EP1778883A4 - PROCESS FOR RECOVERING NICKEL AND COBALT FROM LATERITE ORES BY COMBINATION OF ATMOSPHERIC PRESSURE LIXIVIATION AT MODERATE PRESSURE - Google Patents

PROCESS FOR RECOVERING NICKEL AND COBALT FROM LATERITE ORES BY COMBINATION OF ATMOSPHERIC PRESSURE LIXIVIATION AT MODERATE PRESSURE

Info

Publication number
EP1778883A4
EP1778883A4 EP05761684A EP05761684A EP1778883A4 EP 1778883 A4 EP1778883 A4 EP 1778883A4 EP 05761684 A EP05761684 A EP 05761684A EP 05761684 A EP05761684 A EP 05761684A EP 1778883 A4 EP1778883 A4 EP 1778883A4
Authority
EP
European Patent Office
Prior art keywords
leach
nickel
ore
recited
iron
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.)
Withdrawn
Application number
EP05761684A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP1778883A1 (en
Inventor
David Neudorf
David A Huggins
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.)
SKYE RESOURCES Inc
Original Assignee
SKYE RESOURCES Inc
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 SKYE RESOURCES Inc filed Critical SKYE RESOURCES Inc
Publication of EP1778883A1 publication Critical patent/EP1778883A1/en
Publication of EP1778883A4 publication Critical patent/EP1778883A4/en
Withdrawn legal-status Critical Current

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
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/04Obtaining nickel or cobalt by wet processes
    • C22B23/0407Leaching processes
    • C22B23/0415Leaching processes with acids or salt solutions except ammonium salts solutions
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/04Obtaining nickel or cobalt by wet processes
    • C22B23/0407Leaching processes
    • C22B23/0415Leaching processes with acids or salt solutions except ammonium salts solutions
    • C22B23/043Sulfurated acids or salts thereof
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/04Obtaining nickel or cobalt by wet processes
    • C22B23/0453Treatment or purification of solutions, e.g. obtained by leaching
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/04Obtaining nickel or cobalt by wet processes
    • C22B23/0453Treatment or purification of solutions, e.g. obtained by leaching
    • C22B23/0461Treatment or purification of solutions, e.g. obtained by leaching by chemical methods
    • 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

Definitions

  • U.S. Pat. No. 4,097,575 describes an improvement to the HPAL process which constitutes roasting saprolite ore below about 820 0 C in order to render the ore more reactive with sulfuric acid and then using the roaster calcine to neutralize excess acid in the discharge of an autoclave wherein pressure leaching of limonite ore occurs. Nickel contained in the saprolite ore is largely dissolved during this neutralization.
  • an iron-bearing "seed" material is added to the leach slurry at the start of the saprolite pressure leach stage to accelerate the precipitation of dissolved ferric iron and the extraction of remaining nickel and cobalt from the solid phases.
  • FIG. 2 is a flow sheet showing another embodiment of the process of the present invention in which some of the leach residue is recycled in order to provide seed for iron precipitation.
  • a reductant is added to the limonite leach slurry in order to enhance the dissolution of nickel, and particularly cobalt, from the ore.
  • Most of the cobalt and a smaller proportion of the nickel present in limonite ore is contained typically in a variety of oxidized manganese minerals, referred to collectively as "manganese wad.”
  • Manganese is typically in the tetravalent or trivalent state in these minerals and is refractory to acid leaching unless a reductant is added to cause the manganese to dissolve in the divalent form. The dissolution of manganese is necessary to allow the contained cobalt and nickel to dissolve as well, as will be apparent to those skilled in the art.
  • Suitable reductants include sulfur dioxide (SO 2 ), either as a gas or aqueous solution of SO 2 and ferrous iron, as a soluble salt, e.g. ferrous sulfate, although many other reducing species will also react with oxidized manganese compounds.
  • SO 2 sulfur dioxide
  • ferrous iron as a soluble salt, e.g. ferrous sulfate, although many other reducing species will also react with oxidized manganese compounds.
  • the resulting limonite leach slurry is injected into an autoclave along with the saprolite ore.
  • the saprolite ore typically will be prepared by crushing, grinding and screening or cycloning of the run-of-mine saprolite ore to achieve a particle size that allows the saprolite ore particles to be suspended in the autoclave reactor during the leaching process.
  • the resulting slurry is heated to the desired reaction temperature, for example in the range of 120 to 160 0 C, by any appropriate means, for example by direct injection of intermediate pressure steam into the autoclave, or by direct or indirect steam heating of the leach slurry prior to injection into the autoclave.
  • the autoclave retention time is sufficient to allow most of the iron in solution after the limonite atmospheric leach to hydrolyze and precipitate, and the acid regenerated by iron hydrolysis to react with the saprolite ore, thus extracting most of the contained nickel and cobalt, as well as magnesium and other impurity metals.
  • the saprolite was wet ground to -100 mesh and filtered to produce a filtercake. 262 g (dry basis) of this filtercake was added to the limonite leach slurry, which was then transferred to an autoclave. The autoclave was sealed and heated to 150 0 C, at which temperature leaching was allowed to continue for an additional hour before rapidly cooling the autoclave. The slurry was sampled at the completion of the additional one- hour leach period. The saprolite to limonite ratio was 1.1 and the sulfuric acid addition was 650 kg H 2 SO4 per tonne of ore in this test.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacture And Refinement Of Metals (AREA)
EP05761684A 2004-08-02 2005-06-23 PROCESS FOR RECOVERING NICKEL AND COBALT FROM LATERITE ORES BY COMBINATION OF ATMOSPHERIC PRESSURE LIXIVIATION AT MODERATE PRESSURE Withdrawn EP1778883A4 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US59237504P 2004-08-02 2004-08-02
PCT/CA2005/000988 WO2006029499A1 (en) 2004-08-02 2005-06-23 Method for nickel and cobalt recovery from laterite ores by combination of atmospheric and moderate pressure leaching

Publications (2)

Publication Number Publication Date
EP1778883A1 EP1778883A1 (en) 2007-05-02
EP1778883A4 true EP1778883A4 (en) 2007-08-29

Family

ID=36059658

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05761684A Withdrawn EP1778883A4 (en) 2004-08-02 2005-06-23 PROCESS FOR RECOVERING NICKEL AND COBALT FROM LATERITE ORES BY COMBINATION OF ATMOSPHERIC PRESSURE LIXIVIATION AT MODERATE PRESSURE

Country Status (12)

Country Link
US (1) US20060024224A1 (ja)
EP (1) EP1778883A4 (ja)
JP (1) JP2008508428A (ja)
KR (1) KR20070041770A (ja)
CN (1) CN100402679C (ja)
AU (1) AU2005284620A1 (ja)
BR (1) BRPI0513652A (ja)
CA (1) CA2572420A1 (ja)
GT (1) GT200600110A (ja)
TW (1) TW200607867A (ja)
WO (1) WO2006029499A1 (ja)
ZA (1) ZA200701848B (ja)

Families Citing this family (48)

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WO2007092994A1 (en) * 2006-02-15 2007-08-23 Andreazza Consulting Pty Ltd Processing of laterite ore
EP1994190A4 (en) * 2006-02-24 2010-11-17 Murrin Murrin Operations Pty FILLING HEMATITE AT INCREASED TEMPERATURE AND INCREASED PRESSURE
BRPI0612374B1 (pt) * 2006-11-10 2015-08-11 Vale Sa Processo de recuperação de níquel e cobalto a partir de minérios lateríticos empregando resina de troca iônica e produto contendo níquel ou cobalto
EP2722408A3 (en) * 2007-05-02 2014-07-09 Drinkard Metalox, Inc. A method of recovering metal values from nickel-bearing ores
CN101688267B (zh) * 2007-05-03 2012-12-05 德林卡德.梅塔罗克斯公司 从矿石中回收金属有价物的方法
WO2008138038A1 (en) * 2007-05-14 2008-11-20 Bhp Billiton Ssm Development Pty Ltd LOW Eh LEACH WITH SULFUR RECYCLE
WO2008138039A1 (en) * 2007-05-14 2008-11-20 Bhp Billiton Ssm Development Pty Ltd Nickel recovery from a high ferrous content laterite ore
US20090056502A1 (en) * 2007-08-29 2009-03-05 Vale Inco Limited Hydrometallurgical process for recovery of nickel and cobalt
AP2010005222A0 (en) 2007-09-14 2010-04-30 Barrick Gold Corp Process for recovering platinum group metals usingreductants
JP5143232B2 (ja) * 2007-09-21 2013-02-13 リサーチ インスティチュート オブ インダストリアル サイエンス アンド テクノロジー 石油化学脱硫触媒リサイクル残渣からの鉄ニッケル含有原料及びコバルト含有原料の製造方法、及び鉄ニッケル含有原料を用いたステンレス原料の製造方法、及びフェロニッケルの製造方法
CN101270417B (zh) * 2008-04-30 2010-11-03 江西稀有稀土金属钨业集团有限公司 一种提取镍和/或钴的方法
JP5332418B2 (ja) * 2008-09-04 2013-11-06 住友金属鉱山株式会社 オートクレーブの圧力調整方法
EP2370607A1 (en) * 2008-11-28 2011-10-05 BHP Billiton SSM Development Pty Ltd Process for separating limonite and saprolite
TWI401213B (zh) * 2010-02-02 2013-07-11 廢加氫脫硫觸媒中鎳鈷精礦資源化回收方法
FI123646B (fi) 2010-02-25 2013-08-30 Outotec Oyj Menetelmä kiintoaine-neste-erotuksen tehostamiseksi lateriittien liuotuksen yhteydessä
CN101805828B (zh) * 2010-04-19 2012-01-18 中南大学 一种低成本处理红土镍矿的方法
CN101974685B (zh) * 2010-11-05 2013-02-27 吉林吉恩镍业股份有限公司 用矿浆树脂吸附技术从红土矿中提取镍钴工艺
CN102010993B (zh) * 2010-11-10 2012-07-04 吉林吉恩镍业股份有限公司 用矿浆萃取技术从红土矿中提取镍钴
KR101172897B1 (ko) * 2010-12-13 2012-08-10 재단법인 포항산업과학연구원 니켈 함유 원료로부터 니켈을 회수하는 방법
KR101191042B1 (ko) 2011-12-27 2012-10-15 강호길 니켈정광, 니켈매트로부터 고순도 황산니켈을 제조하는 방법
JP5704410B2 (ja) * 2012-03-21 2015-04-22 住友金属鉱山株式会社 製鉄用ヘマタイトの製造方法
CN102676806A (zh) * 2012-04-18 2012-09-19 赣州腾远钴业有限公司 一种利用二氧化硫还原浸出含钴物料的方法
AU2013256760B2 (en) 2012-05-01 2017-06-01 Dow Global Technologies Llc. Nickel and cobalt recovery using continuous ion exchange
WO2014047672A1 (en) * 2012-09-28 2014-04-03 Direct Nickel Pty Ltd Method for the recovery of metals from nickel bearing ores and concentrates
CN103936080B (zh) * 2013-03-20 2015-10-07 江苏理工学院 一种黄钾铁矾的制备方法
CN103614571A (zh) * 2013-10-09 2014-03-05 北京矿冶研究总院 一种红土镍矿联合浸出的工艺
US10030286B1 (en) 2013-11-13 2018-07-24 Ii-Vi Incorporated Method of direct solvent extraction of rare earth metals from an aqueous acid-leached ore slurry
CN103757261B (zh) * 2013-12-05 2016-07-06 中国科学院过程工程研究所 一种红土镍矿盐酸常压浸出过程铁与镍、钴、硅分离与综合利用的清洁生产方法
CN103757239A (zh) * 2013-12-29 2014-04-30 四川师范大学 镍氢废电池正负极混合材料的浸出方法
CN104630505A (zh) * 2014-12-31 2015-05-20 金川集团股份有限公司 一种通过联合浸出工艺从低品位红土镍矿中回收镍、钴、铁和硅的方法
CN104651609A (zh) * 2014-12-31 2015-05-27 金川集团股份有限公司 一种从红土镍矿中回收镍、钴和铁的方法
CN104611581A (zh) * 2014-12-31 2015-05-13 金川集团股份有限公司 一种从低品位红土镍矿中提取镍的方法
CN104611580A (zh) * 2014-12-31 2015-05-13 金川集团股份有限公司 一种处理低品位红土镍矿的方法
CN104630502A (zh) * 2014-12-31 2015-05-20 金川集团股份有限公司 一种通过联合浸出工艺从褐铁矿中回收镍、钴、铁和硅的方法
CN104611582A (zh) * 2014-12-31 2015-05-13 金川集团股份有限公司 一种通过联合浸出工艺从低品位红土镍矿中回收镍、钴、铁和硅的方法
CN104805283A (zh) * 2014-12-31 2015-07-29 金川集团股份有限公司 常压酸浸和中等压力浸出相结合处理红土镍矿的方法
CN104789766A (zh) * 2014-12-31 2015-07-22 金川集团股份有限公司 通过联合浸出工艺从红土镍矿中回收镍、铁和硅的方法
CN104611579A (zh) * 2014-12-31 2015-05-13 金川集团股份有限公司 一种从低品位红土镍矿中回收镍的方法
US10808296B2 (en) 2015-10-30 2020-10-20 Ii-Vi Delaware, Inc. Selective recovery of rare earth metals from an acidic slurry or acidic solution
US10933410B2 (en) 2015-10-30 2021-03-02 Ii-Vi Delaware, Inc. Composite extractant-enhanced polymer resin, method of making the same, and its usage for extraction of valuable metal(s)
CN106929672B8 (zh) * 2017-04-07 2019-01-11 中南大学 一种利用晶种诱导除铁促进黄铜矿生物浸出的方法
CN107312930B (zh) * 2017-07-07 2018-08-28 金川集团股份有限公司 一种低镍锍硝酸浸出液热解除铁的方法
US11473170B2 (en) 2017-09-25 2022-10-18 Mohammad Asadrokht Treatment of non-sulfidic nickeliferous resources and recovery of metal values therefrom
EP3794164A4 (en) 2018-05-18 2022-03-09 California Institute of Technology PROCESS FOR CONVERTING REDUCED SULFUR SPECIES AND WATER INTO HYDROGEN AND SULFURIC ACID
JP2022544772A (ja) 2019-08-13 2022-10-21 カリフォルニア インスティチュート オブ テクノロジー カルシウム含有岩石および鉱物から酸化カルシウムまたは普通ポルトランドセメントを作製するプロセス
CN111100985B (zh) * 2019-12-30 2021-05-18 荆门市格林美新材料有限公司 一种含钠铵废液应用于红土镍矿的综合处理方法
CN113373315A (zh) * 2021-05-18 2021-09-10 厦门嘉鹭金属工业有限公司 一种高效回收钨渣中钴镍的方法
CN115180661B (zh) * 2022-07-22 2024-02-13 余姚市鑫和电池材料有限公司 一种从铁铝废渣中回收镍钴铜混合硫酸盐的方法

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Also Published As

Publication number Publication date
BRPI0513652A (pt) 2008-05-13
US20060024224A1 (en) 2006-02-02
CN100402679C (zh) 2008-07-16
CN101001964A (zh) 2007-07-18
TW200607867A (en) 2006-03-01
ZA200701848B (en) 2008-04-30
WO2006029499A1 (en) 2006-03-23
GT200600110A (es) 2006-04-26
KR20070041770A (ko) 2007-04-19
EP1778883A1 (en) 2007-05-02
CA2572420A1 (en) 2006-03-23
JP2008508428A (ja) 2008-03-21
AU2005284620A1 (en) 2006-03-23

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