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Describing relationship between concentration and purification 
units with solvent extraction. 
Supervisor 
Dr . Karimi 
Hamid faramarzi 
926181008 
Imam Khomeini International 
University, Qazvin, Iran. 
1
Content 
2 
Introduction 
Steps for Concentration and purification 
Solid-Liquid Separation 
 Separation & Purification 
Solvent extraction 
Examples for Concentration and purification 
 Concentration and purification copper 
Concentration and purification zinc 
Concentration and purification uranium 
Conclusion 
Reference
3 
Leaching processes are rarely, if ever, completely selective and, therefore, 
pregnant leach solutions contain impurities and will almost always require 
purification prior to final metal winning.[4] 
Solvent extraction is now a very well-established process in hydrometallurgy. It is 
used for the hydrometallurgical processing of copper, nickel, cobaIt, zinc, 
uranium and etc.[4] 
Iron removal from nickel-cobalt process liquors, is one case.[4] 
3 
Introduction
4 
solution purification which obtained from depending on the number and 
concentration of interfering ions in solution is done in many different ways had 
the concentration of impurities in solution obtaind from leaching process be 
specific excessive it would caused some problems in electrowining recovery.[2] 
4 
Introduction
5 
Steps for 
Concentration 
and purification 
Solid-Liquid 
Separation 
Filtration 
(incl micro-and 
nano - 
filtration) 
Thickening & 
clarification 
(incl 
coagulation, 
flocculation) 
Counter-current 
decantation 
Flocculation 
5 
[8]
Steps for 
Concentration 
and purification 
Separation & 
Purification 
Ion Exchange Solvent 
Extraction 
Adsorption 
on Carbon 
Precipitation 
of Impurities 
6 
[8]
7 
Solvent 
extraction 
The net result of the technology involving the three principal stages, namely, 
extraction, scrubbing and stripping, is the separation of an impure aqueous 
stream into two aqueous streams, one containing most of the impurities and the 
other containing most of the valuable metal ions. 
Solvent extraction provides the means for producing pure, high Cu" electrolytes 
from dilute, impure pregnant leach solutions. It is a crucial step in the 
production of -2.5 million tonnes of metallic copper per year.[9]
8 
Solvent extraction is used for separation and concentration of metal ions in aqueous 
solutions. The method is based on that an extraction agent, diluted with an organic 
solvent, is mixed by stirring or shaking with an aqueous solution containing the desired 
metal. The extraction agent and the organic solvent are both insoluble in water.. 
By mixing the aqueous and organic phase, the metal ion binds to the extraction agent 
and is transferred to the organic phase. Thereafter, the organic and aqueous phases are 
allowed to disengage and then the two phases are separated.[9] 
8 
Solvent 
extraction
9 
The organic extractant removes Cu++ from pregnant leach solution by the reaction 
So contact of dilute H2so4 aqueous pregnant leach solution with organic gives 
extraction of Cu from the aqueous phase into the organic phase.[5] 
9 
Solvent 
extraction
10 
From the reactions above it is apparent that the pH dependence for extraction and 
stripping is greater for Fe3+ than for Cu2+,. By using a pH between 1.5 and 2.0 Cu2+ 
can be extracted selectively.[3] 
10 
Solvent 
extraction
11 
Concentration 
and purification 
of copper 
The pregnant leach solutions produced by most leaching operations are: 
(a) too dilute in Cu (1-6 kg Cu/m3) and: (b) too impure (1 - 10 kg Fe/m3) 
for direct electrodeposition of high purity cathode copper.[5] 
This high concentration of Cu: 
(a) ensures that CU++ ions are always available for plating at the cathode surface 
(b) gives smooth, dense, high purity, readily marketable cathode copper.[5] 
11
12 
Schematic plan view of copper solvent extraction circuit. 
Solvent extraction circuit that has been perturbed by receiving 3.3 kg Cu/ M3 pregnant leach 
solution.[5] 
12 
Concentration 
and purification 
of copper
13 
Copper solvent extraction mixer-settler. The two mixing compartments, the large settler and the organic 
overflow/aqueous underflow system are notable.[5] 
13 
Concentration 
and purification 
of copper
14 
Rejection of Fe and other impurities 
An efficient extractant must carry Cu forward from pregnant leach solution to 
electrolyte while not forwarding impurities, particularly Fe, Mn and CI. [9] 
Industrial electrowinning requires pure, Cu-rich electrolytes with >35 kg Cu/m3. 
Electrowinning. [9] 
14 
Concentration 
and purification 
of copper
One of the main influence impurities in Hydrometallurgical method zinc is producing iron. 
Concentration and purification of zinc I done in two steps: 
1- sedimenting iron ion 
2- eliminating impurities by the powder of zinc . (cementation) [10] 
1- iron prevent from dissolution some parts of zinc and reduce the 
recovery 
2- iron ion act as a disrupting thing.[10] 
The best qualification of ph for sedimenting ferric hydroxide is 5-5.5 
With iron residual most of impurities such as As , Sb , Ge , will 
sediment.[11] 
15 
Concentration 
and purification 
of zinc 
Removal of iron from the leach solution:
16 
Mn impurities in the pregnant solution reduces recovery of the organic phase and 
electrolyte Raffinate. 
Element name g/l 
Cadmium 0.002 - 0.004 
Copper 0.0001 – 0.0005 
Iron 0.02 – 0.03 
Arsenic 0.0001 
Antimony 0.0001 
Cobalt 0.003 – 0.007 
Manganese Less than 0.7 
Concentration 
and purification 
of zinc 
Permitted levels of elements in the input solution Electro wining [11] 
16
17 
Extraction mechanism equation 
Zinc concentration in the aqueous phase (g/lit) [11] 
17 
Concentration 
and purification 
of zinc
18 
Number of extraction are three stages 
ion manganese iron copper zinc 
Concentration 
( g / lit) 
0.154 0.0094 0.001 15 
The final concentration of electrolyte ions in the washing of the organic 
phase .[11] 
18 
Concentration 
and purification 
of zinc
19 
Concentration 
and purification 
of uranium 
19 
Solvent extraction is a common technique used to recover uranium from sulphuric acid 
leach liquors. The tertiary amines are selective for uranium in the presence of impurities 
such as iron thorium , phosphate and rare earths.[6] 
[7]
20 
20 
Concentration 
and purification 
of uranium 
The presence of chloride in Sulfuric acid leach liquors has a negative impact 
on the solvent extraction process for the recovery of uranium using tertiary 
amine reagents.[1] 
In practice, the chloride concentration in process liquors tends to be limited to <3 g/L 
chloride, so as not to significantly affect uranium solvent loading.[11]
21 
conclusion 
1) Solvent extraction is now a very well-established process in hydrometallurgy. 
2) Steps for Concentration and purification. 
Solid-Liquid Separation 
 Separation & Purification 
3) is the separation of an impure aqueous stream into two aqueous streams, one 
containing most of the impurities and the other containing most of the valuable 
metal ions. 
4) By mixing the aqueous and organic phase, the metal ion binds to the extraction 
agent and is transferred to the organic phase . 
5) An efficient extractant must carry Cu forward from pregnant leach solution to 
electrolyte while not forwarding impurities, particularly Fe, Mn and CI. 
6) One of the main influence impurities in Hydrometallurgical method is producing 
iron. 
7) Solvent extraction is a common technique used to recover uranium from sulphuric 
acid leach liquors. 
8) In practice, the chloride concentration in process liquors tends to be limited to <3 
g/L chloride.
22 
22 
References 
[1] Concentration–Purification of Uranium from an Acid LeachingSolution. 
H. Guettaf*, A.Becis, K. Ferhat, K. Hanou, D. Bouchiha, K. Yakoubi and F. Ferrad. 2009 
[2] A short history of hydrometallurgy Fathi Habashi 
Department of Mining, Metallurgical, and Materials Engineering, Laval University. 
[3] Hydrometallurgy solvent extraction of Cu2+ using LIX-984 
[4] Unit processes in extractive metallurgy , Robert D. Pehlke. 
[5] Extractive Metallurgy of Copper, W.G.Davenport , M. king , M.schlesinger , A.K. biswas. 
[6] Solvent extraction of uranium from saline leach liquors using DEHPA/Alamine 336 
mixed reagent James E. Quinn, Deborah Wilkins, Karin H. Soldenhoff, 
Hydrometallurgy vol 134–135 (2013) 74–79 
[7] Uranium Extraction Technology , International Atomic Energy Agency , VIENNA ,1993.
23 
[8] http://www.parkercentre.com.au/hydrometallurgy/classification-of-processes-in-hydrometallurgy 
[9] Chemical Metallurgy , Chiranjib Kumar Gupta , 2003 
10 ] تولید فلز روی به روش هیدرومتالورژی , سعید مرادی دانشجوی ارشد تربیت مدرس , 1378 ] 
11 ] عوامل موثر بر استخراج حلالی روی از محلول حاوی یونهای آهن و منگنز محمد رضا بلور فرش , منوچهر ] 
اولیازاده , خداکرم غریبی , 1386 
References 
23
Thank from your attention. 
Slide 24

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Concentration and Purification Processes Using Solvent Extraction

  • 1. Describing relationship between concentration and purification units with solvent extraction. Supervisor Dr . Karimi Hamid faramarzi 926181008 Imam Khomeini International University, Qazvin, Iran. 1
  • 2. Content 2 Introduction Steps for Concentration and purification Solid-Liquid Separation  Separation & Purification Solvent extraction Examples for Concentration and purification  Concentration and purification copper Concentration and purification zinc Concentration and purification uranium Conclusion Reference
  • 3. 3 Leaching processes are rarely, if ever, completely selective and, therefore, pregnant leach solutions contain impurities and will almost always require purification prior to final metal winning.[4] Solvent extraction is now a very well-established process in hydrometallurgy. It is used for the hydrometallurgical processing of copper, nickel, cobaIt, zinc, uranium and etc.[4] Iron removal from nickel-cobalt process liquors, is one case.[4] 3 Introduction
  • 4. 4 solution purification which obtained from depending on the number and concentration of interfering ions in solution is done in many different ways had the concentration of impurities in solution obtaind from leaching process be specific excessive it would caused some problems in electrowining recovery.[2] 4 Introduction
  • 5. 5 Steps for Concentration and purification Solid-Liquid Separation Filtration (incl micro-and nano - filtration) Thickening & clarification (incl coagulation, flocculation) Counter-current decantation Flocculation 5 [8]
  • 6. Steps for Concentration and purification Separation & Purification Ion Exchange Solvent Extraction Adsorption on Carbon Precipitation of Impurities 6 [8]
  • 7. 7 Solvent extraction The net result of the technology involving the three principal stages, namely, extraction, scrubbing and stripping, is the separation of an impure aqueous stream into two aqueous streams, one containing most of the impurities and the other containing most of the valuable metal ions. Solvent extraction provides the means for producing pure, high Cu" electrolytes from dilute, impure pregnant leach solutions. It is a crucial step in the production of -2.5 million tonnes of metallic copper per year.[9]
  • 8. 8 Solvent extraction is used for separation and concentration of metal ions in aqueous solutions. The method is based on that an extraction agent, diluted with an organic solvent, is mixed by stirring or shaking with an aqueous solution containing the desired metal. The extraction agent and the organic solvent are both insoluble in water.. By mixing the aqueous and organic phase, the metal ion binds to the extraction agent and is transferred to the organic phase. Thereafter, the organic and aqueous phases are allowed to disengage and then the two phases are separated.[9] 8 Solvent extraction
  • 9. 9 The organic extractant removes Cu++ from pregnant leach solution by the reaction So contact of dilute H2so4 aqueous pregnant leach solution with organic gives extraction of Cu from the aqueous phase into the organic phase.[5] 9 Solvent extraction
  • 10. 10 From the reactions above it is apparent that the pH dependence for extraction and stripping is greater for Fe3+ than for Cu2+,. By using a pH between 1.5 and 2.0 Cu2+ can be extracted selectively.[3] 10 Solvent extraction
  • 11. 11 Concentration and purification of copper The pregnant leach solutions produced by most leaching operations are: (a) too dilute in Cu (1-6 kg Cu/m3) and: (b) too impure (1 - 10 kg Fe/m3) for direct electrodeposition of high purity cathode copper.[5] This high concentration of Cu: (a) ensures that CU++ ions are always available for plating at the cathode surface (b) gives smooth, dense, high purity, readily marketable cathode copper.[5] 11
  • 12. 12 Schematic plan view of copper solvent extraction circuit. Solvent extraction circuit that has been perturbed by receiving 3.3 kg Cu/ M3 pregnant leach solution.[5] 12 Concentration and purification of copper
  • 13. 13 Copper solvent extraction mixer-settler. The two mixing compartments, the large settler and the organic overflow/aqueous underflow system are notable.[5] 13 Concentration and purification of copper
  • 14. 14 Rejection of Fe and other impurities An efficient extractant must carry Cu forward from pregnant leach solution to electrolyte while not forwarding impurities, particularly Fe, Mn and CI. [9] Industrial electrowinning requires pure, Cu-rich electrolytes with >35 kg Cu/m3. Electrowinning. [9] 14 Concentration and purification of copper
  • 15. One of the main influence impurities in Hydrometallurgical method zinc is producing iron. Concentration and purification of zinc I done in two steps: 1- sedimenting iron ion 2- eliminating impurities by the powder of zinc . (cementation) [10] 1- iron prevent from dissolution some parts of zinc and reduce the recovery 2- iron ion act as a disrupting thing.[10] The best qualification of ph for sedimenting ferric hydroxide is 5-5.5 With iron residual most of impurities such as As , Sb , Ge , will sediment.[11] 15 Concentration and purification of zinc Removal of iron from the leach solution:
  • 16. 16 Mn impurities in the pregnant solution reduces recovery of the organic phase and electrolyte Raffinate. Element name g/l Cadmium 0.002 - 0.004 Copper 0.0001 – 0.0005 Iron 0.02 – 0.03 Arsenic 0.0001 Antimony 0.0001 Cobalt 0.003 – 0.007 Manganese Less than 0.7 Concentration and purification of zinc Permitted levels of elements in the input solution Electro wining [11] 16
  • 17. 17 Extraction mechanism equation Zinc concentration in the aqueous phase (g/lit) [11] 17 Concentration and purification of zinc
  • 18. 18 Number of extraction are three stages ion manganese iron copper zinc Concentration ( g / lit) 0.154 0.0094 0.001 15 The final concentration of electrolyte ions in the washing of the organic phase .[11] 18 Concentration and purification of zinc
  • 19. 19 Concentration and purification of uranium 19 Solvent extraction is a common technique used to recover uranium from sulphuric acid leach liquors. The tertiary amines are selective for uranium in the presence of impurities such as iron thorium , phosphate and rare earths.[6] [7]
  • 20. 20 20 Concentration and purification of uranium The presence of chloride in Sulfuric acid leach liquors has a negative impact on the solvent extraction process for the recovery of uranium using tertiary amine reagents.[1] In practice, the chloride concentration in process liquors tends to be limited to <3 g/L chloride, so as not to significantly affect uranium solvent loading.[11]
  • 21. 21 conclusion 1) Solvent extraction is now a very well-established process in hydrometallurgy. 2) Steps for Concentration and purification. Solid-Liquid Separation  Separation & Purification 3) is the separation of an impure aqueous stream into two aqueous streams, one containing most of the impurities and the other containing most of the valuable metal ions. 4) By mixing the aqueous and organic phase, the metal ion binds to the extraction agent and is transferred to the organic phase . 5) An efficient extractant must carry Cu forward from pregnant leach solution to electrolyte while not forwarding impurities, particularly Fe, Mn and CI. 6) One of the main influence impurities in Hydrometallurgical method is producing iron. 7) Solvent extraction is a common technique used to recover uranium from sulphuric acid leach liquors. 8) In practice, the chloride concentration in process liquors tends to be limited to <3 g/L chloride.
  • 22. 22 22 References [1] Concentration–Purification of Uranium from an Acid LeachingSolution. H. Guettaf*, A.Becis, K. Ferhat, K. Hanou, D. Bouchiha, K. Yakoubi and F. Ferrad. 2009 [2] A short history of hydrometallurgy Fathi Habashi Department of Mining, Metallurgical, and Materials Engineering, Laval University. [3] Hydrometallurgy solvent extraction of Cu2+ using LIX-984 [4] Unit processes in extractive metallurgy , Robert D. Pehlke. [5] Extractive Metallurgy of Copper, W.G.Davenport , M. king , M.schlesinger , A.K. biswas. [6] Solvent extraction of uranium from saline leach liquors using DEHPA/Alamine 336 mixed reagent James E. Quinn, Deborah Wilkins, Karin H. Soldenhoff, Hydrometallurgy vol 134–135 (2013) 74–79 [7] Uranium Extraction Technology , International Atomic Energy Agency , VIENNA ,1993.
  • 23. 23 [8] http://www.parkercentre.com.au/hydrometallurgy/classification-of-processes-in-hydrometallurgy [9] Chemical Metallurgy , Chiranjib Kumar Gupta , 2003 10 ] تولید فلز روی به روش هیدرومتالورژی , سعید مرادی دانشجوی ارشد تربیت مدرس , 1378 ] 11 ] عوامل موثر بر استخراج حلالی روی از محلول حاوی یونهای آهن و منگنز محمد رضا بلور فرش , منوچهر ] اولیازاده , خداکرم غریبی , 1386 References 23
  • 24. Thank from your attention. Slide 24