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RECOVERY SILVER AND GOLDBY DIRECT OXIDATIVE PRESSURE
CYANIDATION
by
Jose R. Parga and Jesus L. Valenzuela
3rd International Conference SDIMI
June 2007, Milos Island, Greece.
CYANIDE PROCESS CYANIDE PROCESS The McArthurThe McArthur--Forrest Process (1887)Forrest Process (1887)
Is a metallurgical technique for extracting gold Is a metallurgical technique for extracting gold from low grade ore by converting the gold to from low grade ore by converting the gold to water soluble aurocyanide metallic complex ionswater soluble aurocyanide metallic complex ions
Leaching Time
42 -72 hrs.
REFRACTING OREREFRACTING ORE(Recovery less than 60 %)(Recovery less than 60 %)
IMPROVED TREATMENT PROCESSES:IMPROVED TREATMENT PROCESSES:Fluid Bed RoastingFluid Bed RoastingWhole Ore RoastingWhole Ore RoastingPressure LeachingPressure LeachingBiological OxidationBiological Oxidation
Refractory Gold & Silver OresRefractory Gold & Silver Ores
Oxidative Pretreatment
Direct Leaching
Atmospheric Acid Leaching
Acid LeachingHigh Pressure
AlkalineCyanidation
High Pressure
Chemical Oxidation
Biological Oxidation
Whole OreRoasting
Leaching Gold & Silver
Carbon in Leach
Other LixiviantsThiourea,Thiosulfate
Alkaline Cyanidation &
OxigenHigh Pressure
Bulk Flotation GrindingDirect Oxidative
Pressure Cyanidation90 Minutes
Au(CN)-2
NEW TECHNOLOGY
PRESSURE LEACHING PROCESS
CHEMICAL AND MINERALOGICAL ANALYSISCHEMICAL AND MINERALOGICAL ANALYSISg/ton %
Au Ag Pb Zn Cu Fe As S
Concentrate 87.09 12320 2.6 3.8 0.5 29.2 0.15 32
Ore 4.12 289 0.5 0.4 0.04 3.67 0.1 3.7
THE MINERALOGICAL ANALYSIS ARE:- Silver Iron Sulfide- Argentite , Pyrite- Pyrrhotite, Arsenopyrite- Chalcopyrite, Covellite - Hematite and Magnetite- Quartz and Calcite
Schematic mechanism of gold and silver leaching60 minutes
GALENA
ARGENTITE
ARGENTITE
PYRITEPARTICLE
ARGENTITE
CN-
Ag(CN)2-
15O2 + 2H2O 2Fe(SO4)2 + 2H2SO4
GOLD
CN-
Au(CN)2-
SPHALERITE
Fe2(SO4)3
O2
CN-
Ag(CN)2-
Fe3+Zn2+
SIMULTANEOUSLY OXIDATIONSIMULTANEOUSLY OXIDATIONAND CYANIDATION LEACHINGAND CYANIDATION LEACHING
The primary reactions are:The primary reactions are:
2FeS2FeS2 2 + 7O+ 7O2 2 + 2H+ 2H22O = 2FeO = 2Fe2+2+ + 4SO+ 4SO4422-- + 4H+ 4H++ (1)(1)
FeSFeS22 + 2H+ 2H++ = Fe= Fe2+2+ + H+ H22S + SS + S00 (2)
Ferrous ions produced by reaction (1) and (2)Ferrous ions produced by reaction (1) and (2)are subsequently oxidized to ferric ions:are subsequently oxidized to ferric ions:
2Fe2Fe2+2+ + + 1/21/2OO22 + 2H+ 2H++ = 2Fe= 2Fe3+3+ + H+ H22O O
The ferric ions an also contribute to the oxidationThe ferric ions an also contribute to the oxidationof silver iron sulfide, argentite, pyrite, pyrrhotite,of silver iron sulfide, argentite, pyrite, pyrrhotite,
sphalerite and chalcopyrite:sphalerite and chalcopyrite:
AgFeAgFe22SS33 + Fe+ Fe3+3+ == AgAg++ + 3 Fe+ 3 Fe2+2+ + 2S+ 2S22-- + S+ S00
AgAg22S + 2FeS + 2Fe3+3+ = 2Ag= 2Ag++ + 2Fe+ 2Fe2+2+ + S+ S00
ZnS + 2FeZnS + 2Fe3+3+ = Zn= Zn2+2+ + 2Fe+ 2Fe2+2+ + S+ S00
CuFeSCuFeS22 + 4Fe+ 4Fe3+3+ = Cu= Cu2+2+ + 5Fe+ 5Fe2+2+ + 2S+ 2S00
Then, elemental sulfur may also be further oxidized to Then, elemental sulfur may also be further oxidized to sulfate by oxygen or by ferric sulfate:sulfate by oxygen or by ferric sulfate:
2S2S00 + 3O+ 3O22 + 2 = 4H+ 2 = 4H++ + 2SO+ 2SO4422--
SS00 + 6Fe+ 6Fe3+3+ + 4H+ 4H22O = 6FeO = 6Fe2+2+ + 8H+ 8H++ + SO+ SO4422--
This results in the formation of a porous,but nonprotective, eleThis results in the formation of a porous,but nonprotective, elemental mental sulfur layer, thus allowing cyanide and dissolved oxygen to accesulfur layer, thus allowing cyanide and dissolved oxygen to access to ss to the previously locked gold, silver and electrumthe previously locked gold, silver and electrum
AgAg22S + 4CNS + 4CN-- = 2Ag(CN)= 2Ag(CN)--22 + S+ S22--
4 4 Au + 8CNAu + 8CN-- + O+ O22 + H+ H22O = 4Au(CN)O = 4Au(CN)--22 + 4OH+ 4OH--
Comparison of silver extraction at ambient conditions and high pressure
0
20
40
60
80
100
0 50 100 150 200 250 300 350
TIME (min)
EXTR
ACT
ION
, %
S ILVER 80 C(80 psi)
S ILVER (N.C.)
C ON D ITION S%S olids = 20pH= 11.0P re ssure = 80 psi
rpm = 300
Te mp. = 80 oC
Comparison of gold extraction at ambient Comparison of gold extraction at ambient conditions and high pressureconditions and high pressure
0
20
40
60
80
100
0 30 60 90 120 150 180 210 240 270 300
TIME (min)
EXTR
ACT
ION
, % GOLD 80 p s i80 oC GOLD (1 atm)
25 οC
Effect of autoclave retention time on gold and Effect of autoclave retention time on gold and silver extractionsilver extraction
85
90
95
100
15 30 45 60 75 90 105 120
AUTOCLAVE RETENTION TIME (minutes)
EXTR
ACT
ION
, % GOLD
SILVER
C ON D ITION S%So lids = 20pH = 11.7P res s ure = 80ps irpm = 300Temp. = 80 C
Effect of the cyanide concentration on gold and Effect of the cyanide concentration on gold and silver extractionsilver extraction
50
60
70
80
90
100
0,4 0,6 0,8 1 1,2
CYANIDE CONCENTRATION, %
EXTR
ACT
ION
, %
GOLD
SILVER
C ON D ITION S% So lids = 20pH = 11.7Temp. = 80oCP res s ure = 80 ps irpm = 300leach time = 60 min.
Effect of temperature on gold Effect of temperature on gold and silver extractionand silver extraction
0
20
40
60
80
100
50 100 150 200 250TEMPERATURE, oC
EXTR
ACT
ION
. % GOLDSILVER
C ON D ITION S% So lids = 20pH = 11.2P res s ure = 80 ps irpm = 300leach time = 60 min.
Effect of pH on gold and silver extractionEffect of pH on gold and silver extraction
90
92
94
96
98
100
10 10,5 11 11,5 12 12,5 13 13,5
pH
EXTR
ACT
ION
, %
GOLD
SILVER
C ON D ITION S% So lids = 20Temp. = 80 oCP res s ure = 80 ps irpm = 300NaCN = 1%leach time = 60 min.
Effect of percent solids in the extractionEffect of percent solids in the extractionof gold and silverof gold and silver
0
20
40
60
80
100
0 5 10 15 20 25 30 35
% SOLIDS
EXTR
ACT
ION
, % GOLD
SILVER
CONDITIONSTemp. = 80 oCpH = 11.2P ressure = 80 ps irpm = 300NaCN = 1 %leach time = 60 min.
Results of continuous plant operationResults of continuous plant operation
9394
9596
9798
99
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30
DAYS
EXTR
ACT
ION
, %
SILVER GOLD
CONCLUSIONSCONCLUSIONS
The present study shows that, gold and silver values are The present study shows that, gold and silver values are associated with silver iron sulfide, argentite, pyrite, associated with silver iron sulfide, argentite, pyrite, pyrrhotitepyrrhotite, , sphaleritesphalerite and chalcopyrite in the and chalcopyrite in the BacBacííssconcentrate.concentrate.
The dissolution of gold and silver are due to the strong The dissolution of gold and silver are due to the strong complexingcomplexing capabilities of cyanide anions combined with capabilities of cyanide anions combined with the oxidizing properties of the dissolved molecular oxygenthe oxidizing properties of the dissolved molecular oxygen..
The kinetics of the direct pressure oxidation/The kinetics of the direct pressure oxidation/cyanidationcyanidation was was found to be strongly dependent on particle size, found to be strongly dependent on particle size, concentration of sodium cyanide, temperature and pH.concentration of sodium cyanide, temperature and pH.
Single stage direct pressure oxidation/Single stage direct pressure oxidation/cyanidationcyanidation, has , has proven to be effective in treating pyrite refractory gold and proven to be effective in treating pyrite refractory gold and silver concentrates from silver concentrates from BacBacííss mining, for both gold and mining, for both gold and silver it was found that the precious metals recovery silver it was found that the precious metals recovery exceeded 96%.exceeded 96%.
The relatively mild operating conditions of 80 The relatively mild operating conditions of 80 °°C and 80 C and 80 psipsioxygen pressure offer distinct advantages. oxygen pressure offer distinct advantages. For example, low cost materials of construction can be For example, low cost materials of construction can be utilized for the autoclaveutilized for the autoclave..
Finally in this process, there is obviously lower gold and Finally in this process, there is obviously lower gold and silver inventorysilver inventory..
JesJesúús L. Valenzuelas L. ValenzuelaDept. Chemical Engng. & Metallurgy,Dept. Chemical Engng. & Metallurgy,University of Sonora, University of Sonora, Hermosillo, Sonora, MexicoHermosillo, Sonora, [email protected]@iq.uson.mx
JosJoséé R. PargaR. PargaDept. of Metallurgy and Mater. Sci.,Dept. of Metallurgy and Mater. Sci.,Institute Technology of Saltillo, Institute Technology of Saltillo, Saltillo, Coahuila MexicoSaltillo, Coahuila Mexico
HHééctor Moreno and David L. Cockector Moreno and David L. CockeDept. Chemistry, Lamar University, Dept. Chemistry, Lamar University, Beaumont, Texas, USBeaumont, Texas, US
Thank you for your attention
POTENCIAL DE CRECIMIENTO
10 nuevos proyectos mineros en operaciónen el período 2004-2009
PROYECTO EL CHANATEO r o
PROYECTO CERRO COLORADO
O r o PROYECTO LLUVIA DE OROO r o
PROYECTO MILPILLASCobre
PROYECTO MARIQUITA
Cobre
PROYECTO BACADEHUACHI
Sulfato de Sodio
PROYECTO MULATOSO r o
PROYECTO SAN ANTONIOO r o, Cobre
PROYECTO PIEDRAS VERDES
Cobre PROYECTO ALAMO DORADO
P l a t a