[go: up one dir, main page]

WO1997014818A1 - Procede d'extraction d'or comportant une bioflottation - Google Patents

Procede d'extraction d'or comportant une bioflottation Download PDF

Info

Publication number
WO1997014818A1
WO1997014818A1 PCT/GB1996/002538 GB9602538W WO9714818A1 WO 1997014818 A1 WO1997014818 A1 WO 1997014818A1 GB 9602538 W GB9602538 W GB 9602538W WO 9714818 A1 WO9714818 A1 WO 9714818A1
Authority
WO
WIPO (PCT)
Prior art keywords
flotation
electric field
bioflotation
agitation
minutes
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.)
Ceased
Application number
PCT/GB1996/002538
Other languages
English (en)
Inventor
Nicolay Pertsov
Zoya Ulberg
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CORMACK EDWIN JAMES
Original Assignee
CORMACK EDWIN JAMES
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 CORMACK EDWIN JAMES filed Critical CORMACK EDWIN JAMES
Priority to AU73119/96A priority Critical patent/AU7311996A/en
Publication of WO1997014818A1 publication Critical patent/WO1997014818A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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
    • 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
    • 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
    • C22B11/00—Obtaining noble metals
    • C22B11/04—Obtaining noble metals by wet processes
    • 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 invention relates to a process for extracting gold from mineral suspension, in particular, from the tails containing the finely-dispersed gold, and can be used at the gold-extracting plants.
  • Flotation is known to be one of the widely used processes of gold-containing ore enrichment. Processing of the flotation concentrate in order to recover gold therefrom is simpler and cheaper than the similar treatment of total ore stock. Sometimes the flotation enrichment does not allow to extract all gold contained in concentrate. Nevertheless, even in this case the flotation is advisable, because this process permits to transform into the concentrate the most persistent part of gold which is not usually extracted by the conventional techniques of gravitation enrichment, cyanidation and amalgamation.
  • flotoreagents or flotation reagents in particular, collectors, foaming agents, foam stabilizers, etc. are usually used in the process of flotation.
  • Sulphide-hydril reagents namely, butyl-, amilethyl-xantogenates are used as collectors.
  • Xantogenates are usually selectively adsorbed, that is, they are fixed upon the most active areas of gold surface with hydrophobization of gold surface being provided, and the flotation process being improved thereby.
  • Soya oil is usually used as a foaming agent.
  • a little of fatty-acid reagent, such as sodium oleate is added to stabilize the foam. Suppression of empty rock is achieved by means of liquid glass, carboxymethylcellulose and other reagents.
  • Such reagents as cyanides, sodium sulphide, alkali, blue vitriol, sodium sulphate are are often present in the flotation pulp. To greater or lesser extent these reagents supress the gold flotation process. The strongest supressor is sodium sulphide. The floatibility of gold is also decreased with the increase in pH value of the suspension. The floatability of free gold in acid medium is lower than in the neutral one, that results from the decrease of xantogenase adsorption upon the gold surface and from the reduction in pH value of the solution. The flotation of gold and gold-containing sulphides is actually performed at pH between 7.5 to 8.5 with soda being used as pH value regulator.
  • the flotation tails still contain geld, mainly the finely-disperse one, which is further extracted by cyanidation technique (L.V. Chuguyev. Metallurgy of noble metals. Moscow, " Metallurgy” . 1987, p. 269-270)
  • stage flotation for extracting gold from gold-containing ore to be present in the form of mineral suspension make, possible to recover gold from the most persistent ores, which is not achieved by other known techniques of ore enrichment.
  • the flotation tails however, still contain a considerable amount of gold, basically the finely-disperse one. Further extraction of gold from the flotation tails is performed by the cyanidation technique which is environmentally harmful.
  • the problem of the invention is to develop a process for extracting gold from the mineral suspension, wherein reagents, techniques and parameters of performing thereof enable to provide the conditions under which the maximum extraction of gold from the flotation tails is being achieved, and the environment is not harmfully affected.
  • the problem is solved by that in the known process for extracting gold from mineral suspension consisting in that at least one stage of notation is performed using the known flotoreagents, according to the invention after at least one stage of flotation the biomass of microorganism culture in an amount between 10.0 to 30.0 grams per ton is introduced into the flotation tails, and the agitation is performed over a period between 6.0 to 10.0 minutes after which the biomass of microorganism culture in an amount between 10.0 to 30.0 grams per ton is further added to the mixture of the flotation tails and microorganism culture, and the flotation of said mixture is performed over a period between 12.0 to 15.0 minutes.
  • Said process allows to increase the extraction of finely-disperse gold to be present in the flotation tails with the environmentally harmful reagents being not involved in the process .
  • This effect is achieved because in the process of agitation of a mixture of flotation tails and microorganism culture under said parameters there are created the most favorable conditions for the interaction between the microorganism culture and the surface of ore particles containing the finely-disperse gold with the bioaggregates of a size between 0. 060 to 0.070 mm being produced thereby ..
  • This provides the improved extraction of gold as well as of other noble metals such as silver from the flotation tails in the process of further flotation thereof.
  • Said modification of the process provides the preservation of the produced bioaggregates at the moment of dispersing action of the floating mashine impeller.
  • Said modification of the process provides the most favorable conditions for producing bioaggregates in the process of agitation and for performing the flotation of said bioaggregates.
  • Bacillus cereus B - 5039 be used as a microrganism culture.
  • Said microorganism culture is characterized by the highest degree of selectivity towards the gold, which increases the number of produced bioaggregates resulting in the growth of gold extraction rate.
  • Ore gravitation tails used as a starting raw material and containing 4.6 grams per ton of gold and 9.0 grams per ton of silver were utilized for performing the process.
  • the gravitation tails were disintegrated on the conventional grinding machine with 60% of ore being of a particle size 0.074 mm.
  • the mineral suspension was further prepared by mixing the disintegrated ore and water at a ratio of solid phase to the liquid one being 1:5. Said mineral suspension was subjected to the flotation on the conventional floating machine of the lab or large-scale type.
  • the volume of the lab floating machine chamber was 1.5 litre.
  • the flotation process hereafter referred to as a basic flotation, was performed in the presence of the commercially applied flotoreagents such as butyl potassium xantogenate used in an amount 60.0 grams per ton and pine oil in an amount 80.0 grams per ton.
  • the flotation was performed during 20.0 minutes.
  • the tails of basic flotation representing the mineral suspension were supplied from the flotation chamber to the intermediate vessel of a volume between 2.0 to 3.0 litres which is provided with an agitation device and the electrodes to be connected to the direct power supply source.
  • the biomass of microorganism culture in an amount between 10.0 to 30.0 grams per ton was introduced into this vessel, and the agitation of a mixture of the basic flotation tails and microorganism culture was performed during a period between 6.0 to 10.0 minutes.
  • microorganism culture there could be used any microorganism culture capable of coagulating gold, e.g. the green algae of Chlorella kind.
  • the most rational is to use the microorganism culture of Bacillus cereus kind, strain 5039, deposited in the All-Union Collection of Industrial Microorganisms of VNIT Genetics Institute on 24 October, 1989 under Deposit No. B5039.
  • the culture-morphological and physico-biochemical features of the Bacillus cereus VKPM 5039 strain are as below described.
  • the bacteria are bacillus-like of a cell length between 3.0 to 5.0mm and of a cell width between 1.0 to 1.2 mm. They are gram-positive, produce the ellipse-like spores and are of central location. On the meat-peptone agar they form a solid film, and produce little turbidity and deposit. When being grown upon the meat-peptone broth the bacteria do not produce hydrogen sulphide, indol and ammonia Hydiolize starch do not hydrolize kasein, urea and thyrazine. Do not produce acids from mannite, soibitol, xylose, arabinose. An acid is formed from glucose and sacharose. Produce catalaze. The Foges-Proskauer reaction is positive .
  • Reduce nitrates into nitrites do not form a gas from glucose.
  • the bacteria do not grow in the presence of 7.0% NaCl.
  • the optimal temperature of cultivation is 30°C.
  • Said microoiganism strain was separated from the shelves of the Far East. It is characterized by the increased capacity to gold coagulation. Said microorganism culture is cultivated on the meat-peptone broth (1:3) or in 3-5 % solution of the hydralizate of carbohydrate-oxidating yeast prepared on oil paraphines at a temperature between 30.0 to 32.0oC and pH between 6.3 to 6.7.
  • the agitation of the flotation tails and microorganism culture was performed over a period between 6.0 to 10.0 minutes in the presence of sodium hexametaphosphace which is also introduced into said vessel.
  • the power supply source could be connected to the electrodes, and the agitation of said mixture be performed under effect of the electric field of the intensity between 0.5 to 2.0 V/cm.
  • the mixture of the flotation tails and biomass or microorganism culture was further supplied to the floating mashine with its chamber being provide with the electrodes connected to the direct power supply source.
  • the biomass of microorganism culture in an amount between 10.0 to 30.0 grams per ton as well as such flotoreagents as buthyl potassium xantogenate in an amount between 40.0 to 60.0 grams per ton and pine oil in an amount between 40.0 to 45.0 grams per ton were introduced into the chamber of said floating mashine.
  • the flotation process which is further referred to as a bioflotation process was performed over a period between 12.0 to 15.0 minutes. 2.0 - 3.0 minutes after starting the bioflotation process the direct power supply source may be switched on, and bioflotation be carried out during between 1.0 to 1.5 minute under the effect of electric field of intensity between 1.5 to 2.5 V/cm.
  • Pre-desintegrated tails of gravitation ore enrichment in an amount 250.0 grams were used to perform the process.
  • 60% of mineral particles were of a size 0.074 mm.
  • the mineral suspension was prepared with the ratio of solid particles to liquid being 1 :5.
  • the basic flotation was performed in the impeller-type floating mashine of a chamber volume 1.5 litre.
  • the flotation was performed over a period of 20 minutes in the presence of buthyl potassium xantogenate in an amount 60.0 grams per ton, and of pine oil in an amount 80.0 grams per ton.
  • the mineral suspension was further supplied to an intermediate agitation vessel of a volume 2.0 litres provided with the electrodes connected to direct power supply source and designed for inducing an electric field.
  • the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 25 grams per ton and sodium hexametaphosphate in an amount 40 grams per ton were introduced into this vessel, and the mixture of mmeral suspension and microorganism culture v/as subjected to agitation over a period of 6.0 minutes. 0.75 minutes prior to the completion of agitation the direct power supply source was switched on, the electric field of intensity 0.5 V/cm was produced in said vessel, and the agitation of said mixture was performed under the effect of electric field.
  • the mixture of mineral suspension and microorganism culture was supplied to the floating mashine provided with electrodes connected to the direct power supply source. 15.0 grams per ton of said microorganism culture. 45 grams per ton of buthyl potassium xantogenate and 45.0 grams per ton of pine oil were additionally introduced into the floating mashine, and bioflotation was performed during 2.0 minutes.
  • the direct power supply source was then switched on, the electric field of intensity 2.5 V/cm was produced in the floating mashine cell, and bioflotation was performed under the effect of electric field during 1.5 minutes.
  • the power supply source was then switched off, and bioflotation was further performed without the action of electric field.
  • the total duration of bioflotation process constituted 14.0 minutes.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 10.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 6.0 minutes.
  • the electric field of intensity 0.5 V/cm was produced in said agitation vessel, and agitation was performed under the effect of the electric field.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 10.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 6.0 minutes.
  • 1.0 minute prior to completion of agitation the electric field of intensity 2.0 V/cm was produced in said agitation vessel, and agitation was performed under the effect of electric field.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 10.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 10.0 minutes .0.5 minute prior to completion of agitation the electric field of intensity 2.0 V/cm was produced in said agitation vessel, and agitation was performed under the effect of electric field .
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 15.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 6.0 minutes.
  • the electric field of intensity 1.5 V/cm was produced in said agitation vessel, and agitation was performed under the effect of electric field.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 30.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 6.0 minutes.
  • the electric field of intensity 0.5 V/cm was produced in said agitation vessel, and agitation was performed under the effect of electric field.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250 0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 10.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 6.0 minutes.
  • the electric field of intensity 0.5 V/cm was producedin said agitation vessel, and agitation was performed under the effect of electric field.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microalga culture Chlorella Vulgaris Larg 3. in an amount 30.0 g/t and 40.0 g/t of sodium hexametaphosphate were
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 25.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 6.0 minutes.
  • said mixture was supplied to the floating mashine similar to that described in example 1 to realize the bioflotation process.
  • 20.0 g/t of biomass of said microorganism culture, 40.0 g/t of buthyl potassium xantogenate and 40.0 g/t of pine oil were additionally introduced into the floating mashine cell, and bioflotation was
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 20.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 6.0 minutes. 0.5 minutes prior to completion of agitation the electric field of intensity 1.5 V/cm was produced in said agitation chamber, and the agitation was carried out under the effect of electric field.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used to perform the process.
  • the basic flotation was carried out as in example 1.
  • the mineral suspension was further supplied from the floating machine chamber to the intermediate vessel similar to that of example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 25.0 grams per ton and sodium hexametaphosphate in an amount 40.0 grams per ton were introduced, and the obtained mixture was subjected to agitation over a period of 6.0 minutes. After the completion of agitation the above mixture was supplied into the floating mashine as described in example 1.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1, whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 5.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 6.5 minutes.0,25 minute prior to completion of agitation the electric field of intensity 1.5 V/cm was produced in said agitation chamber, and the agitation was carried out under the effect of electric field.
  • the electric field of intensity 0.5 V/cm was then produced and the bioflotation process was performed during 1.5 minutes under the effect of electric field.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 20.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 7.0 minutes. 2.0 minute prior to completion of agitation the electric field of intensity 3.5 V/cm was produced in said agitation chamber, and the agitation was carried out under the effect of electric field.
  • the electric field of intensity 3.0 V/cm was then produced and the bioflotation process was performed during 1.6 minute (100 sec.) under the effect of electric field.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1 , whereinto the biomass of microorganism culture Bacillus cereus VKPM 5039 in an amount 25.0 g/t and 40.0 g/t of sodium hexametaphosphate were introduced, and the agitation of the obtained mixture was performed during 6.0 minutes. 1 .5 minute prior to completion or agitation the electric field of intensity 2.0 V/cm was produced in said agitation chamber, and the agitation was carried out under the effect of electric field.
  • the electric field of intensity 2.0 V/cm was then produced and the bioflotation process was performed during 3.0 minutes under the effect of electric field.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the tails of gravitation ore enrichment in an amount 250.0 grams were used for performing the process.
  • the preliminary operations were carried out as in example 1.
  • the basic flotation was performed as described in example 1.
  • the mineral suspension was supplied from the floating mashine cell to the intermediate vessel similar to that described in example 1, whereinto 40.0 g/t of sodium hexametaphosphate was introduced, and the agitation of the obtained mixture was performed during 6.0 minutes.
  • the electric field of intensity 2.0 V/cm was produced in said agitation chamber, and the agitation was carried out under the effect of electric field.
  • said mixture was supplied to the floating mashine similar to that described in example 1 to realize the bioflotation process.
  • 40.0 g/t of buthyl potassium xantogenate and 40.0 g/t of pine oil were additionally introduced into the floating mashine cell, and flotation was performed during 2.0 minutes.
  • the electric field of intensity 1.5 V/cm was then produced intheflotation cell, and the flotation process was performed during 1.0 minute under the effect of electric field.
  • the yield, the gold and silver content were determined in the concentrates of basic flotation and bioflotation processes as well as in the bioflotation tails.
  • the process for extracting gold from mineral suspension according to the invention allows to efficiently recover gold from the mineral suspension with the remaining gold in the bioflotation tails constituting between 0.19 to 0.61 grams per ton. Silver is also effectively extracted along with gold, and its residue in the bioflotation tails amounts to between 2.1 to 4.6 grams per ton (example 1 through 11)
  • the implementation of the process under operation conditions beyond the claimed limits results in the reduction of the process efficiency.
  • the increase in the amount of biomass to be introduced into the mineral suspension to the level lower to the claimed limits causes the increase in the quantity of the remaining gold and silver in the bioflotation tails (example 12).
  • the process of the invention for extracting gold from a mineral suspension may be used in the mining industry at plants for extracting gold present in the ore in a finely dispersed state.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Metallurgy (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Biotechnology (AREA)
  • Geology (AREA)
  • Geochemistry & Mineralogy (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

L'invention concerne un procédé d'extraction d'or à partir d'une suspension minérale, comportant au moins une étape de flottation mettant en oeuvre les réactifs de flottation, à la suite de laquelle la culture de micro-organismes en une quantité comprise entre 10,0 et 30,0 grammes par tonne est introduite dans les résidus de flottation, et l'agitation est effectuée pendant 6,0 à 10,0 minutes. La biomasse de la culture de micro-organismes en une quantité comprise entre 10,0 et 30,0 grammes par tonne est ensuite en plus introduite dans le mélange des résidus de flottation et de la culture de micro-organismes, et la flottation dudit mélange s'effectue pendant une durée comprise entre 12,0 et 15,0 minutes.
PCT/GB1996/002538 1995-10-16 1996-10-16 Procede d'extraction d'or comportant une bioflottation Ceased WO1997014818A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU73119/96A AU7311996A (en) 1995-10-16 1996-10-16 Gold extraction process including bioflotation

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ZA95/8716 1995-10-16
ZA958716A ZA958716B (en) 1995-10-16 1995-10-16 Process for extracting gold from mineral suspension

Publications (1)

Publication Number Publication Date
WO1997014818A1 true WO1997014818A1 (fr) 1997-04-24

Family

ID=25585361

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1996/002538 Ceased WO1997014818A1 (fr) 1995-10-16 1996-10-16 Procede d'extraction d'or comportant une bioflottation

Country Status (3)

Country Link
AU (1) AU7311996A (fr)
WO (1) WO1997014818A1 (fr)
ZA (1) ZA958716B (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1179604A3 (fr) * 2000-08-10 2002-07-10 Firma BIOMEDY AG Procédé pour extraire des métaux de minéraux par lixivation bactérielle
US6686202B2 (en) 2001-08-08 2004-02-03 Placer Dome, Inc. Methods for detecting and extracting gold
WO2009130006A1 (fr) 2008-04-21 2009-10-29 B.R.A.I.N. Biotechnology Research And Information Network Ag Exploitation minière écologique : procédé de biolixiviation et de bioadsorption de métaux précieux sans cyanure
WO2022071903A3 (fr) * 2020-08-21 2022-07-28 Eski̇şehi̇r Osmangazi̇ Üni̇versi̇tesi̇ Procédé d'amélioration de l'efficacité de flottation dans des minéraux carbonatés à l'aide d'un bioflotteur

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109576187B (zh) * 2018-12-27 2022-04-15 黄河三角洲京博化工研究院有限公司 一株氰化物降解菌株及利用该菌株降解氰化物的方法

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2157669A (en) * 1984-04-17 1985-10-30 Linde Ag Exploiting metal deposits of low concentrations
GB2180829A (en) * 1985-09-20 1987-04-08 Aurotech N L Precious metal extraction
US4729788A (en) * 1987-01-23 1988-03-08 Advanced Mineral Technologies, Inc. Thermophilic microbial treatment of precious metal ores
RU1527918C (ru) * 1987-10-06 1993-12-30 Центральный научно-исследовательский геологоразведочный институт цветных и благородных металлов Способ извлечени золота и серебра из продуктов бактериального выщелачивани железосульфидных концентратов
WO1994000608A1 (fr) * 1992-06-29 1994-01-06 Colin James Burns Lessivage electrocinetique
US5364453A (en) * 1992-09-22 1994-11-15 Geobiotics, Inc. Method for recovering gold and other precious metals from carbonaceous ores
RU2023729C1 (ru) * 1992-07-13 1994-11-30 Иркутский государственный научно-исследовательский институт редких и цветных металлов Способ переработки золотосодержащих сульфидных концентратов

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2157669A (en) * 1984-04-17 1985-10-30 Linde Ag Exploiting metal deposits of low concentrations
GB2180829A (en) * 1985-09-20 1987-04-08 Aurotech N L Precious metal extraction
US4729788A (en) * 1987-01-23 1988-03-08 Advanced Mineral Technologies, Inc. Thermophilic microbial treatment of precious metal ores
RU1527918C (ru) * 1987-10-06 1993-12-30 Центральный научно-исследовательский геологоразведочный институт цветных и благородных металлов Способ извлечени золота и серебра из продуктов бактериального выщелачивани железосульфидных концентратов
WO1994000608A1 (fr) * 1992-06-29 1994-01-06 Colin James Burns Lessivage electrocinetique
RU2023729C1 (ru) * 1992-07-13 1994-11-30 Иркутский государственный научно-исследовательский институт редких и цветных металлов Способ переработки золотосодержащих сульфидных концентратов
US5364453A (en) * 1992-09-22 1994-11-15 Geobiotics, Inc. Method for recovering gold and other precious metals from carbonaceous ores

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Week 9415, 1994 Derwent World Patents Index; AN 94-125224, XP002024842 *
DATABASE WPI Week 9527, 1995 Derwent World Patents Index; AN 95-205061, XP002024843 *
NIEVES IGLESIAS AND FRANCISCO CARRANZA: "Refractory gold-bearing ores: a review of treatment methods and recent advances in biotechnological techniques", HYDROMETALLURGY, vol. 34, no. 3, January 1994 (1994-01-01), AMSTERDAM, NL, pages 383 - 395, XP000430417 *

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1179604A3 (fr) * 2000-08-10 2002-07-10 Firma BIOMEDY AG Procédé pour extraire des métaux de minéraux par lixivation bactérielle
US6686202B2 (en) 2001-08-08 2004-02-03 Placer Dome, Inc. Methods for detecting and extracting gold
US6875254B2 (en) 2001-08-08 2005-04-05 University Of Washington Methods for detecting and extracting gold
AU2002300483B2 (en) * 2001-08-08 2008-09-25 Placer Dome, Inc Methods for detecting and extracting gold
AU2002300483B8 (en) * 2001-08-08 2008-10-23 Placer Dome, Inc Methods for detecting and extracting gold
WO2009130006A1 (fr) 2008-04-21 2009-10-29 B.R.A.I.N. Biotechnology Research And Information Network Ag Exploitation minière écologique : procédé de biolixiviation et de bioadsorption de métaux précieux sans cyanure
AU2009240211B2 (en) * 2008-04-21 2013-03-07 B.R.A.I.N. Biotechnology Research And Information Network Ag Green mining: process of cyanide-free bioleaching and bioadsorption of precious metals
WO2022071903A3 (fr) * 2020-08-21 2022-07-28 Eski̇şehi̇r Osmangazi̇ Üni̇versi̇tesi̇ Procédé d'amélioration de l'efficacité de flottation dans des minéraux carbonatés à l'aide d'un bioflotteur

Also Published As

Publication number Publication date
AU7311996A (en) 1997-05-07
ZA958716B (en) 1996-07-31

Similar Documents

Publication Publication Date Title
CA1159781A (fr) Recuperation microbiologique des metaux
CA1308916C (fr) Traitement de metaux precieux par procede aux bacteries thermophiles
Groudev Use of heterotrophic microorganisms in mineral biotechnology
Vasan et al. Some recent advances in the bioprocessing of bauxite
Abbruzzese et al. Biological and chemical processing of low-grade manganese ores
US5162105A (en) Processes to recover and reconcentrate gold from its ores with microorganisms
Deo et al. Biological removal of some flotation collector reagents from aqueous solutions and mineral surfaces
Matis et al. Flotation of cadmium‐loaded biomass
EP0432935B1 (fr) Procédé de récupération et reconcentration d'or de ses minerais
Yang et al. Pretreatment of deep-sea bacteria for reverse flotation of magnesite tailings: Cleaner production, behavior and mechanism
Mulligan et al. Bioremediation of metal contamination
Langhans et al. Biooxidation of an arsenic-bearing refractory gold ore
Qing Effect of biological pretreatment on flotation recovery of pyrolusite
CN1958815A (zh) 一种氧化镍钴矿的生物浸出工艺
CN105238925A (zh) 一种减少生物氧化工艺中金流失的方法
RU2603934C1 (ru) Способ очистки кварцевых песков от железа
Gupta et al. Selective and non-selective bioleaching of manganese from a manganese-containing silver ore
Vegliò et al. Batch and semi-continuous tests in the bioleaching of manganiferous minerals by heterotrophic mixed microorganisms
WO1997014818A1 (fr) Procede d'extraction d'or comportant une bioflottation
Natarajan Electrobioleaching of base metal sulfides
US20020037245A1 (en) Method for segregating metals and minerals from one another by leaching
Mulligan et al. Bioleaching of copper mining residues by Aspergillus niger
CN104525381A (zh) 一种微生物诱导铝土矿浮选脱硅的方法
Styriakova et al. Nutrients enhancing the bacterial iron dissolution in the processing of feldspar raw materials
RU2095453C1 (ru) Комбинированный безотходный способ переработки марганцевых руд

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AL AM AT AU AZ BB BG BR BY CA CH CN CU CZ DE DK EE ES FI GB GE HU IL IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MD MG MK MN MW MX NO NZ PL PT RO RU SD SE SG SI SK TJ TM TR TT UA UG US UZ VN AM AZ BY KG KZ MD RU TJ TM

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): KE LS MW SD SZ UG AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI

WWE Wipo information: entry into national phase

Ref document number: 320387

Country of ref document: NZ

121 Ep: the epo has been informed by wipo that ep was designated in this application
REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

122 Ep: pct application non-entry in european phase