GB2456645A - Extraction from an ore using a redox reagent, a pH adjuster and a dissolution promoter - Google Patents
Extraction from an ore using a redox reagent, a pH adjuster and a dissolution promoter Download PDFInfo
- Publication number
- GB2456645A GB2456645A GB0801378A GB0801378A GB2456645A GB 2456645 A GB2456645 A GB 2456645A GB 0801378 A GB0801378 A GB 0801378A GB 0801378 A GB0801378 A GB 0801378A GB 2456645 A GB2456645 A GB 2456645A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reactive element
- dissolution promoter
- ore
- element dissolution
- complexes
- 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.)
- Granted
Links
- 239000003153 chemical reaction reagent Substances 0.000 title claims abstract description 74
- 238000004090 dissolution Methods 0.000 title claims abstract description 46
- 238000000605 extraction Methods 0.000 title claims abstract description 26
- 239000003002 pH adjusting agent Substances 0.000 title description 2
- 239000000203 mixture Substances 0.000 claims abstract description 48
- 238000000034 method Methods 0.000 claims abstract description 33
- 230000008569 process Effects 0.000 claims abstract description 27
- 230000001590 oxidative effect Effects 0.000 claims abstract description 21
- 229910052751 metal Inorganic materials 0.000 claims abstract description 15
- 239000002184 metal Substances 0.000 claims abstract description 14
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 12
- 239000002253 acid Substances 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 6
- 239000007800 oxidant agent Substances 0.000 claims abstract description 6
- 150000001875 compounds Chemical class 0.000 claims abstract description 4
- -1 oxo anions Chemical class 0.000 claims abstract description 4
- 229910052723 transition metal Inorganic materials 0.000 claims abstract description 4
- 150000003624 transition metals Chemical class 0.000 claims abstract description 4
- 150000001450 anions Chemical class 0.000 claims abstract description 3
- 150000001768 cations Chemical class 0.000 claims abstract description 3
- 239000002738 chelating agent Substances 0.000 claims abstract description 3
- 230000009977 dual effect Effects 0.000 claims abstract description 3
- 239000013110 organic ligand Chemical class 0.000 claims abstract description 3
- 102000004169 proteins and genes Human genes 0.000 claims abstract description 3
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 3
- 125000002524 organometallic group Chemical class 0.000 claims abstract 2
- 239000000758 substrate Substances 0.000 claims description 48
- 239000000872 buffer Substances 0.000 abstract description 2
- 239000000470 constituent Substances 0.000 abstract 1
- 230000002829 reductive effect Effects 0.000 description 19
- 239000000126 substance Substances 0.000 description 17
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- 238000005065 mining Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 150000002739 metals Chemical class 0.000 description 6
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 229910052804 chromium Inorganic materials 0.000 description 5
- 239000011651 chromium Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 4
- 238000011065 in-situ storage Methods 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- 235000019846 buffering salt Nutrition 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- YZCKVEUIGOORGS-UHFFFAOYSA-N Hydrogen atom Chemical compound [H] YZCKVEUIGOORGS-UHFFFAOYSA-N 0.000 description 2
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
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- 229910052802 copper Inorganic materials 0.000 description 2
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- 229910052748 manganese Inorganic materials 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
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- 150000007522 mineralic acids Chemical class 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 229910052755 nonmetal Inorganic materials 0.000 description 2
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- 238000011084 recovery Methods 0.000 description 2
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- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- KEQXNNJHMWSZHK-UHFFFAOYSA-L 1,3,2,4$l^{2}-dioxathiaplumbetane 2,2-dioxide Chemical compound [Pb+2].[O-]S([O-])(=O)=O KEQXNNJHMWSZHK-UHFFFAOYSA-L 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 235000015076 Shorea robusta Nutrition 0.000 description 1
- 244000166071 Shorea robusta Species 0.000 description 1
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- 238000003723 Smelting Methods 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052924 anglesite Inorganic materials 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000009412 basement excavation Methods 0.000 description 1
- 229910001570 bauxite Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 229910001593 boehmite Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 description 1
- 150000005829 chemical entities Chemical class 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052956 cinnabar Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 229910052963 cobaltite Inorganic materials 0.000 description 1
- 238000010668 complexation reaction Methods 0.000 description 1
- 239000008139 complexing agent Substances 0.000 description 1
- 239000002739 cryptand Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 229910001648 diaspore Inorganic materials 0.000 description 1
- ZXOKVTWPEIAYAB-UHFFFAOYSA-N dioxido(oxo)tungsten Chemical compound [O-][W]([O-])=O ZXOKVTWPEIAYAB-UHFFFAOYSA-N 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 229910052949 galena Inorganic materials 0.000 description 1
- 229910001679 gibbsite Inorganic materials 0.000 description 1
- 239000010438 granite Substances 0.000 description 1
- 229910052595 hematite Inorganic materials 0.000 description 1
- 239000011019 hematite Substances 0.000 description 1
- 229910052864 hemimorphite Inorganic materials 0.000 description 1
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- YDZQQRWRVYGNER-UHFFFAOYSA-N iron;titanium;trihydrate Chemical compound O.O.O.[Ti].[Fe] YDZQQRWRVYGNER-UHFFFAOYSA-N 0.000 description 1
- XCAUINMIESBTBL-UHFFFAOYSA-N lead(ii) sulfide Chemical compound [Pb]=S XCAUINMIESBTBL-UHFFFAOYSA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- XMWCXZJXESXBBY-UHFFFAOYSA-L manganese(ii) carbonate Chemical compound [Mn+2].[O-]C([O-])=O XMWCXZJXESXBBY-UHFFFAOYSA-L 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 229910052961 molybdenite Inorganic materials 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- CWQXQMHSOZUFJS-UHFFFAOYSA-N molybdenum disulfide Chemical compound S=[Mo]=S CWQXQMHSOZUFJS-UHFFFAOYSA-N 0.000 description 1
- 229910052758 niobium Inorganic materials 0.000 description 1
- 239000010955 niobium Substances 0.000 description 1
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- SIOXPEMLGUPBBT-UHFFFAOYSA-M picolinate Chemical compound [O-]C(=O)C1=CC=CC=N1 SIOXPEMLGUPBBT-UHFFFAOYSA-M 0.000 description 1
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910021646 siderite Inorganic materials 0.000 description 1
- 239000001509 sodium citrate Substances 0.000 description 1
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 229910052950 sphalerite Inorganic materials 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- DNYWZCXLKNTFFI-UHFFFAOYSA-N uranium Chemical compound [U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U] DNYWZCXLKNTFFI-UHFFFAOYSA-N 0.000 description 1
- YIIYNAOHYJJBHT-UHFFFAOYSA-N uranium;dihydrate Chemical compound O.O.[U] YIIYNAOHYJJBHT-UHFFFAOYSA-N 0.000 description 1
- 229910052821 vanadinite Inorganic materials 0.000 description 1
- 229910052845 zircon Inorganic materials 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
- GFQYVLUOOAAOGM-UHFFFAOYSA-N zirconium(iv) silicate Chemical compound [Zr+4].[O-][Si]([O-])([O-])[O-] GFQYVLUOOAAOGM-UHFFFAOYSA-N 0.000 description 1
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
- 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
-
- 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
- C22B3/16—Extraction of metal compounds from ores or concentrates by wet processes by leaching in organic 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
- C22B34/00—Obtaining refractory metals
- C22B34/30—Obtaining chromium, molybdenum or tungsten
- C22B34/32—Obtaining chromium
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/28—Dissolving minerals other than hydrocarbons, e.g. by an alkaline or acid leaching agent
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Geology (AREA)
- Geochemistry & Mineralogy (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Mining & Mineral Resources (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Fluid Mechanics (AREA)
- Physics & Mathematics (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
A process for the extraction of a reactive element from ore by feeding a redox reagent, a pH adjusting entity (including buffers) and a reactive element dissolution promoter into the proximity of the ore via at least one bore hole and recovering reaction products from at least one bore hole. The redox reagent, pH adjusting entity and reactive element dissolution promoter can be fed separately or together as a single reagent composition with each constituent dissolved or suspended in water. The reactive element dissolution promoter may be a secondary oxidant, a secondary reductant, a secondary acid, a secondary base, dual valency transition metal coordination compounds, chelating agents, (poly)oxo anions, complex anions/cations, zero charge complexes, organometallics, organic ligand complexes, enzymic complexes, protein inorganic metal complexes, crown structures and cryptstands.
Description
IMPROVED EXTRACTION FROM ORES
The present invention relates to a process by which elements can be extracted from ores, and a substrate specific reagent composition for use in the process.
In particular, the invention relates to a process which utilises substrate specific reagents applied to ore bodies in situ, that is in locations within the geological strata wherein they are contained.
Such substrate specific reagents may be percolated through strata containing the ore body of the element or elements to be extracted.
An advantage of the present invention is that the process may be applied to a wide range of minerals and native elemental entities, without the need for extensive mining or other conventional extraction procedures.
The present invention provides both a range of novel substrate specific reagents and a process by which they may be applied in the extraction of ranges of elements from specific ores.
In this specification the ore body is the substrate to be reacted.
Whereas it is known that certain acids, alkalis, oxidants and reductants may dissolve or partially dissolve specific ores, so as to facilitate the extraction of certain elements, it has now been discovered that this effect can be significantly improved by the application of these reactants in the form of the substrate specific reagent compositions of the present invention.
By substrate specific reagents, in this specification, we mean reagents that act preferentially on a reactive element in the ore body.
By reactive element in the ore body we mean a specific element present in the ore, which may or may not be the targeted element.
By targeted element we mean the valuable element present in the ore, which is the subject of the main commercial aim of the extractive process.
By way of an explanation, it has now been discovered that targeted elements may be extracted from ores via the dissolving effect caused by substrate specific reagent compositions. This dissolution process may solubilise either the reactive element or the targeted element or both. The dissolution process suitably de-structures the ore body and allows for the removal of the targeted element in a freed physico- chemical format.
The physico-chemical function achieved by the substrate specific reagent composition of the present invention may be for example, an accelerated form of acid dissolution, alkali, dissolution, oxidative dissolution, reductive dissolution or any known chemical combination of the above, of the reactive element, which may or may not be the targeted element.
The physico-chemical format produced by the substrate specific reagent composition may be a solubilised or suspended form of acidified, basified, oxidised or reduced form or any known chemical combination, of the reactive element which may or may not be the targeted element.
In simple terms we may describe the overall effect of the process of the present invention as kinetically breaking the ore body so as to release elements that can then be freed for extraction.
The present invention provides a process for the extraction of various elements from their ore bodies without the need for conventional mining via the application of substrate specific reagents which solubilise components of the ore and render them recoverable as pumpable solutions or suspensions.
The process may provide for the chemical extraction of metal, transition metal and non-metal elements from ore bodies.
According to a first aspect of the present invention, there is provided a substrate specific reagent composition comprising: a redox reagent; a pH adjusting entity; and a reactive element dissolution promoter.
The substrate specification reagent composition is
preferably an aqueous composition. Suitably the redox reagent, pH adjusting entity and reactive element dissolution promoter are dissolved or suspended in water.
According to a second aspect of the present invention, there is provided a process for the extraction of a reactive element from an ore body, the process comprising applying to the ore body a redox reagent, a pH adjusting entity and a reactive element dissolution promoter.
In the process of the second aspect, each of the redox reagent, pH adjusting entity and reactive element dissolution promoter may be applied alone or in combination with one or more of the other components.
Each component may optionally comprise a mixture of reagents. For example the process may comprise applying a mixture of one or more redox reagents and/or one or more pH adjusting agents and/or one or more reactive element dissolution promoters. Thus the redox reagent, pH adjusting entity and reactive element dissolution promoter may be applied concurrently or sequentially. Preferably the process of the second aspect comprises applying to the ore body a composition of the first aspect.
The nature of the substrate specific reagent composition that is the subject of the present invention will now be defined.
The redox reagent (also referred to herein as redox entity) is suitably an oxidant or a reductant. A mixture of two or more oxidants and/or reductants may be used.
Hydrogen peroxide contained in an aqueous solution is an example of a suitable oxidic ingredient for use as a redox reagent in the substrate specific reagent composition.
Nascent hydrogen derived from, for example, the reaction between powered zinc and a strong inorganic acid, may be used as a redox reagent and is an example of a suitable reductive entity in the substrate specific reagent composition.
The pH adjusting entity (or pH controlling entity), may be an acid, an alkali, a buffering salt or a mixture thereof.
Suitable examples of useful pH adjusting entities include strong inorganic acids, strong inorganic alkalis and chemical buffering salts. Chemical buffering salts are typically either salts based on strong acids and weak bases, or weak acids and strong bases. The overall result of the addition of such buffers is to alter and then maintain a specific mid range pH.
The substrate specific reagent composition also comprises a reactive element dissolution promoter.
By reactive element dissolution promoters we mean specific complex chemical substances that act so as to accelerate the effect of the other two components in the substrate specific reagent composition.
Suitable reactive element dissolution promoters include secondary oxidants, secondary reductants, secondary acids and secondary bases. Advantageously these may also contain secondary buffering agents, and complexing agents that maintain either or both the reactive and the targeted element in solubilised form.
Though not catalysts in the chemical sense of the term, these reactive element dissolution promoters suitably work with the redox and pH adjusting chemicals so as to promote and accelerate the desired reaction on the ore.
Though as yet not fully understood it is believed that these reactive element dissolution promoters function by providing oxidative or reductive chemical bridges for the desired reactions on the targeted element in the ore body.
The reactive element dissolution promoters may be selected from complex chemical entities for example, coordination compounds of dual valency transition metals, chelating agents, oxo and poly oxo anions, complex cations, complex anions, zero charge complexes, organometalics, organic ligand complexes, enzymic complexes, protein inorganic metal complexes, crown structures, cryptands and other advanced chemicals.
The reactive element dissolution promoters may confer chemically distinguishing features as specific extracted elements from the core bodies treated, via approaches such as coordinate compound formation, complexation, chelation and crypstand formation.
It is a feature of the present invention that a wide range of highly specific reactive element dissolution promoters have been discovered and can be made available for the treatment of many commercial and currently mined ore bodies.
These reactive element dissolution promoters may accelerate the solubilisation of the reactive element in the ore body and may also serve to maintain the dissolved substances in solution.
It is believed that the solubility maintaining function of the above grouping of types of reactive element dissolution promoters is that they provide linkage points with specific ionic radii. In this way they may be targeted for the abstraction of specific elements contained in specific form in specific ores.
It is a feature of the present invention that relatively small quantities of reactive element dissolution promoter are needed to effect the accelerated dissolution and solubility maintenance of reactive elements in specific ores on which they are targeted.
Preferably the substrate specific reagent composition of the present invention is an aqueous composition comprising significant quantities of a redox reagent, significant quantities of a pH adjusting entity, and smaller quantities of a reactive element dissolution promoter.
Typically, the substrate specific reagent composition contains: 5% to 95% w/w of a redox reagent; 5% to 95% wlw of a pH adjusting entity; and -% to 5% w/w of a reactive element dissolution promoter.
Preferably, the substrate specific reagent composition contains: 50% to 90% w/w of a redox reagent; 5% to 50% w/w of a pH adjusting entity; and 0.0001% to 0.1% w/w of a reactive element dissolution promoter.
By applying a substrate specific reagent composition, as defined herein, to specific ores the reactive element, which may or may not also be the targeted element, may be abstracted into the aqueous phase via an accelerated process.
The targeted element, if it is not also the reactive element, may then be extracted from the ore body either as a solution or a suspension.
The result of using a substrate specific reagent composition, as defined herein, is to significantly reduce the current difficulties associated with the mining of certain specific elements.
The scope for the use of the substrate specific reagent approach to mining will now be defined, firstly in general terms.
Substrate specific reagents may be applied in the extraction of a wide range of elements.
Any element may be extracted from an ore in which it is contained if either the target element or the reactive element, or both, are capable of chemical existences in two or more valencies. Thus both native element and mineral ores may be so treated.
Also it will be recognised that a wide range of metal and metal containing ores may be so treated.
Rare elements contained in small quantities in ores may also be recovered.
Additionally many non-metallic elements can be so treated.
Many rarer metals and elements contained in small quantities in ores together with less rare metals or elements may be treated as to first solubilise the less rare element. The effect of dissolving the less rare element from the ore matrix frees or aids the release of the rarer element.
The use of substrate specific reagents is believed to amount to a significant commercial improvement, in the form of an alternative to conventional mining. This assertion stems from the recognition that substrate specific reagent compositions may be used in-situ i.e. via pipelines or bore holes to the proximity of the ore body rather than massive excavation, as is current practice.
These aspects of the current invention will be described later in this patent application.
The scope for the use of substrate specific reagent compositions will now be defined in terms of a limited number of specific examples of types of reagent developed for the treatment of a specific ore.
To date we have discovered and are developing many substrate specific reagents, as described herein, for the in-situ treatment of many specific ores, and our research continues. The following are therefore only examples of the types of substrate specific reagents we have developed, together with definitions of appropriate ore bodies.
We have chosen the following two examples because they are based on commercially available reactive element dissolution promoters.
The first quoted example is a form of alkaline oxidative extraction.
The second quoted example is a form of acidic reductive extraction.
Example 1
A suitable substrate specific reagent for the extraction of chromium from chromite ore, may comprise a water based solution of hydrogen peroxide an alkaline, buffering agent such as sodium citrate together with sodium hydroxide and a small quantity of a manganese complex based on nine member ligand rings known as "Gandor". Gandor is a commercially available reagent used in the peroxide bleaching of cellulosics for example cotton and wood pulp.
The result of applying the above substrate specific reagent is the oxidation of both iron, the reactive element and chromium, the target element, and their removal from the spinal structure of the chromite ore, in dissolved form.
Example 2
A suitable substrate specific reagent for the extraction of chromium from chromite ore may comprise a water based solution of nascent hydrogen produced in-situ via reaction of hydrochloric acid on finely divided zinc powder, together with the aforementioned acid and a small quantity of a vanadium complex based on picolinate ligands known as a LOMI reagent.
LOMI (Low Oxidation Metal Ion) reagents are commercially available heater circuit descaling agents used in the nuclear power generation industry. The result of applying the above substrate specific reagent is the reduction of the chromium, which in this case is both the reactive and the target element, and its removal from the spinal structure of the chromite ore, in dissolved form.
Many other substrate specific reagents both based on currently commercially available reactive element dissolution promoters and further types currently under development, have been shown to be effective in the improved ore extraction procedure which is the subject of the current invention.
The scope of the current invention will now be further demonstrated via a listing of proven examples of ores that can be treated via selected substrate specific reagent compositions for the extraction of the targeted element: Copper via an acidic reductive version on malachite.
Tin via an acidic reductive version on cassiterite.
Titanium via an acidic oxidatative version on ilmenite.
Manganese via either an alkaline oxidative version on rhodochrosite, or an acidic reductive version on pyrolusive.
Chromium via an alkaline oxidative version on chromite, or an acidic reductive version on the same ore.
Nickel via an acidic oxidative version on suiphide ores, or an acidic reductive version on divalent ores.
Molybdenum via an alkaline or buffered oxidative version on molybdenite, or an acidic reductive system on higher valency ores.
Tungsten via an alkaline or buffered oxidative version on wolframite, or an acidic reductive version on woiframite or scheelite.
Cobalt via an acidic oxidative version on cobaltite, or an acidic reductive version on trivalent ores or nickel/copper tailings.
Uranium via an alkaline oxidative version on uraninite ie pitchblend, or an acidic reductive version based on ores containing one or more higher valency.
Zirconium via an acidic reductive version on zircon sands.
Vanadium via an alkaline oxidative version on vanadinite or carnotite, or an acidic reductive version on higher valency ores.
Cerium via an alkaline or buffered oxidative version on monozite sands, or an acidic reductive version on bastnasite.
Niobium via an alkaline oxidative version on niobite or columbite.
Tantalum via an alkaline oxidative version on tantalite or colurnbite.
Platinum group via alkaline or acid oxidative versions on native metals or suiphide ores.
Nobel metals via alkaline or acid oxidative versions on native metal or suiphide ores.
Additionally, our work continues on the development of substrate specific reagent compositions for treatment of the following ores: Carbonate-based oil shales for oil extraction.
Magnetite, hematite, siderite for iron extraction.
Bauxite, boehmite, diaspore and gibbsite for aluminium extraction.
Sphalerite and hemimorphite for zinc and associated rarer metals.
Galena, anglesite for lead and associated rarer metals.
Cinnabar, for mercury.
Basalt, for a wide range of rarer elements.
Granite, for a wide range of rarer elements.
Ways in which the substrate specific reagent compositions, as defined herein, may be applied to ore bodies will now be described.
Typically a substrate specific reagent composition is pumped or fed into the proximity of the ore body via a hole or bore holes and, after reaction, the reaction products are recovered in a similar manner.
In a relatively simple embodiment of the current invention the substrate specific reagent composition may be applied and the reaction products recovered via a single concentric bore hole. The composition may be transported to the ore body down the annulus and the reaction products recovered via the central pipe.
Alternatively, two simple bore holes may be used. These are to be positioned one upstream of the ore body, in terms of natural subterranean water flowing through the strata, and the other downstream of the ore body. The composition is supplied through the upstream bore and the reaction products recovered through the downstream bore.
In a further embodiment a single reactant bore hole may be surrounded or partially surrounded by a ring of reaction product extraction bore holes.
In some situations a single bore hole can be used for the composition, and the reaction products recovered from natural springs issuing from the ore body.
Using any of the above four examples or any further currently applied bore hole mining technologies, substrate specific reagent compositions may conveniently be applied to ore bodies.
In the case of some alluvial deposits, bore holes are not required and the ore sands may be treated in lined lagoons or tanks.
A similar system may be applied in the cases of previously mined ores and ore tailings.
In many situations the simple provision of the substrate specific reagent composition and the recovery of the reaction products will yield the targeted element.
However, in more sophisticated embodiments of the current invention, extraction efficiencies may be increased by any one or combinations of the following: In a further embodiment of the current invention the substrate specific reagent compositions may be heated prior to use.
In a further embodiment of the current invention the pH of the substrate specific reagent composition may be progressively changed during the application of the substrate specific reagents.
In a further embodiment of the current invention a sequence of two or more substrate specific reagent compositions may be introduced, with differing redox potentials, in sequence or concurrently.
In a further embodiment of the current invention two or more reactive element dissolution promoters may be used, in sequence or concurrently.
In a further embodiment of the current invention, an electric current may be established between bore hole systems.
In a further embodiment of the current invention a two stage extraction process may be used which can involve firstly an oxidative phase followed by a reductive phase, or, firstly a reductive phase followed by an oxidative phase.
By applying any one or a combination of the above embodiments, the extraction rate of targeted elements may be improved.
The result obtained is suitably a flow of reaction products containing the extracted targeted element together with other entities derived from the dissolution process and residues from the pH adjusting and redox components and reactive element dissolution promoter.
The target element may be recovered from this water based mixture by any appropriate standard chemical separation procedure, for example as is currently applied to the element concerned.
These recovery processes are well known in mining chemistry and may involve the application of any one or a sequence of the following: pH alteration; precipitation; solubilisation; ion exchange; solvent extraction; froth floatation; chelation; electrochemical reaction; evaporation; crystallisation; oxidation; reduction, and smelting.
The resulting product will be the targeted element in the form of either the metal or non-metal or commercially usable chemicals derived from the same.
It is an advantage of the current invention that the separation of the targeted element from the reaction products may be simplified or improved in terms of efficiency because of the specific nature of the reactive element dissolution promoter used in the substrate specific reagent. This effect stems from the ability of the reactive element dissolution promoter to selectivity abstract specific targeted elements. Specifically, we believe, this is achieved on the basis of ionic radii, although other mechanisms may also be involved.
The result is that the targeted element entities produced differ chemically, and are therefore easier to separate from, the other reaction products.
In some cases valuable dissolved co-products may also be recovered via the above techniques.
In still further cases at least some part of the reactive element dissolution promoter may also be recoverable.
The overall result achieved by the process of the present invention is the economic extraction of a wide range of commercially important elements from their ores.
Moreover, the present invention permits much energy to be saved because of the significant reduction in extractive effort. Far less overburden and non-ore rock needs to be excavated than in conventional mining.
This reduction in the generation of mine spoils also has a beneficial effect on the local scenery, the local ecology and the environment generally.
Taken together, we believe the above improvements constitute a major breakthrough in the extractive industry Attention is directed to all papers and documents which are filed concurrently with or previous to this specification in connection with this application and which are open to public inspection with this specification, and the contents of all such papers and documents are incorporated herein by reference.
All of the features disclosed in this specification (including any accompanying claims, abstract and drawings), and/or all of the steps of any method or process so disclosed, may be combined in any combination, except combinations where at least some of such features and/or steps are mutually exclusive.
Each feature disclosed in this specification (including any accompanying claims, abstract and drawings) may be replaced by alternative features serving the same, equivalent or similar purpose, unless expressly stated otherwise. Thus, unless expressly stated otherwise, each feature disclosed is one example only of a generic series of equivalent or similar features.
The invention is not restricted to the details of the foregoing embodiment(s). The invention extends to any novel one, or any novel combination, of the features
disclosed in this specification (including any
accompanying claims, abstract and drawings), or to any novel one, or any novel combination, of the steps of any method or process so disclosed.
Claims (9)
1. A substrate specific reagent composition comprising: a redox reagent; a pH adjusting entity; and a reactive element dissolution promoter.
2. A composition according to claim 1 wherein the redox reagent, pH adjusting entity and reactive element dissolution promoter are dissolved or suspended in water.
3. A composition according to claim 1 or claim 2, wherein the reactive element dissolution promoter is selected from a secondary oxidant, a secondary reductant, a secondary acid and a secondary base.
4. A composition according to claim 1 or claim 2, wherein a reactive element dissolution promoter is selected from coordination compounds of dual valency transition metals, chelating agents, oxo and poiy oxo anions, complex cations, complex anions, zero charge complexes, organometallics, organic ligand complexes, enzymic complexes, protein inorganic metal complexes, crown structures and cryptstands.
5. A composition according to any preceding claim which comprises: 50% to 90% w/w of a redox reagent; 5% to 50% w/w of a pH adjusting entity; and 0.0001% to 0.1% w/w of a reactive element dissolution promoter.
6. A process for the extraction of a reactive element from an ore body, the process comprising applying to the ore body a redox reagent, a pH adjusting entity and a reactive element dissolution promoter.
7. A process according to claim 6, which comprises applying to the ore body a composition as claimed in any of claims 1 to 5.
8. A process as claimed in claim 6 or claim 7 in which the redox reagent, a pH adjusting entity and a reactive element dissolution promoter are pumped or fed into the proximity of the ore body via a bore hole or bore holes and reaction products are recovered via a bore hole or bore holes.
9. A composition or process substantially as hereinbefore described with reference to the examples.
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US2896930A (en) * | 1954-06-10 | 1959-07-28 | Nuclear Dev Corp Of America | Method of recovering uranium from underground deposit |
US3545964A (en) * | 1968-04-18 | 1970-12-08 | Atomic Energy Commission | Gold recovery process |
US3640579A (en) * | 1970-04-28 | 1972-02-08 | Arthur E Lewis | In situ pressure leaching method |
US3912330A (en) * | 1974-03-04 | 1975-10-14 | Us Interior | Chemical mining of copper porphyry ores |
US4069293A (en) * | 1975-05-06 | 1978-01-17 | The United States Of America As Represented By The United States Department Of Energy | Method for dissolving plutonium dioxide |
US4340252A (en) * | 1979-05-07 | 1982-07-20 | Mobil Oil Corporation | Process for the in-situ leaching of uranium |
SU1408057A1 (en) * | 1986-07-07 | 1988-07-07 | Производственное Геологическое Объединение "Краснохолмскгеология" | Method of mining mineral deposits by underground leaching |
US4784688A (en) * | 1985-03-29 | 1988-11-15 | Interox Chemicals Limited | Tungsten recovery |
Family Cites Families (1)
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US4243638A (en) * | 1978-06-15 | 1981-01-06 | Westinghouse Electric Corp. | Iron EDTA chelate catalyzed oxidation of uranium |
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2008
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US2896930A (en) * | 1954-06-10 | 1959-07-28 | Nuclear Dev Corp Of America | Method of recovering uranium from underground deposit |
US3545964A (en) * | 1968-04-18 | 1970-12-08 | Atomic Energy Commission | Gold recovery process |
US3640579A (en) * | 1970-04-28 | 1972-02-08 | Arthur E Lewis | In situ pressure leaching method |
US3912330A (en) * | 1974-03-04 | 1975-10-14 | Us Interior | Chemical mining of copper porphyry ores |
US4069293A (en) * | 1975-05-06 | 1978-01-17 | The United States Of America As Represented By The United States Department Of Energy | Method for dissolving plutonium dioxide |
US4340252A (en) * | 1979-05-07 | 1982-07-20 | Mobil Oil Corporation | Process for the in-situ leaching of uranium |
US4784688A (en) * | 1985-03-29 | 1988-11-15 | Interox Chemicals Limited | Tungsten recovery |
SU1408057A1 (en) * | 1986-07-07 | 1988-07-07 | Производственное Геологическое Объединение "Краснохолмскгеология" | Method of mining mineral deposits by underground leaching |
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GB2456645B (en) | 2011-03-02 |
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