Combination of carrier-magnetic-separation and a further separation for mineral processing

US2021316316A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2021316316-A1
Application numberUS-201917268160-A
CountryUS
Kind codeA1
Filing dateAug 6, 2019
Priority dateAug 13, 2018
Publication dateOct 14, 2021
Grant date

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

Official abstract text for this publication.

The present invention relates to a process for concentrating desired particles comprising a carrier-magnetic-separation comprising the following steps a) providing a feedstock which contains the desired particles and an undesired material; b) adding hydrophobic magnetic particles to the feedstock which results in a loaded feedstock containing agglomerates of the magnetic particles and the desired particles or of the magnetic particles and the undesired material; c) separating the agglomerates from the loaded feedstock by a separation method which results in isolated agglomerates, where the separation method is selected from sorting, electric separation, magnetic separation, screening, classification, gravity concentration, and flotation; d) breaking up the isolated agglomerates to obtain a suspension comprising the magnetic particles in desagglomerated form; and e) separating the magnetic particles from the suspension obtained in step d) by a separation method selected from sorting, electric separation, magnetic separation, screening, classification, gravity concentration, and flotation.

First claim

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1 - 18 . (canceled) 19 . A process for concentrating desired particles comprising a carrier-magnetic-separation comprising the following steps, a) providing a feedstock which contains the desired particles and an undesired material; b) adding hydrophobic magnetic particles to the feedstock which results in a loaded feedstock containing agglomerates of the magnetic particles and the desired particles or of the magnetic particles and the undesired material; c) separating the agglomerates from the loaded feedstock by a separation method which results in isolated agglomerates, where the separation method is selected from sorting, electric separation, magnetic separation, screening, classification, gravity concentration, and flotation; d) breaking up the isolated agglomerates to obtain a suspension comprising the magnetic particles in desagglomerated form; and e) separating the magnetic particles from the suspension obtained in step d) by a separation method selected from sorting, electric separation, magnetic separation, screening, classification, gravity concentration, and flotation; and f) optionally re-introducing the magnetic particles obtained in step e) to step b); g) provided that at least one separation method of steps c) or e) is a magnetic separation, and where the process comprises at least one further separation before or after the steps a), b), c), d) or e), and where the further separation is selected from sorting, electric separation, screening, classification, gravity concentration, and flotation. 20 . The process according to claim 19 , wherein the gravity concentration is achieved with jigs, spiral concentrators, shaking tables, centrifugal concentrators, sluices, cones, fluidized bed separators, dense medium separators or elutriators. 21 . The process according to claim 19 , wherein the gravity concentration is achieved with jigs selected from the group consisting of Harz jig, IHC radial jig, in line pressure jig, Denver mineral jig and air-pulsated jig, spiral concentrators selected from the group consisting of Humpreys spiral, souble start and spiral concentrator, shaking tables selected from the group consisting of sand tables, slime tables, Duplex concentrator, and Mozley laboratory separator, centrifugal concentrators selected from the group consisting of Kelsey centrifugal jig, Knelson concentrator, Falcon concentrator and multi-gravity separator, pinched sluiced, Reichert cone, fluidized bed separators selected from the group consisting of, CrossFlow separator, and Reflux Classifier, dense medium separators selected from the group consisting of gravitational vessels like drum separators, Wemco cone separator, Drewboy bath, Norwalt washer; centrifugal separators like dense medium cyclones, water-only cyclones, Vorsyl separator, large coal dense medium separator, Dyna whirlpool separator, and Tri-Flo separator, or elutriators selected from the group consisting of teetered bed separator, Floatex density separator, HydroFloat separator, and allflux separator. 22 . The process according to claim 19 , wherein where the flotation is achieved with mechanical flotation machines, pneumatic flotation machines, hybrid flotation machines, flotation columns, reactor/separator flotation machines, flash flotators, Hydrofloat separator, or Stack cells. 23 . The process according to claim 19 , wherein the sorting is achieved by hand or sensor based sorting, where the sensor type is selected from color in visible light, ultraviolet, gamma radiation, neutron radiation, conductivity, X-ray fluorescence, X-ray luminiscence, infrared, Raman, or microwave attenuation. 24 . The process according to claim 19 , wherein the electric separation is achieved by charging via ion or electron bombardment, conductive induction, or triboelectric charging. 25 . The process according to claim 19 , wherein the magnetic separation is achieved by low-intensity, high-intensity, high-gradient, or superconducting magnetic separators. 26 . The process according to claim 19 , wherein the classification is achieved with centrifugal classifiers or gravitational classifier, such as sedimentation classifier, counter flow classifier, or air classifier. 27 . The process according to claim 19 , wherein the screening is achieved with vibrating screens, static grizzlies, Mogensen Divergators, trommes, bradford breaker, roller screens, flip-flow screen, rotaspiral, Pansep screen, sieve bends, or tumbler screens. 28 . The process according to claim 19 , wherein the separation method in step c) is selected from sorting, electric separation, magnetic separation, screening, classification, gravity concentration, and where in case the further separation is flotation then the flotation is not made in step c) or not between step c) and step d). 29 . The process according to claim 19 , wherein the further separation is made before the step b), in between the step b) and the step d), or after the step d). 30 . The process according to claim 19 , wherein the further separation is selected from gravity concentration, which is made before the agglomeration step b), after the separation step e), or after step b), and optionally the gravity concentration is excluding elutriation. 31 . The process according to claim 19 , wherein the further separation is selected from screening, which is made before the agglomeration step b), after the separation step e) or after step b). 32 . The process according to claim 19 , wherein the further separation is selected from classification, which is made before the agglomeration step b), after the separation step e), or after step b). 33 . The process according to claim 19 , wherein the further separation is selected from sorting and is made before step b). 34 . The process according to claim 19 , wherein the further separation is selected from classification and is made before step b). 35 . The process according to claim 19 , wherein the further separation is made before step a). 36 . The process according to claim 19 , wherein the further separation is selected from sorting and electric separation and is made in dry state before step a).

Assignees

Inventors

Classifications

  • B03C1/30Primary

    Combinations with other devices, not otherwise provided for · CPC title

  • Magnetic separation whereby the particles are suspended in a liquid · CPC title

  • Carrier flotation; Flotation of a carrier material to which the target material attaches · CPC title

  • Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect · CPC title

  • General arrangement of separating plant, e.g. flow sheets · CPC title

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What does patent US2021316316A1 cover?
The present invention relates to a process for concentrating desired particles comprising a carrier-magnetic-separation comprising the following steps a) providing a feedstock which contains the desired particles and an undesired material; b) adding hydrophobic magnetic particles to the feedstock which results in a loaded feedstock containing agglomerates of the magnetic particles and the desir…
Who is the assignee on this patent?
Basf Se
What technology area does this patent fall under?
Primary CPC classification B03C1/30. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Thu Oct 14 2021 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).