EP2525915B1 - Flotationsreagenz für magnetit- und/oder hämatithaltige eisenerze - Google Patents

Flotationsreagenz für magnetit- und/oder hämatithaltige eisenerze Download PDF

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Publication number
EP2525915B1
EP2525915B1 EP11700151.1A EP11700151A EP2525915B1 EP 2525915 B1 EP2525915 B1 EP 2525915B1 EP 11700151 A EP11700151 A EP 11700151A EP 2525915 B1 EP2525915 B1 EP 2525915B1
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EP
European Patent Office
Prior art keywords
carbon atoms
group
radical
independently
another
Prior art date
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Application number
EP11700151.1A
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German (de)
English (en)
French (fr)
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EP2525915A1 (de
Inventor
Klaus-Ulrich Pedain
Uwe Dahlmann
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Clariant International Ltd
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Clariant Finance BVI Ltd
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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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/004Organic compounds
    • B03D1/01Organic compounds containing nitrogen
    • 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/004Organic compounds
    • B03D1/0043Organic compounds modified so as to contain a polyether group
    • 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/02Froth-flotation processes
    • 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2201/00Specified effects produced by the flotation agents
    • B03D2201/02Collectors
    • 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2203/00Specified materials treated by the flotation agents; Specified applications
    • B03D2203/02Ores
    • B03D2203/04Non-sulfide ores

Definitions

  • the present invention relates to the use of collectors in the flotation of iron ore containing magnetite and / or hematite.
  • silicates are naturally occurring ores and minerals.
  • these include calcite, phosphate ore and feldspar.
  • the silicate content reduces the quality of the iron ore and interferes with iron production.
  • the iron ore is separated from the silicate in addition to the magnetic separation by inverse flotation.
  • the ground iron ore is brought together in a flotation cell with water and flotation reagents, wherein the silicate is discharged through the use of a collector with the foam, while the iron ore remains back in the so-called pulp.
  • fatty amines alkyl ether amines and alkyl ether diamines are used as silicate collectors. These are known under the trade name Flotigam ®.
  • Alkyl ether amines and alkyl ether diamines are mostly used in their partially neutralized forms as partial acetates as in U.S. 4,319,987 described. The reason for this is their better solubility in the pulp.
  • the silicate flotation, including iron ore, with the help of Alkyloxyalkanaminen is in U.S. 5,540,337 described.
  • DE-A-10 2006 010 939 discloses the use of a compound of formula (I) R 1 -OR 2 -NH (2-m) - [(R 3 ) n -H] m (I) wherein R 1 is a hydrocarbon group having 1 to 40 carbon atoms, R 2 is an aliphatic hydrocarbon group having 2 to 4 carbon atoms and R 3 is an alkoxy group, n is a number between 1 and 50 and m is 1 or 2, as a flotation reagent in the silicate flotation.
  • iron ore float collectors known in the prior art have insufficient selectivity and yield, especially when iron ores containing magnetite and / or hematite are to be separated from silicates as an accompanying mineral.
  • the ratio of the collector components A: B is preferably between 98: 2 and 2:98 by weight, in particular between 70:30 and 30:70 by weight.
  • the collector according to the invention is free of quaternary ammonium compounds which comprise at least one organic radical containing 8 to 36 carbon atoms and bound to the ammonium nitrogen atom, optionally containing heteroatoms.
  • a quaternary ammonium compound is meant a compound which does not carry a hydrogen atom on the ammonium nitrogen atom but in which the ammonium nitrogen atom is bonded to four carbon atoms.
  • This particularly preferred embodiment is thus not to be understood as the embodiment in which either the compound of the formula 1 or the compound B) of the formula D-NH 2 or both are present as mono- or diammonium salts.
  • These mono- or diammonium salts carry at least one hydrogen atom on the ammonium nitrogen atom.
  • component B) can be used as a salt, for example as an acetate.
  • Component B) of the collector according to the invention is preferably one or more of the compounds of the formulas (II) to (IV). These connections are R 9 -OR 5 -NH 2 (II) wherein R 9 corresponds to a hydrocarbon group of 1-40, preferably 8 to 32 carbon atoms and R 5 corresponds to an aliphatic hydrocarbon group of 2 to 4 carbon atoms; R 6 -OR 7 -NH-R 8 -NH 2 (III) wherein R 6 corresponds to a hydrocarbon group of 1-40, preferably 8 to 32 carbon atoms, R 7 and R 8 correspond to one or more aliphatic hydrocarbon group having 2 to 4 carbon atoms; R 13 -NH 2 (IV) wherein R 13 corresponds to a hydrocarbon group having 1-40, preferably 8 to 32 carbon atoms.
  • R 1 preferably represents a linear or branched alkyl or alkenyl group comprising 10 to 22 carbon atoms. Particularly preferred for R 1 are isodecyl isotridecyl, dodecyl, Cocosfettalkyl- and Talgfettalkylreste.
  • R 1 in a preferred embodiment represents an alkyl and alkenyl chain cut derived from coconut oil fatty acid, palm oil fatty acid, tallow fatty acid, oleic acid, tall oil fatty acid or rapeseed oil fatty acid.
  • R 2 , R 3 , R 4 are independently acyl radicals having 8 to 24 carbon atoms.
  • the acyl radicals preferably comprise 10 to 18 carbon atoms. They can be linear or branched.
  • the acyl radicals can be saturated or unsaturated.
  • Preferred acyl radicals are stearoyl and oleoyl radicals.
  • R 6 , R 9 , R 13 independently of one another preferably represent a linear or branched alkyl or alkenyl group having 8 to 18 carbon atoms. Particularly preferred for R 6 , R 9 , R 13 are 2-ethylhexyl, isononyl, isodecyl and Isotridecyl- and dodecyl.
  • R 5 , R 7 , R 8 independently of one another preferably represent alkylene groups having 2, 3 or 4 carbon atoms, in particular ethylene or propylene groups.
  • A is in particular either an ethylene - (- C 2 H 4 -), a propylene - (- C 3 H 6 -) or a butylene group (-C 4 H 8 -).
  • A is an ethylene group.
  • B is in particular either an ethylene - (- C 2 H 4 -), a propylene - (- C 3 H 6 -) or a butylene group (-C 4 H 8 -).
  • B is an isopropylene group.
  • x, y and z preferably give an integer of 15 to 30, in particular 20 to 25.
  • the aminoalkoxylate ester constituting component A) is in the form of its mono- or di-ammonium salts obtained by neutralization with both organic and mineral acids.
  • the use of the flotation reagent according to the invention can also be carried out in combination with foaming agents and pushers, as known from the prior art.
  • foaming agents and pushers as known from the prior art.
  • hydrophilic polysaccharides such as modified starch, carboxymethylcellulose, or gum arabic are added in dosages of 10 to 1,000 g / t as pushers.
  • the silicate flotation is preferably carried out at a pH of 7-12, in particular 8-11, which is for example adjusted with sodium hydroxide.
  • the following table represents the flotative results of the inventive collector compared to the standard reagent. Flotation experiments were carried out on an iron ore containing magnetite and hematite. A) Composition of iron ore lodestone 59% by weight hematite 25% by weight (other components) 16% by weight B) Composition of the collector
  • the content of Fe in the concentrate was determined analytically.

Landscapes

  • Compounds Of Iron (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
EP11700151.1A 2010-01-19 2011-01-04 Flotationsreagenz für magnetit- und/oder hämatithaltige eisenerze Active EP2525915B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102010004893A DE102010004893A1 (de) 2010-01-19 2010-01-19 Flotationsreagenz für magnetit- und/oder hämatithaltige Eisenerze
PCT/EP2011/000007 WO2011088963A1 (de) 2010-01-19 2011-01-04 Flotationsreagenz für magnetit- und/oder hämatithaltige eisenerze

Publications (2)

Publication Number Publication Date
EP2525915A1 EP2525915A1 (de) 2012-11-28
EP2525915B1 true EP2525915B1 (de) 2015-07-08

Family

ID=43828316

Family Applications (1)

Application Number Title Priority Date Filing Date
EP11700151.1A Active EP2525915B1 (de) 2010-01-19 2011-01-04 Flotationsreagenz für magnetit- und/oder hämatithaltige eisenerze

Country Status (14)

Country Link
US (1) US8939291B2 (pt)
EP (1) EP2525915B1 (pt)
CN (1) CN102770213B (pt)
AU (1) AU2011208902B2 (pt)
BR (1) BR112012017237B1 (pt)
CA (1) CA2787445C (pt)
CL (1) CL2012002001A1 (pt)
DE (1) DE102010004893A1 (pt)
DK (1) DK2525915T3 (pt)
ES (1) ES2542746T3 (pt)
RU (1) RU2562284C2 (pt)
UA (1) UA106784C2 (pt)
WO (1) WO2011088963A1 (pt)
ZA (1) ZA201202694B (pt)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104307640B (zh) * 2014-11-07 2016-08-17 中蓝连海设计研究院 一种磷矿反浮选方解石的捕收剂
CN104646186A (zh) * 2015-01-30 2015-05-27 武汉理工大学 一种三酯基季铵盐阳离子捕收剂及其制备方法和应用
US20190314828A1 (en) 2016-07-08 2019-10-17 Akzo Nobel Chemicals International B.V. Process to treat magnetite ore and collector composition
CN106179765B (zh) * 2016-07-27 2018-12-28 湖北富邦科技股份有限公司 一种提磷降镁率高的磷矿反浮选捕收剂及制备方法
CN106492998B (zh) * 2016-11-02 2018-11-20 广西大学 一种赤铁矿捕收剂的制备方法
CN112808463B (zh) * 2020-12-30 2022-06-21 中南大学 一种将铁钛矿与含铁脉石浮选分离的药剂和方法

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2389763A (en) 1941-04-24 1945-11-27 Emulsol Corp Separation of mineral values from ores
US3363758A (en) * 1966-12-08 1968-01-16 Ashland Oil Inc Use of primary aliphatic ether amine acid salts in froth flotation process
US4319987A (en) 1980-09-09 1982-03-16 Exxon Research & Engineering Co. Branched alkyl ether amines as iron ore flotation aids
SU1090449A1 (ru) * 1983-02-08 1984-05-07 Институт минеральных ресурсов Способ обогащени железных руд
SU1269846A1 (ru) * 1985-07-25 1986-11-15 Институт Органической Химии Ан Усср Способ обогащени железных руд
DE4133063A1 (de) * 1991-10-04 1993-04-08 Henkel Kgaa Verfahren zur herstellung von eisenerzkonzentraten durch flotation
US5540337A (en) 1994-04-04 1996-07-30 Baker Hughes Incorporated Alkyloxyalkaneamines useful as cationic froth flotation collectors
DE19602856A1 (de) * 1996-01-26 1997-07-31 Henkel Kgaa Biologisch abbaubare Esterquats als Flotationshilfsmittel
SE521949C2 (sv) 1997-11-27 2003-12-23 Akzo Nobel Nv Förfarande för skumflotation av silikatinnehållande järnmalm
SE514435C2 (sv) 1999-04-20 2001-02-26 Akzo Nobel Nv Kvartära ammoniumföreningar för skumflotation av silikater från järnmalm
DE102006010939A1 (de) 2006-03-09 2007-09-13 Clariant International Limited Flotationsreagenz für Silikate
DE102006019561A1 (de) * 2006-04-27 2007-10-31 Clariant International Limited Flotationsreagenz für silikathaltige Mineralien
RU2365425C2 (ru) * 2007-04-04 2009-08-27 Совместное предприятие в форме закрытого акционерного общества "Изготовление, внедрение, сервис" Способ флотационной доводки магнетитовых концентратов
RU2467804C2 (ru) * 2007-06-12 2012-11-27 Акцо Нобель Н.В. Коллектор для флотации глинистых минералов из калийных руд

Also Published As

Publication number Publication date
BR112012017237A2 (pt) 2016-03-22
AU2011208902B2 (en) 2015-12-03
AU2011208902A1 (en) 2012-05-03
RU2562284C2 (ru) 2015-09-10
CA2787445A1 (en) 2011-07-28
WO2011088963A1 (de) 2011-07-28
BR112012017237B1 (pt) 2019-11-19
CA2787445C (en) 2017-08-29
CL2012002001A1 (es) 2013-01-11
RU2012135550A (ru) 2014-02-27
DK2525915T3 (en) 2015-09-14
CN102770213A (zh) 2012-11-07
US8939291B2 (en) 2015-01-27
ZA201202694B (en) 2013-02-27
UA106784C2 (uk) 2014-10-10
US20120325725A1 (en) 2012-12-27
DE102010004893A1 (de) 2011-07-21
EP2525915A1 (de) 2012-11-28
ES2542746T3 (es) 2015-08-11
CN102770213B (zh) 2014-04-02

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