out said process for the preconcentration of ores by induced measure of the superficial contents
US3837582A (en) * 1972-12-27 1974-09-24 Cyprus Mines Corp Beneficiation of new york state talc
US3901793A (en) * 1971-11-10 1975-08-26 Rech Geolog Miniere Process for the preconcentration of ores by induced measure of the superficial contents
US4169045A (en) * 1978-04-19 1979-09-25 Occidental Research Corporation Separation of shale from waste material
WO1979000950A1 (en) * 1978-04-19 1979-11-15 Occidental Res Corp Separation of calcium-containing material from ore
WO1979000952A1 (en) * 1978-04-19 1979-11-15 Occidental Res Corp Separation of coal from waste material
US4207175A (en) * 1978-04-19 1980-06-10 Occidental Research Corporation Separation of magnesite from ores which also contain calcite or dolomite
US4208272A (en) * 1978-04-19 1980-06-17 Occidental Research Corporation Separation of limestone from limestone ore
US4235708A (en) * 1978-04-19 1980-11-25 Occidental Research Corporation Method of separating a mixture of ore particles
FR2455482A1 (en) * 1979-05-04 1980-11-28 Occidental Res Corp Sepg. calcareous components from mineral ores - by conditioning ore particles with coupling agent, pref. carboxylic acid or amine, adding marking agent and sepg.
US4236640A (en) * 1978-12-21 1980-12-02 The Superior Oil Company Separation of nahcolite from oil shale by infrared sorting
US4241102A (en) * 1979-06-04 1980-12-23 Occidental Research Corporation Apparatus and method for the selective wetting of particles
WO1981001530A1 (en) * 1979-12-05 1981-06-11 Occidental Res Corp Process using detectable marking compounds to sort particles
US4326950A (en) * 1978-04-19 1982-04-27 Occidental Research Corporation Process for separating oil shale waste material
US4347125A (en) * 1979-12-05 1982-08-31 Occidental Research Corporation Sorting of ores with detectable compounds
US4352731A (en) * 1980-11-03 1982-10-05 Occidental Research Corporation Apparatus for selective wetting of particles
US4355231A (en) * 1980-08-25 1982-10-19 Suncor Inc. Remote analysis using thermal radiation
US4382515A (en) * 1978-04-19 1983-05-10 Occidental Research Corp. Separation of limestone from limestone ore
US4423814A (en) 1981-06-05 1984-01-03 Occidental Research Corporation Separation or concentration of magnesium-bearing minerals by induced fluorescence
US4462495A (en) * 1979-06-04 1984-07-31 Occidental Research Corporation Process and apparatus for the separation of particles into three fractions of similar compositions
US5024753A (en) * 1989-10-03 1991-06-18 Iowa State University Research Foundation, Inc. Material separation efficiency determination employing fluorescing control particles
US5236092A (en) * 1989-04-03 1993-08-17 Krotkov Mikhail I Method of an apparatus for X-radiation sorting of raw materials
US5303310A (en) * 1991-08-30 1994-04-12 Imc Fertilizer, Inc. Method and apparatus for image analysis of composite ores
US5305895A (en) * 1991-02-13 1994-04-26 Samro-Bystronic Maschinen Ag Method and device for measuring a dimension of a body, and use of said method
US5615778A (en) * 1991-07-29 1997-04-01 Rwe Entsorgung Aktiengesellschaft Process to sort waste mixtures
US20040020831A1 (en) * 2000-09-23 2004-02-05 Peter Meinlschmidt Method and device for determining a temperature distribution of bulk material
WO2005106438A1 (en) * 2004-04-30 2005-11-10 Titech Visionsort As Apparatus and method for inspecting a stream of matter by light scattering inside the matter
EP1647337A1 (en) * 2004-10-18 2006-04-19 M.A.M.I. Modern Allround Management International Apparatus and method for sorting articles
US20060219612A1 (en) * 2005-01-28 2006-10-05 Satake Usa, Inc. Multiport ejector for use with sorter
DE102011007666A1 (en) * 2011-04-19 2012-10-25 Siemens Aktiengesellschaft fluorescence control
US20130345856A1 (en) * 2012-06-25 2013-12-26 International Business Machines Corporation Identification of Plastic Material Composition
US20130341249A1 (en) * 2012-06-25 2013-12-26 International Business Machines Corporation Identification of Plastic Material Composition

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2121535B (en) * 1982-06-02 1986-04-30 Anglo Amer Corp South Africa Detector for use in sorting system
GB8805103D0 (en) * 1988-03-03 1988-03-30 Molins Plc Cigarette manufacture
GB8914363D0 (en) * 1989-06-22 1989-08-09 Bxl Plastics Ltd Waste recovery
DE102014201939A1 (en) * 2014-02-04 2015-08-06 Siemens Aktiengesellschaft Method and device for separating a rock into dead rock and at least one value rock

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1577328A (en) * 1920-07-26 1926-03-16 Minerals Separation North Us Ore concentration
US2096099A (en) * 1935-08-16 1937-10-19 Method of detecting leaks in
US2267999A (en) * 1939-03-20 1941-12-30 Robert C Switzer Magnetic testing
US2717693A (en) * 1949-09-06 1955-09-13 Fred T Holmes Method of and apparatus for sorting radiation emissive material
US2878392A (en) * 1954-12-07 1959-03-17 Gen Electric Method of detecting leaks and testing media therefor
US3011634A (en) * 1958-03-03 1961-12-05 K & H Equipment Ltd Method and apparatus for sorting materials
US3016143A (en) * 1958-12-19 1962-01-09 Int Minerals & Chem Corp Flotation of granular ores
US3061723A (en) * 1959-11-06 1962-10-30 Standard Oil Co Analytical system
US3118060A (en) * 1959-10-16 1964-01-14 Courtaulds Ltd Control of finish on fibrous material by the use of a fluorescing substance
US3255881A (en) * 1961-05-29 1966-06-14 Anaconda Co Flotation process control

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE516130C (en) * 1926-08-14 1931-01-19 Fried Krupp Grusonwerk Akt Ges Process for the management of physically different behaving, individually presented one after the other pieces of material in separate movement paths
AT114673B (en) * 1926-08-14 1929-10-25 Krupp Fried Grusonwerk Ag Process for separating raw mined products.

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1577328A (en) * 1920-07-26 1926-03-16 Minerals Separation North Us Ore concentration
US2096099A (en) * 1935-08-16 1937-10-19 Method of detecting leaks in
US2267999A (en) * 1939-03-20 1941-12-30 Robert C Switzer Magnetic testing
US2717693A (en) * 1949-09-06 1955-09-13 Fred T Holmes Method of and apparatus for sorting radiation emissive material
US2878392A (en) * 1954-12-07 1959-03-17 Gen Electric Method of detecting leaks and testing media therefor
US3011634A (en) * 1958-03-03 1961-12-05 K & H Equipment Ltd Method and apparatus for sorting materials
US3016143A (en) * 1958-12-19 1962-01-09 Int Minerals & Chem Corp Flotation of granular ores
US3118060A (en) * 1959-10-16 1964-01-14 Courtaulds Ltd Control of finish on fibrous material by the use of a fluorescing substance
US3061723A (en) * 1959-11-06 1962-10-30 Standard Oil Co Analytical system
US3255881A (en) * 1961-05-29 1966-06-14 Anaconda Co Flotation process control

Cited By (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3795310A (en) * 1971-11-10 1974-03-05 Rech Geol Minieres Bureau De Process and apparatus for carrying out said process for the preconcentration of ores by induced measure of the superficial contents
US3901793A (en) * 1971-11-10 1975-08-26 Rech Geolog Miniere Process for the preconcentration of ores by induced measure of the superficial contents
US3837582A (en) * 1972-12-27 1974-09-24 Cyprus Mines Corp Beneficiation of new york state talc
US4207175A (en) * 1978-04-19 1980-06-10 Occidental Research Corporation Separation of magnesite from ores which also contain calcite or dolomite
WO1979000950A1 (en) * 1978-04-19 1979-11-15 Occidental Res Corp Separation of calcium-containing material from ore
WO1979000952A1 (en) * 1978-04-19 1979-11-15 Occidental Res Corp Separation of coal from waste material
US4326950A (en) * 1978-04-19 1982-04-27 Occidental Research Corporation Process for separating oil shale waste material
US4208272A (en) * 1978-04-19 1980-06-17 Occidental Research Corporation Separation of limestone from limestone ore
US4208273A (en) * 1978-04-19 1980-06-17 Occidental Research Corporation Separation of coal from waste material
US4235708A (en) * 1978-04-19 1980-11-25 Occidental Research Corporation Method of separating a mixture of ore particles
US4169045A (en) * 1978-04-19 1979-09-25 Occidental Research Corporation Separation of shale from waste material
US4382515A (en) * 1978-04-19 1983-05-10 Occidental Research Corp. Separation of limestone from limestone ore
US4236640A (en) * 1978-12-21 1980-12-02 The Superior Oil Company Separation of nahcolite from oil shale by infrared sorting
FR2455482A1 (en) * 1979-05-04 1980-11-28 Occidental Res Corp Sepg. calcareous components from mineral ores - by conditioning ore particles with coupling agent, pref. carboxylic acid or amine, adding marking agent and sepg.
US4462495A (en) * 1979-06-04 1984-07-31 Occidental Research Corporation Process and apparatus for the separation of particles into three fractions of similar compositions
EP0052681A1 (en) * 1979-06-04 1982-06-02 Occidental Research Corporation Selective wetting of particles
US4241102A (en) * 1979-06-04 1980-12-23 Occidental Research Corporation Apparatus and method for the selective wetting of particles
EP0030802A2 (en) * 1979-12-05 1981-06-24 Occidental Research Corporation Sorting particles
US4347125A (en) * 1979-12-05 1982-08-31 Occidental Research Corporation Sorting of ores with detectable compounds
EP0030802A3 (en) * 1979-12-05 1983-07-20 Occidental Research Corporation Sorting particles
WO1981001530A1 (en) * 1979-12-05 1981-06-11 Occidental Res Corp Process using detectable marking compounds to sort particles
US4355231A (en) * 1980-08-25 1982-10-19 Suncor Inc. Remote analysis using thermal radiation
US4352731A (en) * 1980-11-03 1982-10-05 Occidental Research Corporation Apparatus for selective wetting of particles
US4423814A (en) 1981-06-05 1984-01-03 Occidental Research Corporation Separation or concentration of magnesium-bearing minerals by induced fluorescence
US5236092A (en) * 1989-04-03 1993-08-17 Krotkov Mikhail I Method of an apparatus for X-radiation sorting of raw materials
US5024753A (en) * 1989-10-03 1991-06-18 Iowa State University Research Foundation, Inc. Material separation efficiency determination employing fluorescing control particles
US5305895A (en) * 1991-02-13 1994-04-26 Samro-Bystronic Maschinen Ag Method and device for measuring a dimension of a body, and use of said method
US5615778A (en) * 1991-07-29 1997-04-01 Rwe Entsorgung Aktiengesellschaft Process to sort waste mixtures
US5303310A (en) * 1991-08-30 1994-04-12 Imc Fertilizer, Inc. Method and apparatus for image analysis of composite ores
US20040020831A1 (en) * 2000-09-23 2004-02-05 Peter Meinlschmidt Method and device for determining a temperature distribution of bulk material
WO2005106438A1 (en) * 2004-04-30 2005-11-10 Titech Visionsort As Apparatus and method for inspecting a stream of matter by light scattering inside the matter
JP2007535671A (en) * 2004-04-30 2007-12-06 ティテス ヴィションソルト アクチスカベット Apparatus and method for inspecting material flow by light scattering inside the material
JP4824017B2 (en) * 2004-04-30 2011-11-24 ティテス ヴィションソルト アクチスカベット Apparatus and method for inspecting material flow by light scattering inside the material
EP1647337A1 (en) * 2004-10-18 2006-04-19 M.A.M.I. Modern Allround Management International Apparatus and method for sorting articles
US20060219612A1 (en) * 2005-01-28 2006-10-05 Satake Usa, Inc. Multiport ejector for use with sorter
DE102011007666A1 (en) * 2011-04-19 2012-10-25 Siemens Aktiengesellschaft fluorescence control
US20130345856A1 (en) * 2012-06-25 2013-12-26 International Business Machines Corporation Identification of Plastic Material Composition
US20130341249A1 (en) * 2012-06-25 2013-12-26 International Business Machines Corporation Identification of Plastic Material Composition
US9000318B2 (en) * 2012-06-25 2015-04-07 International Business Machines Corporation Identification of plastic material composition
US9164017B2 (en) * 2012-06-25 2015-10-20 International Business Machines Corporation Identification of plastic material composition
US10413944B2 (en) 2012-06-25 2019-09-17 International Business Machines Corporation Identification of plastic material composition

Also Published As

Publication number Publication date
OA02048A (en) 1970-05-05
SE311501B (en) 1969-06-16
DE1237512B (en) 1967-03-30
GB1078430A (en) 1967-08-09
FR1475692A (en) 1967-04-07

Similar Documents

Publication Publication Date Title
US3356211A (en) Separation of ore particles preferentially coated with liquid fluorescent material
US3472375A (en) Apparatus and method for separating ore
US4423814A (en) Separation or concentration of magnesium-bearing minerals by induced fluorescence
US3346111A (en) Method of rendering asbestos ore particles differentially fluorescent
US4462495A (en) Process and apparatus for the separation of particles into three fractions of similar compositions
KR101722457B1 (en) Sorting device using ultraviolet wavelengths for luminous material
AU2010235964B2 (en) Mineral Separating Means
US4241102A (en) Apparatus and method for the selective wetting of particles
US4208272A (en) Separation of limestone from limestone ore
Poloko Physical separation methods, part 1: A review
US4352731A (en) Apparatus for selective wetting of particles
GB1604419A (en) Mineral exploration
US7852469B1 (en) Particle detector
US4347125A (en) Sorting of ores with detectable compounds
US4208273A (en) Separation of coal from waste material
US4169045A (en) Separation of shale from waste material
RU2733434C1 (en) Electric pulsed crushing-separation method and device
US4207175A (en) Separation of magnesite from ores which also contain calcite or dolomite
JPH10216651A (en) Metal sorting method and metal sorter using the method
US4382515A (en) Separation of limestone from limestone ore
RU2424860C1 (en) Method of separating diamond-containing materials
GB2067753A (en) Method of and apparatus for sorting particulate material
US4326950A (en) Process for separating oil shale waste material
Kolacz New high definition X-ray sorting system based on X-MINE detection technology
CA1121761A (en) Separation of calcium-containing material from ore