WO2004081241A1 - Improved heap leach - Google Patents

Improved heap leach Download PDF

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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
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WO
WIPO (PCT)
Prior art keywords
heap
ore
elemental sulphur
sulphur
addition
Prior art date
Application number
PCT/AU2004/000236
Other languages
French (fr)
Inventor
Tamsin Lisa Williams
Colin John Hunger
Original Assignee
Bioheap Limited
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 Bioheap Limited filed Critical Bioheap Limited
Priority to EP04713821A priority Critical patent/EP1620576A4/en
Priority to AU2004219986A priority patent/AU2004219986B2/en
Priority to CA2517693A priority patent/CA2517693C/en
Priority to US10/548,470 priority patent/US20060248983A1/en
Publication of WO2004081241A1 publication Critical patent/WO2004081241A1/en

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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
    • 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
    • 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
    • C22B3/18Extraction of metal compounds from ores or concentrates by wet processes with the aid of microorganisms or enzymes, e.g. bacteria or algae
    • 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

  • 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.

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  • 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

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.

Description

"Improved Heap Leach"
Field of the Invention
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.
Background Art
The extraction of metals from sulphide ores by use of bacterially assisted heap leaching has been demonstrated previously. The majority of the prior art processes involve the use of mesophilic bacteria, including Thiobacillus and Leptospirillium species. Such bacterial species generally operate in a temperature range of 20°C to 45°C (Peterson and Dickson, Thermophillic Heap Leaching of a Chalcopyrite Concentrate, Minerals Engineering, 15 (2002), pages 777 to 785). However, the use of bacterially assisted heap leaching in the extraction of copper from chalcopyrite ores is an exception. In such circumstances higher temperatures are required in order to achieve commercially acceptable leach kinetics. In either case, the success of the heap leaching operation is largely dependent upon the oxidation of sulphide minerals to elevate the temperature within the heap above ambient levels and to keep the temperature at those levels.
If the sulphide mineralisation of an ore is below a particular level, the amount of heat generated will be relatively small. Consequently, only a small elevation of the internal heap temperature would be achieved during leaching of that ore, this elevation possibly not being sufficient to result in an economically acceptable leach rate. One apparent remedy for any such short fall in heat generation is to supply heat to the heap from an external source. Such an external source might be the leach liquor that is conventionally applied to the top of the heap, or the air supply, which in some operations is blown into the base of the heap in order to promote the oxidation of sulphide minerals. Further, International Patent Application PCT/ZA 00154 (WO 02/029124) discloses a means for supplying heat to a heap leach, the heat being generated externally of the heap in a bio- reactor.
It should be apparent that if an ore contains a sulphide mineral that requires a temperature in excess of 45°C before it will begin to leach, such as chalcopyrite, then the above circumstance is exacerbated. Irrespective of the quantity of chalcopyrite present, if there is no other sulphide mineral present that will begin to oxidise at lower temperatures, the heap cannot autogenously be brought up to the required operating temperature. As a result, the heap will remain at ambient temperature without the addition of a significant quantity of heat to start the chalcopyrite oxidation reaction. After the injection of the necessary additional heat, if there is sufficient sulphide mineral present the reaction may become self- sustaining. In International Patent Application PCT/US99/28962 (WO 00/36168) there is disclosed a heap leach process in which the process liquor may be added to the top of the heap, requiring an external source of heat. Also, the heap is described as being heated by way of the pumping of steam or hot air through supply lines into the heap, again requiring an external source of heat Still further, a complicated method for stacking heaps on top of an existing heat generating heap is also described, a process that may extend over several generations of heap.
It is one object of the present invention to overcome the abovementioned problems associated with the prior art, or to at least provide a useful alternative thereto.
The preceding discussion of the background art is intended to facilitate an understanding of the present invention only. It should be appreciated that the discussion is not an acknowledgement or admission that any of the material referred to was part of the common general knowledge in Australia or any country, region or territory as at the priority date of the application.
Throughout the specification, unless the context requires otherwise, the word "comprise" or variations such as "comprises" or "comprising", will be understood to imply the inclusion of a stated integer or group of integers but not the exclusion of any other integer or group of integers.
Disclosure of the Invention
In accordance with the present invention there is provided 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.
Preferably, 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. Further, 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.
Still preferably, the blending or addition of elemental sulphur to the ore provides between about 2 to 20% elemental sulphur to ore (w/w).
In accordance with the present invention there is further provided 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.
In one form of the present invention chalcopyrite comprises the predominant sulphide mineral in the ore. Preferably, the blending or addition of elemental sulphur to the ore provides between about 2 to 20% elemental sulphur to ore (w/w).
Still preferably, 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.
Brief Description of the Drawings
The improved heap leach process of the present invention will now be described, by way of example only, with reference to one embodiment thereof and the accompanying drawing, in which:-
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.
Best Mode(s) for Carrying Out the Invention
In Figure 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.
It is to be understood that 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. Further, 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.
During the process of the present invention mesophilic bacteria ("mesophiles") 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.
Savings compared to processes of the prior art are also achieved with the process of the present invention with respect to the generation of sulphuric acid through the oxidation of elemental sulphur. This is particularly the case if the ore to be leached is an overall consumer of acid during the leaching process.
It is envisaged that 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. In addition, 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.
It is envisaged that the blending or addition of elemental sulphur to ore provides between about 2 to 20% elemental sulphur to ore (w/w).
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.
Modifications and variations such as would be apparent to the skilled addressee are considered to fall within the scope of the present invention.

Claims

Claims
1. 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.
2. A process according to claim 1 , wherein 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.
3. A process according to claim 1 , wherein the sulphur is 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.
4. A process according to any one of claims 1 to 3, wherein the blending or addition of elemental sulphur to ore provides between about 2 to 20% elemental sulphur to ore (w/w).
5. 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.
6. A process according to claim 5, wherein chalcopyrite comprises the predominant sulphide mineral in the ore.
7. A process according to claim 5 or 6, wherein the blending or addition of elemental sulphur to ore provides between about 2 to 20% elemental sulphur to ore (w/w).
8. A process according to any one of the preceding claims, wherein 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.
9. An improved heap leach process for the bacterial heap leaching of base metal sulphide ores substantially as hereinbefore described with reference to Figure 1.
PCT/AU2004/000236 2003-03-12 2004-02-24 Improved heap leach WO2004081241A1 (en)

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

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ID=31500149

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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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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.

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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

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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

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Cited By (9)

* Cited by examiner, † Cited by third party
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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