FI121713B - Förfarande för upplösning av kalkopyritkoncentrat - Google Patents

Förfarande för upplösning av kalkopyritkoncentrat Download PDF

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Publication number
FI121713B
FI121713B FI20090251A FI20090251A FI121713B FI 121713 B FI121713 B FI 121713B FI 20090251 A FI20090251 A FI 20090251A FI 20090251 A FI20090251 A FI 20090251A FI 121713 B FI121713 B FI 121713B
Authority
FI
Finland
Prior art keywords
solution
concentrate
leaching
copper
zinc
Prior art date
Application number
FI20090251A
Other languages
English (en)
Finnish (fi)
Other versions
FI20090251A0 (sv
FI20090251A (sv
Inventor
Mikko Ruonala
Jaakko Leppinen
Jari Tiihonen
Original Assignee
Outotec Oyj
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 Outotec Oyj filed Critical Outotec Oyj
Publication of FI20090251A0 publication Critical patent/FI20090251A0/sv
Priority to FI20090251A priority Critical patent/FI121713B/sv
Priority to ES10791667.8T priority patent/ES2617148T3/es
Priority to PE2011002167A priority patent/PE20121078A1/es
Priority to AU2010264622A priority patent/AU2010264622B2/en
Priority to CN201080028321.2A priority patent/CN102803524B/zh
Priority to CA2765926A priority patent/CA2765926C/en
Priority to PCT/FI2010/050484 priority patent/WO2010149841A1/en
Priority to EP10791667.8A priority patent/EP2449139B1/en
Priority to BRPI1013501-4A priority patent/BRPI1013501B1/pt
Priority to EA201290017A priority patent/EA023157B1/ru
Priority to MX2011013483A priority patent/MX347485B/es
Priority to US13/380,023 priority patent/US20120103827A1/en
Priority to PL10791667T priority patent/PL2449139T3/pl
Publication of FI20090251A publication Critical patent/FI20090251A/sv
Application granted granted Critical
Publication of FI121713B publication Critical patent/FI121713B/sv
Priority to US13/316,422 priority patent/US20120129063A1/en
Priority to CL2011003269A priority patent/CL2011003269A1/es
Priority to ZA2012/00612A priority patent/ZA201200612B/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • C22B15/0002Preliminary treatment
    • C22B15/0004Preliminary treatment without modification of the copper constituent
    • C22B15/0006Preliminary treatment without modification of the copper constituent by dry processes
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • C22B15/0063Hydrometallurgy
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • C22B15/0063Hydrometallurgy
    • C22B15/0065Leaching or slurrying
    • C22B15/0067Leaching or slurrying with acids or salts thereof
    • C22B15/0071Leaching or slurrying with acids or salts thereof containing sulfur
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/04Extraction of metal compounds from ores or concentrates by wet processes by leaching
    • C22B3/06Extraction of metal compounds from ores or concentrates by wet processes by leaching in inorganic acid solutions, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions
    • C22B3/08Sulfuric acid, other sulfurated acids or salts thereof
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Metallurgy (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Environmental & Geological Engineering (AREA)
  • Geology (AREA)
  • Geochemistry & Mineralogy (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Claims (4)

1. Förfarande för upplösning av kalkopyritkoncentrat med hjälp av en svavelsyrahaltig vattenlösning och syretillförsel under atmosfäriskt 5 tryck och vid temperaturen 75 °C - lösningens kokpunkt, kännetecknat därav, att upplösningen utförs som motströms-upplösning i tvä steg, varvid kalkopyritkoncentratet, vars kornstorlek ligger inom omrädet 80 % under 60 - 100 pm, mätäs tili ett upplösningssteg (1) med utspädd syra, i vilket det upplöses med en 10 lösning (5) som kommer frän ett upplösningssteg (2) med stark syra; aciditeten hos kopparsulfatlösningen (6) som avlägsnas frän upplösningssteget med utspädd syra regleras att vara inom omrädet 5-15 g/l och lösningen leds tili lösningsrening (3) och vidare tili elektrolys (4) för produktion av ren koppar; utfällningen (7) frän 15 upplösningssteget med utspädd syra mätäs tili upplösningssteget (2) med stark syra, väri utfällningen upplöses med ett raffinat (8) frän lösningsreningen, varvid raffinatets aciditet regleras att vara i storleksklassen 20-90 g/l, och väri den lösning (5) som bildas mätäs tili upplösningssteget (1) med utspädd syra. 20
2. Förfarande enligt patentkrav 1, kännetecknat därav, att före upplösningen utförs pä koncentratet en kort renande malning för rengöring av mineralytorna. 25
3. Förfarande enligt patentkrav 1, kännetecknat därav, att kalkopyritkoncentratet är ett bulkkoncentrat, väri ingär zinksulfid.
4. Förfarande enligt patentkrav 1, kännetecknat därav, att lösningens (5) aciditet i upplösningssteget med stark syra regleras att vara i 30 storleksklassen 40-70 g/l.
FI20090251A 2004-10-28 2009-06-26 Förfarande för upplösning av kalkopyritkoncentrat FI121713B (sv)

Priority Applications (16)

Application Number Priority Date Filing Date Title
FI20090251A FI121713B (sv) 2009-06-26 2009-06-26 Förfarande för upplösning av kalkopyritkoncentrat
BRPI1013501-4A BRPI1013501B1 (pt) 2009-06-26 2010-06-10 Method for calcopirite concentrate leaching
MX2011013483A MX347485B (es) 2009-06-26 2010-06-10 Método para la lixiviación de concentrado de calcopirita.
AU2010264622A AU2010264622B2 (en) 2009-06-26 2010-06-10 Method for leaching chalcopyrite concentrate
CN201080028321.2A CN102803524B (zh) 2009-06-26 2010-06-10 黄铜矿精矿的浸取方法
CA2765926A CA2765926C (en) 2009-06-26 2010-06-10 Method for leaching chalcopyrite concentrate
PCT/FI2010/050484 WO2010149841A1 (en) 2009-06-26 2010-06-10 Method for leaching chalcopyrite concentrate
EP10791667.8A EP2449139B1 (en) 2009-06-26 2010-06-10 Method for leaching chalcopyrite concentrate
ES10791667.8T ES2617148T3 (es) 2009-06-26 2010-06-10 Método para lixiviar concentrado de calcopirita
EA201290017A EA023157B1 (ru) 2009-06-26 2010-06-10 Способ выщелачивания халькопиритового концентрата
PE2011002167A PE20121078A1 (es) 2009-06-26 2010-06-10 Metodo para lixiviar un concentrado de calcopirita
US13/380,023 US20120103827A1 (en) 2009-06-26 2010-06-10 Method for leaching chalcopyrite concentration
PL10791667T PL2449139T3 (pl) 2009-06-26 2010-06-10 Sposób ługowania koncentratu chalkopirytu
US13/316,422 US20120129063A1 (en) 2004-10-28 2011-12-09 Flow arrangement for fuel cell stacks
CL2011003269A CL2011003269A1 (es) 2009-06-26 2011-12-22 Método para lixiviar concentrado de calcopirita con solución acuosa de h2so4 que lixivia en contracorriente en dos etapas partículas de concentrado de tamaño 80% bajo 60-100 µm con ácido de concentración de 5-15 g/l, la solución de lixiviación sale de lixiviación con ácido de concentración de 40-70 g/l y forma solución de cu2so4 y lixiviación de residuo con ácido de concentración de 20-90 g/l.
ZA2012/00612A ZA201200612B (en) 2009-06-26 2012-01-25 Method for leaching chalcopyrite concentrate

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20090251 2009-06-26
FI20090251A FI121713B (sv) 2009-06-26 2009-06-26 Förfarande för upplösning av kalkopyritkoncentrat

Publications (3)

Publication Number Publication Date
FI20090251A0 FI20090251A0 (sv) 2009-06-26
FI20090251A FI20090251A (sv) 2010-12-27
FI121713B true FI121713B (sv) 2011-03-15

Family

ID=40825303

Family Applications (1)

Application Number Title Priority Date Filing Date
FI20090251A FI121713B (sv) 2004-10-28 2009-06-26 Förfarande för upplösning av kalkopyritkoncentrat

Country Status (15)

Country Link
US (1) US20120103827A1 (sv)
EP (1) EP2449139B1 (sv)
CN (1) CN102803524B (sv)
AU (1) AU2010264622B2 (sv)
BR (1) BRPI1013501B1 (sv)
CA (1) CA2765926C (sv)
CL (1) CL2011003269A1 (sv)
EA (1) EA023157B1 (sv)
ES (1) ES2617148T3 (sv)
FI (1) FI121713B (sv)
MX (1) MX347485B (sv)
PE (1) PE20121078A1 (sv)
PL (1) PL2449139T3 (sv)
WO (1) WO2010149841A1 (sv)
ZA (1) ZA201200612B (sv)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013068645A1 (en) 2011-11-08 2013-05-16 Outotec Oyj Method for leaching a sulphidic metal concentrate

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20150211092A1 (en) * 2012-11-12 2015-07-30 Flsmidth A/S Method and process for the enhanced leaching of copper sulfide minerals containing chalcopyrite
PE20170111A1 (es) * 2014-06-06 2017-03-11 Soluciones Tecnologicas Mineras Coriolis Ltda Metodo de extraccion de cobre
CN105063351B (zh) * 2015-09-22 2017-10-27 北京矿冶研究总院 一种从复杂钼精矿中选择性分离铜铼的方法
CN108118157B (zh) * 2017-12-30 2019-04-12 北京工业大学 线路板焚烧烟灰预处理及溴的回收方法
WO2020142856A1 (es) * 2019-01-11 2020-07-16 Compañia Minera Pargo Minerals Spa Proceso de obtención de sulfato de cobre pentahidratado
WO2020142855A1 (es) * 2019-01-11 2020-07-16 Compañía Minera Pargo Minerals Spa Planta para la obtención de sulfato de cobre pentahidratato
CN115772607A (zh) * 2022-12-12 2023-03-10 昆明理工大学 一种利用超声强化配位剂高效浸出黄铜矿的方法

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US1857494A (en) * 1925-10-06 1932-05-10 Carson George Campbell Method and means for treating sulphide ores and the production of sulphuric acid thereby
DE895530C (de) * 1942-04-15 1953-11-02 Guaranty Invest Corp Ltd Verfahren zur Verarbeitung von sulfidischen Erzen
US2424866A (en) * 1942-04-15 1947-07-29 Marvin J Udy Process for the treatment of matte to recover metallic salts
US3241950A (en) * 1963-02-13 1966-03-22 Sherritt Gordon Mines Ltd Aqueous acid oxidation of copper bearing mineral sulphides
US3891522A (en) * 1972-02-28 1975-06-24 Cominco Ltd Hydrometallurgical process for treating copper-iron sulphides
US3888748A (en) * 1972-06-28 1975-06-10 Du Pont Recovery of metal values from ore concentrates
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US4256553A (en) * 1980-01-23 1981-03-17 Envirotech Corporation Recovering copper from chalcopyrite concentrate
US5250273A (en) * 1990-01-18 1993-10-05 Canadian Liquid Air Ltd - Air Liquide Canada Ltee Hydrometallurgical leaching process and apparatus
CN1085959A (zh) * 1992-10-22 1994-04-27 云南师范大学 一种氧化铜矿湿法制取氧化铜的方法
AUPN191395A0 (en) * 1995-03-22 1995-04-27 M.I.M. Holdings Limited Atmospheric mineral leaching process
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WO2005118894A1 (en) * 2004-06-03 2005-12-15 The University Of British Columbia Leaching process for copper concentrates
FI118473B (sv) * 2006-02-17 2007-11-30 Outotec Oyj Förfarande för att utvinna koppar ur kopparsulfidmalm

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013068645A1 (en) 2011-11-08 2013-05-16 Outotec Oyj Method for leaching a sulphidic metal concentrate
US9359657B2 (en) 2011-11-08 2016-06-07 Outotec Oyj Method for leaching a sulphidic metal concentrate

Also Published As

Publication number Publication date
CN102803524A (zh) 2012-11-28
BRPI1013501A2 (pt) 2016-04-05
AU2010264622A2 (en) 2012-02-16
PE20121078A1 (es) 2012-08-29
FI20090251A0 (sv) 2009-06-26
CA2765926A1 (en) 2010-12-29
AU2010264622A1 (en) 2012-02-02
EP2449139A1 (en) 2012-05-09
MX2011013483A (es) 2012-01-31
PL2449139T3 (pl) 2017-06-30
ES2617148T3 (es) 2017-06-15
EP2449139B1 (en) 2016-11-23
CL2011003269A1 (es) 2012-07-13
ZA201200612B (en) 2012-10-31
AU2010264622B2 (en) 2013-07-11
EA023157B1 (ru) 2016-04-29
MX347485B (es) 2017-04-28
CA2765926C (en) 2015-11-17
EA201290017A1 (ru) 2012-07-30
CN102803524B (zh) 2015-08-19
BRPI1013501B1 (pt) 2017-12-12
US20120103827A1 (en) 2012-05-03
WO2010149841A1 (en) 2010-12-29
EP2449139A4 (en) 2015-09-23
FI20090251A (sv) 2010-12-27

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