WO2011154540A1 - Nutzung der natürlich vorkommenden magnetischen bestandteile von erzen - Google Patents

Nutzung der natürlich vorkommenden magnetischen bestandteile von erzen Download PDF

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Publication number
WO2011154540A1
WO2011154540A1 PCT/EP2011/059736 EP2011059736W WO2011154540A1 WO 2011154540 A1 WO2011154540 A1 WO 2011154540A1 EP 2011059736 W EP2011059736 W EP 2011059736W WO 2011154540 A1 WO2011154540 A1 WO 2011154540A1
Authority
WO
WIPO (PCT)
Prior art keywords
substance
magnetic particles
magnetic
mixture
group
Prior art date
Application number
PCT/EP2011/059736
Other languages
German (de)
English (en)
French (fr)
Inventor
Alexej Michailovski
Imme Domke
Original Assignee
Basf Se
Siemens Aktiengesellschaft
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=44342917&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO2011154540(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Basf Se, Siemens Aktiengesellschaft filed Critical Basf Se
Priority to PL11724259T priority Critical patent/PL2579987T3/pl
Priority to AU2011263640A priority patent/AU2011263640B2/en
Priority to EP11724259.4A priority patent/EP2579987B1/de
Publication of WO2011154540A1 publication Critical patent/WO2011154540A1/de

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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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C1/00Magnetic separation
    • B03C1/005Pretreatment specially adapted for magnetic separation
    • B03C1/015Pretreatment specially adapted for magnetic separation by chemical treatment imparting magnetic properties to the material to be separated, e.g. roasting, reduction, oxidation
    • 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C1/00Magnetic separation
    • B03C1/005Pretreatment specially adapted for magnetic separation
    • B03C1/01Pretreatment specially adapted for magnetic separation by addition of magnetic adjuvants
    • 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C2201/00Details of magnetic or electrostatic separation
    • B03C2201/18Magnetic separation whereby the particles are suspended in a liquid

Definitions

  • step (B) contacting the mixture containing at least a first substance and at least one second substance from step (A) with magnetic particles so that the at least one first substance and the magnetic particles are deposited,
  • a typically used ore mixture which can be separated by the method according to the invention, has the following composition: about 30% by weight of Si0 2 , about 30% by weight of Na (Si 3 Al) 0 8 , 2% by weight FeCuS 2 , about 0.01 wt .-% MoS 2 , about 1 wt .-% Fe 3 0 4 , balance chromium, iron, titanium and magnesium oxides.
  • dispersants all dispersants are generally suitable in which the mixture to be treated according to the invention is not completely soluble.
  • Suitable dispersants are for example selected from the group consisting of water, water-soluble organic compounds, for example alcohols having 1 to 4 carbon atoms, and mixtures thereof.
  • the dispersant is water.
  • the amount of dispersant may be selected to provide a dispersion which is readily stirrable and / or recoverable.
  • the amount of mixture to be treated based on the total slurry or dispersion, is 10 to 50% by weight, particularly preferably 25 to 40% by weight.
  • the comminution is wet, preferably aqueous, in a ball mill, such. B. in a rotary or stirred ball mill.
  • a grinding medium inert body can serve with 1 to 50 mm in diameter, consisting of metal or preferably of ceramic materials.
  • the hydrophobing is preferably carried out by contacting the comminuted magnetic particles, which are separated in step (A), with a suitable hydrophobing agent, for.
  • a suitable hydrophobing agent for.
  • the hydrophobization can be carried out in an aqueous or organic, preferably aqueous medium.
  • step (B) of the process according to the invention it is generally possible to use all magnetic particles known to those skilled in the art which satisfy the requirements of the process according to the invention, for example dispersibility in the dispersant used and the ability to form sufficiently stable agglomerates with the at least one first substance.
  • the magnetic particles should have a sufficiently high saturation magnetizability, for example 25-300 emu / g, and a low remanence so that the agglomerate can be separated from the dispersion in sufficient quantity in step (C) of the process according to the invention.
  • magnetic particles are used in step (B) of the method according to the invention, selected from the group consisting of magnetic metals, for example iron, Cobalt, nickel and mixtures thereof, ferromagnetic alloys of magnetic metals, magnetic iron oxides such as magnetite (Fe 3 O 4 ), maghemite (Fe 2 O 3 ), pyrrhotite (Fei -x S where 0 ⁇ x ⁇ 0.5), ilmenite (FeTi0 3 ), further minerals of the FeO-Fe 2 0 3 -Ti0 2 system, cubic ferrites of the general formula (I)
  • the size of the magnetic particles used according to the invention is preferably from 10 nm to 1 ⁇ m.
  • the annealing according to step (B) can generally be carried out by any attractive forces known to those skilled in the art between the at least one first material and the magnetic particles.
  • essentially only the at least one first substance and the magnetic particles are deposited in step (B) of the method according to the invention, whereas the at least one second substance and the magnetic particles are essentially not deposited.
  • surface-active substance means a substance which is able to change the surface of the particle to be separated, ie of the at least one first substance, in the presence of the other particles which are not to be separated off,
  • the surface-active substances which can be used according to the invention are selectively attached to the at least one first substance and thereby bring about a suitable hydrophobicity of the first substance.
  • Z is a group with which the compound of the general formula (III) binds to the at least one first material to be separated off.
  • A is preferably a linear or branched, preferably linear, C 6 -C 2 o alkyl.
  • A is preferably a branched C 6 -C 4 -alkyl, wherein the at least one substituent, preferably having 1 to 6 carbon atoms, is preferably present in the 2-position, for example 2-ethylhexyl and / or 2-propylheptyl.
  • step (B) of the process according to the invention preference is given to using at least one hydrophobizing agent according to the general formula (III) shown above. With regard to the preferred embodiments, the above also applies.
  • the at least one water repellent is generally used in an amount sufficient to achieve the desired effect.
  • the at least one hydrophobizing agent is added in an amount of from 0.01 to 5% by weight, based on the at least one first substance present in the mixture.
  • the embodiment B3 of step (B) comprises contacting the adduct of at least a first material and hydrophobing agent with magnetic particles which are functionalized on the surface with at least one polymeric compound having a transition temperature LCST (Lower Critical Solution Temperature).
  • LCST Lower Critical Solution Temperature
  • the magnetic particles are functionalized in the embodiment B3 on the surface with at least one polymeric compound.
  • B is an alkyl radical having 1 to 6 carbon atoms, for example methyl, ethyl, propyl, butyl, for example n-butyl, pentyl, hexyl.
  • the determination of the isoelectric point of the substances present in the mixture can take place via the ⁇ -potential of the individual substances in aqueous solution.
  • the measured ⁇ potential varies with the type of device used, the method of measurement and the evaluation method.
  • Important parameters to be reported are temperature, pH, concentration of the salt background solution, conductivity and measurement voltage, so that the parameters mentioned must be known for comparable measurements.
  • Further details and exemplary isoelectric points of various preferred metal oxides and sulfides are disclosed in WO 2009/065802 A2, the contents of which are expressly referred to.
  • Suitable basic compounds are selected from the group consisting of organic or inorganic bases, for example ammonia, sodium hydroxide NaOH, potassium hydroxide KOH, amines, for example triethylamine, soluble alkali metal carbonates and mixtures thereof.
  • Heteroatoms are, for example, O, S, N, and / or P.
  • Suitable aromatic or heteroaromatic units are, for example, selected from substituted or unsubstituted aromatic or heteroaromatic units having 6 to 20 carbon and optionally heteroatoms, for example phenyl, benzyl and / or naphthyl.
  • the aromatic moieties may be incorporated into the chain via the 1, 2-1, 3- and / or 1-4 positions.
  • step (D) of the method according to the invention is dependent on the method by which the agglomerates have been formed in step (B).
  • suitable organic solvents are methanol, ethanol, propanol, for example n-propanol or isopropanol, aromatic solvents, for example benzene, toluene, xylenes, ethers, for example diethyl ether, methyl t-butyl ether, ketones, for example acetone, aromatic or aliphatic hydrocarbons, for example saturated hydrocarbons having, for example, 8 to 16 carbon atoms, for example dodecane and / or Shellsol®, diesel fuels and mixtures thereof.
  • the main components of the diesel fuel are mainly alkanes, cycloalkanes and aromatic hydrocarbons having about 9 to 22 carbon atoms per molecule and a boiling range between 170 ° C and 390 ° C.
  • step (E) of step (B) of the process according to the invention in which the agglomeration takes place by means of polymeric compounds which have an LCST (Lower Critical Solution Temperature), the agglomerates can be separated in step (E) by setting a temperature in which the polymeric compounds have no hydrophobic character, so that the agglomerates are cleaved.
  • LCST Lower Critical Solution Temperature
  • step (E) separating the magnetic particles from the mixture of step (D) to obtain the at least one first substance.
  • the water can likewise be removed by methods known to the person skilled in the art, for example distillation, filtration, decantation and / or centrifuging.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Magnetic Resonance Imaging Apparatus (AREA)
PCT/EP2011/059736 2010-06-11 2011-06-10 Nutzung der natürlich vorkommenden magnetischen bestandteile von erzen WO2011154540A1 (de)

Priority Applications (3)

Application Number Priority Date Filing Date Title
PL11724259T PL2579987T3 (pl) 2010-06-11 2011-06-10 Zastosowanie naturalnie występujących składników magnetycznych z rud
AU2011263640A AU2011263640B2 (en) 2010-06-11 2011-06-10 Use of the naturally occurring magnetic components of ores
EP11724259.4A EP2579987B1 (de) 2010-06-11 2011-06-10 Nutzung der natürlich vorkommenden magnetischen bestandteile von erzen

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP10165690.8 2010-06-11
EP10165690 2010-06-11

Publications (1)

Publication Number Publication Date
WO2011154540A1 true WO2011154540A1 (de) 2011-12-15

Family

ID=44342917

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2011/059736 WO2011154540A1 (de) 2010-06-11 2011-06-10 Nutzung der natürlich vorkommenden magnetischen bestandteile von erzen

Country Status (6)

Country Link
EP (1) EP2579987B1 (es)
AU (1) AU2011263640B2 (es)
CL (1) CL2012003499A1 (es)
PE (1) PE20131009A1 (es)
PL (1) PL2579987T3 (es)
WO (1) WO2011154540A1 (es)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108440641A (zh) * 2018-02-07 2018-08-24 复旦大学 一种特异性分离富集磷酸化肽和糖基化肽的方法
WO2020035352A1 (en) 2018-08-13 2020-02-20 Basf Se Combination of carrier-magnetic-separation and a further separation for mineral processing
US10799881B2 (en) 2014-11-27 2020-10-13 Basf Se Energy input during agglomeration for magnetic separation
US11998929B2 (en) 2018-08-13 2024-06-04 Basf Se Combination of carrier-magnetic-separation and a further separation for mineral processing

Citations (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB205122A (en) * 1922-04-12 1923-10-12 Alfred Arthur Lockwood Improved process for treating tin ores and concentrates
US3672579A (en) * 1970-08-10 1972-06-27 Univ Minnesota Process for beneficiating magnetite iron ore
US3926789A (en) * 1973-07-05 1975-12-16 Maryland Patent Dev Co Inc Magnetic separation of particular mixtures
US4289528A (en) * 1978-07-03 1981-09-15 Hazen Research, Inc. Process for beneficiating sulfide ores
WO1984004701A1 (en) * 1983-05-21 1984-12-06 British Petroleum Co Plc Beneficiation of carbonaceous fuels
US4657666A (en) 1981-10-26 1987-04-14 W.S.R. Pty. Ltd. Magnetic flotation
US4810368A (en) * 1985-04-10 1989-03-07 Electro Minerals (Canada) Inc. Automatic method for separating and cleaning silicon carbide furnace materials
US4834898A (en) 1988-03-14 1989-05-30 Board Of Control Of Michigan Technological University Reagents for magnetizing nonmagnetic materials
US5051199A (en) 1987-11-17 1991-09-24 Fospur Limited Froth flotation of mineral fines
US5161694A (en) * 1990-04-24 1992-11-10 Virginia Tech Intellectual Properties, Inc. Method for separating fine particles by selective hydrophobic coagulation
US5858060A (en) * 1995-05-04 1999-01-12 Th Engineering France S.A. Magnetic separation method for iron carbide
WO2001037291A1 (en) * 1999-11-17 2001-05-25 Roche Diagnostics Gmbh Magnetic glass particles, method for their preparation and uses thereof
WO2002066168A1 (en) 2001-02-19 2002-08-29 Ausmelt Limited Improvements in or relating to flotation
WO2003049530A2 (en) * 2001-12-07 2003-06-19 Dyax Corporation Method and apparatus for washing magnetically responsive particles
EP1200408B1 (de) 1999-08-03 2003-09-03 STN ATLAS Elektronik GmbH Haftvermittler
WO2007008322A1 (en) 2005-07-06 2007-01-18 Cytec Technology Corp. Process and magnetic reagent for the removal of impurities from minerals
WO2009030669A2 (de) 2007-09-03 2009-03-12 Basf Se Aufbereitung von werterzen durch magnetpartikel
WO2009065802A2 (de) 2007-11-19 2009-05-28 Basf Se Magnetische trennung von substanzen basierend auf ihren unterschiedlichen oberflächenladungen
WO2010007157A1 (de) * 2008-07-18 2010-01-21 Basf Se Anorganische partikel mit einer durch temperatur hydrophil/hydrophob schaltbaren organischen beschichtung

Patent Citations (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB205122A (en) * 1922-04-12 1923-10-12 Alfred Arthur Lockwood Improved process for treating tin ores and concentrates
US3672579A (en) * 1970-08-10 1972-06-27 Univ Minnesota Process for beneficiating magnetite iron ore
US3926789A (en) * 1973-07-05 1975-12-16 Maryland Patent Dev Co Inc Magnetic separation of particular mixtures
US4289528A (en) * 1978-07-03 1981-09-15 Hazen Research, Inc. Process for beneficiating sulfide ores
US4657666A (en) 1981-10-26 1987-04-14 W.S.R. Pty. Ltd. Magnetic flotation
WO1984004701A1 (en) * 1983-05-21 1984-12-06 British Petroleum Co Plc Beneficiation of carbonaceous fuels
US4810368A (en) * 1985-04-10 1989-03-07 Electro Minerals (Canada) Inc. Automatic method for separating and cleaning silicon carbide furnace materials
US5051199A (en) 1987-11-17 1991-09-24 Fospur Limited Froth flotation of mineral fines
US4834898A (en) 1988-03-14 1989-05-30 Board Of Control Of Michigan Technological University Reagents for magnetizing nonmagnetic materials
US5161694A (en) * 1990-04-24 1992-11-10 Virginia Tech Intellectual Properties, Inc. Method for separating fine particles by selective hydrophobic coagulation
US5858060A (en) * 1995-05-04 1999-01-12 Th Engineering France S.A. Magnetic separation method for iron carbide
EP1200408B1 (de) 1999-08-03 2003-09-03 STN ATLAS Elektronik GmbH Haftvermittler
WO2001037291A1 (en) * 1999-11-17 2001-05-25 Roche Diagnostics Gmbh Magnetic glass particles, method for their preparation and uses thereof
WO2002066168A1 (en) 2001-02-19 2002-08-29 Ausmelt Limited Improvements in or relating to flotation
WO2003049530A2 (en) * 2001-12-07 2003-06-19 Dyax Corporation Method and apparatus for washing magnetically responsive particles
WO2007008322A1 (en) 2005-07-06 2007-01-18 Cytec Technology Corp. Process and magnetic reagent for the removal of impurities from minerals
WO2009030669A2 (de) 2007-09-03 2009-03-12 Basf Se Aufbereitung von werterzen durch magnetpartikel
WO2009065802A2 (de) 2007-11-19 2009-05-28 Basf Se Magnetische trennung von substanzen basierend auf ihren unterschiedlichen oberflächenladungen
WO2010007157A1 (de) * 2008-07-18 2010-01-21 Basf Se Anorganische partikel mit einer durch temperatur hydrophil/hydrophob schaltbaren organischen beschichtung

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
CRESPY ET AL., POLYMER INTERNATIONAL, vol. 56, no. 12, 2007, pages 1461 - 1468
LI ET AL., INTERNATIONAL JOURNAL OF PHARMACOLOGY, vol. 2, no. 5, 2006, pages 513 - 519
S. R. GRAY, D. LANDBERG, N. B. GRAY, EXTRACTIVE METALLURGY CONFERENCE, PERTH, vol. 2 - 4, October 1991 (1991-10-01), pages 223 - 226

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10799881B2 (en) 2014-11-27 2020-10-13 Basf Se Energy input during agglomeration for magnetic separation
CN108440641A (zh) * 2018-02-07 2018-08-24 复旦大学 一种特异性分离富集磷酸化肽和糖基化肽的方法
CN108440641B (zh) * 2018-02-07 2021-11-19 复旦大学 一种特异性分离富集磷酸化肽和糖基化肽的方法
WO2020035352A1 (en) 2018-08-13 2020-02-20 Basf Se Combination of carrier-magnetic-separation and a further separation for mineral processing
US11998929B2 (en) 2018-08-13 2024-06-04 Basf Se Combination of carrier-magnetic-separation and a further separation for mineral processing

Also Published As

Publication number Publication date
AU2011263640B2 (en) 2014-02-20
PL2579987T3 (pl) 2020-08-24
PE20131009A1 (es) 2013-09-19
EP2579987B1 (de) 2020-03-18
AU2011263640A1 (en) 2013-01-10
CL2012003499A1 (es) 2013-02-15
EP2579987A1 (de) 2013-04-17

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