WO2004081241A1 - Improved heap leach - Google Patents
Improved heap leach Download PDFInfo
- Publication number
- WO2004081241A1 WO2004081241A1 PCT/AU2004/000236 AU2004000236W WO2004081241A1 WO 2004081241 A1 WO2004081241 A1 WO 2004081241A1 AU 2004000236 W AU2004000236 W AU 2004000236W WO 2004081241 A1 WO2004081241 A1 WO 2004081241A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- heap
- ore
- elemental sulphur
- sulphur
- addition
- Prior art date
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
- C22B15/00—Obtaining copper
- C22B15/0063—Hydrometallurgy
- C22B15/0065—Leaching or slurrying
- C22B15/0067—Leaching or slurrying with acids or salts thereof
- C22B15/0071—Leaching or slurrying with acids or salts thereof containing sulfur
-
- 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
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/04—Extraction of metal compounds from ores or concentrates by wet processes by leaching
- C22B3/06—Extraction 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
- C22B3/08—Sulfuric acid, other 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
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/18—Extraction of metal compounds from ores or concentrates by wet processes with the aid of microorganisms or enzymes, e.g. bacteria or algae
-
- 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
- the present invention relates to an improved heap leach. More particularly, the improved heap leach of the present invention is directed to the bacterial heap leaching of base metal sulphide ores.
- an improved heap leach process for the bacterial heap leaching of base metal sulphide ores the process characterised by the addition of elemental sulphur to the ore, whereby sulphur oxidising bacteria indigenous to, or added to, the ore may oxidise the elemental sulphur and generate heat within the ore heap.
- the elemental sulphur is either blended with the ore during agglomeration or added to the ore at another point prior to or during stacking of the heap.
- the sulphur may also be added to the top of the ore heap subsequent to stacking, such that the leach liquor is heated as it passes through the layer or level of the heap that is actively oxidising sulphur.
- the blending or addition of elemental sulphur to the ore provides between about 2 to 20% elemental sulphur to ore (w/w).
- an improved heap leach process for the bacterial heap leaching of base metal sulphide ores containing a mineral or an assemblage of minerals that require temperatures of greater than 45°C for efficient oxidation of the or each mineral, the process characterised by the addition of elemental sulphur to the ore, whereby the elemental sulphur is oxidised at temperatures lower than about 45°C by mesophilic bacteria present in the ore heap, this oxidation of elemental sulphur generating heat and raising the internal temperature of the heap upwardly such that thermophilic bacteria can operate.
- chalcopyrite comprises the predominant sulphide mineral in the ore.
- the blending or addition of elemental sulphur to the ore provides between about 2 to 20% elemental sulphur to ore (w/w).
- the addition of elemental sulphur to a process for the bacterial heap leaching of base metal sulphide ores generates sulphuric acid through the oxidation of elemental sulphur, in addition to the generation of heat.
- Figure 1 is a schematic representation of a process for the bacterial heap leaching of base metal sulphide ores in accordance with the present invention.
- FIG. 1 there is shown an improved heap leach process for the bacterial heap leaching of base metal sulphide ores in accordance with the present invention.
- a blending facility 10 is provided for the blending of a base metal sulphide ore containing chalcopyrite as the predominant sulphide mineral and an elemental sulphur.
- the amount of elemental sulphur to be added to the blend is calculated prior to blending so as to be sufficient to satisfy at least part of the heap requirement and/or the acid demand of the ore. Such decisions are typically made by those responsible for management of the heap leaching process.
- water, acid, bacteria, raffinate and other liquor streams associated with the metal recovery portion of an operating hydrometallurgical base metals recovery plant may also be utilised in the process of the present invention, as may additional reagents or chemicals.
- the blended ore and elemental sulphur are then stacked to form a heap 20.
- the heap 20 is fitted with pipes to supply air and/or other gasses to the heap 20.
- an irrigation system (not shown) is provided in or on the heap to allow liquor from a liquor pond 30 to be circulated therebetween.
- a bacteria breeding facility 40 separate to the ore heap 20, is provided such that bacteria can be added to the ore. It is envisaged that the bacteria may be added to the ore prior to, during, or after blending with the elemental sulphur. Alternately, the bacteria may be added to the heap 20, before or after irrigation of the heap 20 has commenced.
- mesophilic bacteria indigenous to the ore heap 20, or added to the ore heap 20 from the bacteria breeding facility 40, will begin the oxidation of elemental sulphur at temperatures of about 20°C, and possibly as low as 10°C.
- the oxidation reaction of elemental sulphur to form sulphate is exothermic, thereby releasing heat into the ore heap 20 and raising the temperature thereof.
- the increased temperature within the heap 20 resulting from the action of the mesophiles on the elemental sulphur increases the temperature within the heap 20 such that thermophilic bacteria begin to operate efficiently and oxidise the chalcopyrite within the ore heap 20. This provides a more efficient bacterial heap leach process with greater recoveries of base metal than might otherwise have been achieved without the addition of elemental sulphur to the ore heap 20.
- blending of the elemental sulphur with the ore may be adequately achieved during agglomeration of the ore or might be added to the ore at another point prior to, or during stacking of the ore heap 20.
- the elemental sulphur might also be added directly to the top of the ore heap 20 subsequent to stacking, whereby the leach liquor would be heated as it passes downwardly thorough the layer of the heap containing the elemental sulphur undergoing oxidation.
- the improved process of the present invention can be seen from the above description to embody several advantages when compared with prior art processes requiring heat generation externally of the ore heap, after which the heat is required to be passed to the heap, or the heating of the ore prior to stacking.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Metallurgy (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Geochemistry & Mineralogy (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Inorganic Chemistry (AREA)
- Biochemistry (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP04713821A EP1620576A4 (en) | 2003-03-12 | 2004-02-24 | Improved heap leach |
AU2004219986A AU2004219986B2 (en) | 2003-03-12 | 2004-02-24 | Improved heap leach |
CA2517693A CA2517693C (en) | 2003-03-12 | 2004-02-24 | Heap leach process using elemental sulphur to generate heat |
US10/548,470 US20060248983A1 (en) | 2003-03-12 | 2004-02-24 | Heap leach |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2003901105A AU2003901105A0 (en) | 2003-03-12 | 2003-03-12 | Improved heap leach |
AU2003901105 | 2003-03-12 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2004081241A1 true WO2004081241A1 (en) | 2004-09-23 |
Family
ID=31500149
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/AU2004/000236 WO2004081241A1 (en) | 2003-03-12 | 2004-02-24 | Improved heap leach |
Country Status (9)
Country | Link |
---|---|
US (1) | US20060248983A1 (en) |
EP (1) | EP1620576A4 (en) |
CN (1) | CN1320138C (en) |
AR (1) | AR043514A1 (en) |
AU (1) | AU2003901105A0 (en) |
CA (1) | CA2517693C (en) |
PE (1) | PE20050303A1 (en) |
WO (1) | WO2004081241A1 (en) |
ZA (1) | ZA200506897B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008054648A2 (en) * | 2006-10-18 | 2008-05-08 | Earth Based Solutions, Llp | Method for producing sulfuric acid |
WO2009059336A1 (en) | 2007-10-31 | 2009-05-07 | Bhp Billiton Sa Limited | High temperature leaching process |
US8119085B2 (en) | 2005-03-21 | 2012-02-21 | Bioheap Limited | Heap leaching of sulphide ores |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CL2011001440A1 (en) * | 2010-06-15 | 2011-10-28 | Teck Resources Ltd | Process for recovering copper from heap leaching rubble, which comprises mixing said rubble with a material to form a mixture or agglomerating the rubble of the leaching into batteries, and leaching the pile of the rubble treated of the leaching into batteries with a solution of leaching. |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998007892A1 (en) * | 1996-06-12 | 1998-02-26 | Yes Technologies | Method and apparatus for biocatalyzed anaerobic oxidation of metal sulfides |
WO2001036693A2 (en) * | 1999-11-17 | 2001-05-25 | Bhp Minerals International, Inc. | Recovery of metals from ore by bioleaching with sulfur addition |
CN1310239A (en) * | 2000-02-22 | 2001-08-29 | 中国科学院化工冶金研究所 | Microbe leaching-out method of valuable metals from deep-sea polymetal nodule |
US20020157504A1 (en) * | 1999-12-14 | 2002-10-31 | Alexander Beckmann | Sulfidization of sulfide ores for hydrometallurgical extraction of copper and other metals |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4497778A (en) * | 1981-04-06 | 1985-02-05 | University College Cardiff Consultants Limited | Microbial leaching of sulphide-containing ores |
US4729788A (en) * | 1987-01-23 | 1988-03-08 | Advanced Mineral Technologies, Inc. | Thermophilic microbial treatment of precious metal ores |
AUPP444298A0 (en) * | 1998-07-01 | 1998-07-23 | Bactech (Australia) Pty Limited | Leaching of low sulphur ores |
DE19835291A1 (en) * | 1998-08-05 | 2000-02-10 | Herberts Gmbh | Plastic container for storing liquid coating agents |
US6110253A (en) * | 1998-12-14 | 2000-08-29 | Geobiotics, Inc. | High temperature heap bioleaching process |
AU2843500A (en) * | 1998-12-15 | 2000-07-03 | Electric Fuel Limited | Structure for a prism-shaped metal-air battery cell with features to prevent electrolyte leakage and to maintain connectivity between an air cathode and a casing element |
US6245125B1 (en) * | 1999-09-15 | 2001-06-12 | Billiton S.A. Limited | Copper, nickel and cobalt recovery |
-
2003
- 2003-03-12 AU AU2003901105A patent/AU2003901105A0/en not_active Abandoned
-
2004
- 2004-02-24 US US10/548,470 patent/US20060248983A1/en not_active Abandoned
- 2004-02-24 EP EP04713821A patent/EP1620576A4/en not_active Withdrawn
- 2004-02-24 CA CA2517693A patent/CA2517693C/en not_active Expired - Lifetime
- 2004-02-24 WO PCT/AU2004/000236 patent/WO2004081241A1/en active Application Filing
- 2004-02-24 CN CNB2004800065903A patent/CN1320138C/en not_active Expired - Fee Related
- 2004-03-08 PE PE2004000247A patent/PE20050303A1/en not_active Application Discontinuation
- 2004-03-09 AR ARP040100744A patent/AR043514A1/en not_active Application Discontinuation
-
2005
- 2005-08-29 ZA ZA200506897A patent/ZA200506897B/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998007892A1 (en) * | 1996-06-12 | 1998-02-26 | Yes Technologies | Method and apparatus for biocatalyzed anaerobic oxidation of metal sulfides |
WO2001036693A2 (en) * | 1999-11-17 | 2001-05-25 | Bhp Minerals International, Inc. | Recovery of metals from ore by bioleaching with sulfur addition |
US20020157504A1 (en) * | 1999-12-14 | 2002-10-31 | Alexander Beckmann | Sulfidization of sulfide ores for hydrometallurgical extraction of copper and other metals |
CN1310239A (en) * | 2000-02-22 | 2001-08-29 | 中国科学院化工冶金研究所 | Microbe leaching-out method of valuable metals from deep-sea polymetal nodule |
Non-Patent Citations (2)
Title |
---|
DATABASE WPI Week 200205, Derwent World Patents Index; Class D16, AN 2002-034952, XP008094203, INST CHEM METALLURGY ACAD SINICA * |
See also references of EP1620576A4 * |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8119085B2 (en) | 2005-03-21 | 2012-02-21 | Bioheap Limited | Heap leaching of sulphide ores |
WO2008054648A2 (en) * | 2006-10-18 | 2008-05-08 | Earth Based Solutions, Llp | Method for producing sulfuric acid |
WO2008054648A3 (en) * | 2006-10-18 | 2008-10-23 | Earth Based Solutions Llp | Method for producing sulfuric acid |
WO2009059336A1 (en) | 2007-10-31 | 2009-05-07 | Bhp Billiton Sa Limited | High temperature leaching process |
CN101855374A (en) * | 2007-10-31 | 2010-10-06 | Bhp比尔顿有限公司 | High temperature leaching process |
US8268038B2 (en) | 2007-10-31 | 2012-09-18 | Bhp Billiton Sa Limited | High temperature leaching process |
EA017998B1 (en) * | 2007-10-31 | 2013-04-30 | Би Эйч Пи Биллитон Са Лимитед | High temperature leaching process |
CN101855374B (en) * | 2007-10-31 | 2014-01-29 | Bhp比尔顿有限公司 | High temperature leaching process |
AP2861A (en) * | 2007-10-31 | 2014-03-31 | Bhp Billiton Sa Ltd | High temperature leaching process |
Also Published As
Publication number | Publication date |
---|---|
EP1620576A1 (en) | 2006-02-01 |
CA2517693A1 (en) | 2004-09-23 |
PE20050303A1 (en) | 2005-07-08 |
CN1320138C (en) | 2007-06-06 |
CA2517693C (en) | 2012-08-14 |
CN1759193A (en) | 2006-04-12 |
US20060248983A1 (en) | 2006-11-09 |
AR043514A1 (en) | 2005-08-03 |
ZA200506897B (en) | 2007-02-28 |
EP1620576A4 (en) | 2008-05-21 |
AU2003901105A0 (en) | 2003-03-27 |
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