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 PRESSUREInfo
- 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- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B23/00—Obtaining nickel or cobalt
- C22B23/04—Obtaining nickel or cobalt by wet processes
- C22B23/0407—Leaching processes
- C22B23/0415—Leaching processes with acids or salt solutions except ammonium salts solutions
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B23/00—Obtaining nickel or cobalt
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B23/00—Obtaining nickel or cobalt
- C22B23/04—Obtaining nickel or cobalt by wet processes
- C22B23/0407—Leaching processes
- C22B23/0415—Leaching processes with acids or salt solutions except ammonium salts solutions
- C22B23/043—Sulfurated acids or salts thereof
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B23/00—Obtaining nickel or cobalt
- C22B23/04—Obtaining nickel or cobalt by wet processes
- C22B23/0453—Treatment or purification of solutions, e.g. obtained by leaching
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B23/00—Obtaining nickel or cobalt
- C22B23/04—Obtaining nickel or cobalt by wet processes
- C22B23/0453—Treatment or purification of solutions, e.g. obtained by leaching
- C22B23/0461—Treatment or purification of solutions, e.g. obtained by leaching by chemical methods
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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)
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 |
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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 |
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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 |
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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 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3804613A (en) * | 1971-09-16 | 1974-04-16 | American Metal Climax Inc | Ore conditioning process for the efficient recovery of nickel from relatively high magnesium containing oxidic nickel ores |
US6379636B2 (en) * | 1999-11-03 | 2002-04-30 | Bhp Minerals International, Inc. | Method for leaching nickeliferous laterite ores |
WO2003093517A1 (en) * | 2002-04-29 | 2003-11-13 | Qni Technology Pty Ltd | Atmospheric pressure leach process for lateritic nickel ore |
US6680035B2 (en) * | 1999-11-03 | 2004-01-20 | Bhp Minerals International Inc. | Atmospheric leach process for the recovery of nickel and cobalt from limonite and saprolite ores |
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US3772422A (en) * | 1971-09-07 | 1973-11-13 | M Taylor | Process for the selective recovery of chromium from chromium containing materials and solutions |
US3793432A (en) * | 1972-01-27 | 1974-02-19 | D Weston | Hydrometallurgical treatment of nickel group ores |
US4097575A (en) * | 1976-11-05 | 1978-06-27 | Amax Inc. | Roast-neutralization-leach technique for the treatment of laterite ore |
US4548794A (en) * | 1983-07-22 | 1985-10-22 | California Nickel Corporation | Method of recovering nickel from laterite ores |
US5571308A (en) * | 1995-07-17 | 1996-11-05 | Bhp Minerals International Inc. | Method for recovering nickel from high magnesium-containing Ni-Fe-Mg lateritic ore |
-
2005
- 2005-06-23 AU AU2005284620A patent/AU2005284620A1/en not_active Abandoned
- 2005-06-23 BR BRPI0513652-0A patent/BRPI0513652A/pt not_active IP Right Cessation
- 2005-06-23 CA CA002572420A patent/CA2572420A1/en not_active Abandoned
- 2005-06-23 KR KR1020077005105A patent/KR20070041770A/ko not_active Application Discontinuation
- 2005-06-23 JP JP2007524144A patent/JP2008508428A/ja active Pending
- 2005-06-23 CN CNB2005800262605A patent/CN100402679C/zh not_active Expired - Fee Related
- 2005-06-23 EP EP05761684A patent/EP1778883A4/en not_active Withdrawn
- 2005-06-23 WO PCT/CA2005/000988 patent/WO2006029499A1/en active Application Filing
- 2005-06-24 US US11/165,362 patent/US20060024224A1/en not_active Abandoned
- 2005-07-22 TW TW094124881A patent/TW200607867A/zh unknown
-
2006
- 2006-03-10 GT GT200600110A patent/GT200600110A/es unknown
-
2007
- 2007-03-02 ZA ZA200701848A patent/ZA200701848B/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3804613A (en) * | 1971-09-16 | 1974-04-16 | American Metal Climax Inc | Ore conditioning process for the efficient recovery of nickel from relatively high magnesium containing oxidic nickel ores |
US6379636B2 (en) * | 1999-11-03 | 2002-04-30 | Bhp Minerals International, Inc. | Method for leaching nickeliferous laterite ores |
US6680035B2 (en) * | 1999-11-03 | 2004-01-20 | Bhp Minerals International Inc. | Atmospheric leach process for the recovery of nickel and cobalt from limonite and saprolite ores |
WO2003093517A1 (en) * | 2002-04-29 | 2003-11-13 | Qni Technology Pty Ltd | Atmospheric pressure leach process for lateritic nickel ore |
Non-Patent Citations (1)
Title |
---|
BOLT J.R. JR.: "The Winning of Nickel, its Geology, Mining, and Extractive Metallurgy", 1967, LONGMANS CANADA LTD. * |
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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