industry as the first commercially available tertiary amine solvent extraction (SX) reagent for the recovery and concentration of uranium. Prior to 1957, ion exchange (IX) was the accepted route for the recovery of uranium from acid leach solutions.
Extraction Stripping LO BO PLS LE Raff RE Fig. 1. General flow diagram of the copper solvent extraction process. The copper transfer between the aqueous and organic phases takes place in mixers and the phases are separated in settlers. The equipment
Solvent extraction (SX) has been recognized as a one of the most important separation techniques for metals in solutions.The technology is increasingly being used in hy- drometallurgy to separate, purify and concentrate metals such as nickel, cobalt,
By McCabe Thiele diagram number of stages required for the counter current extraction of copper and zinc has been ... of copper and zinc by solvent extraction with Versatic 10 acid and Cyanex 272. 3. Results and Discussion 3.1. Solvent Extraction Sep
By McCabe Thiele diagram number of stages required for the counter current extraction of copper and zinc has been ... Solvent Extraction Separation of Copper and Zinc with Versatic 10 Acid 3.1.1. Effect of pH ... Solvent Extraction and Separation of
Abstract. A simultaneous distillation-solvent extraction (SDE) procedure was evaluated for the recovery of volatile compo nents from pasteurized orange juice. The Godefroot semi-micro SDE apparatus with methylene chloride solvent was used and extract
Accelerated solvent extraction (ASE), also referred to as pressurized fluid extrac-tion (PFE) and pressurized liquid extraction (PLE), is a liquid solvent extraction technique that uses aqueous and organic extraction solvents at elevated tempera-ture
extraction process. The result is faster extraction times and a significant reduction in solvent use. Many of the organic solvents used in extractions boil at relatively low temperatures. This is a limitation to techniques such as Soxhlet or automate
Solvent Extraction of Radionuclides from Aqueous Tank Waste Peter V. Bonnesen, Richard A. Sachleben, and Bruce A. Moyer, Oak Ridge National Laboratory Task Description The purpose of this task is to develop an efficient solvent-extraction and strippi
end, this study evaluated the efficacy of three techniques (accelerated solvent extraction [ASE], Soxhlet and so- nication) for the extraction of a large suite of synthetic and natural estrogens, androgens and progestogens, as
Copper Solvent Extraction
BASF LIX® technology – recovery of copper from leach solutions Leaching copper from oxide ores, low grade secondary sulfide ores, and primary sulfide concentrates with aqueous acid or ammonia solutions, followed by solvent extraction (SX) has been practiced commercially since the late 1960’s. Over time, LIX® Reagents (hydroxyoximes – chelating agents) used in these solvent extraction processes have become more efficient, more selective and more economical to use.
The benefits and objectives of the copper solvent extraction process are purification of copper, concentration of copper and conversion of the copper to a form that allows BASF’s customers to produce desired final metal products including cathode, powder and crystals. BASF produces a complete line of copper solvent extraction reagents, including ketoximes, aldoximes, non-modified blends and modified blends of ketoximes and aldoximes. These reagents and reagent blends allow BASF to supply its customers with an optimized reagent formulation tailored to meet the needs of their specific applications. The overall leaching, solvent extraction and final metal production processes can be summarized in the following simplified flowsheet.
LEACHING PROCESS / SOLVENT EXTRACTION / FINAL COPPER RECOVERY led leach soluti on cyc Re
ip p e
d L IX ® R e a g e
s strip solut ion ueou Aq
Pure copper product
lu t a l l e a ch s o
a ed LIX Re ®
n t ra t e
d d & purifie
FINAL COPPER RECOVERY
Advantages of BASF LIX® Reagents • Fast kinetics: Rapid copper uptake and copper stripping • Selective: Very high iron rejection • Net copper transfer: Can be adjusted to maximize process performance • Ease of operations: Cleaner phase separation and lower crud formation • High purity final copper product: Lower entrainment levels and lower transfer of contaminants • Low viscosity: Operate better at high reagent concentrations and low temperatures • Lower costs: Lower losses, higher net transfer, improved chemical stability
THE CHEMICAL STRUCTURES FOR THE KETOXIME AND ALDOXIME REAGENTS LIX® OXIME EXTRACTANTS OH
R Ketoxime R = C 9 H 25
R Aldoxime R = C 9 H 25 or C12 H 25
COPPER EQUILIBRIUM REACTION
Service All LIX® Reagents are backed by BASF’s comprehensive MSP® Minesite Services Program and BASF’s qualified e xperts and engineers.
Computer modeling The BASF Isocalc® computer simulation program provides plant operators with fast and accurate simulations of virtually any copper solvent extraction process involving sulfuric acid leaching followed by copper solvent extraction with LIX® Reagents. The Isocalc® program will generate extraction and stripping isotherms and construct McCabe-Thiele diagrams for a large number of circuit configurations. The program can also be calibrated to match the performance of commercial SX plants, which allows the production engineer to accurately determine the impact that changes in PLS chemistry, reagent concentration, reagent blend and /or circuit configuration will have on copper recovery.
2 RH(org) + Cu+2 SO42-(aq)
R2Cu(org) + 2H+1SO42-(aq)
Ketoximes: Moderately strong extractants and can be used without equilibrium modifiers. Aldoximes: Very strong extractants and have to be used in mixture with an equilibrium modifier or ketoxime to aid the stripping process and obtain adequate net copper transfer. LIX® Reagents work on a hydrogen ion cycle. Acid is generated in electrowinning, transferred to the organic in stripping in exchange for copper and then exchanged for copper in extraction.
Final Copper Cathode product bundled, weighed and ready for shipment.
Equilibrium extraction isotherm / two stage McCabe-Thiele diagram with a typical LIX® Reagent
Equilibrium strip isotherm /one strip stage McCabe-Thiele diagram with a typical LIX® Reagent 60
40 S. E. 30
2.0 S. O. 1.0
0.0 Raff. = 0.22
Aqueous g / l copper
Loaded organic = 3.90 g / l Cu
S. O. = 1.77
Aqueous g / l copper
P. E. Feed = 2.50 g / l Cu
Organic g / l copper
Organic g / l copper
SX plant configurations and final copper product Commercial copper SX plants are designed around one of the several proven circuit configurations: series, series parallel, modified series parallel and optimum series parallel (or interlaced). The circuit configuration chosen will depend on several variables unique to the site including economics, leach solution chemistry and the operating philosophy of the company associated with each plant. The solvent extraction process can produce several different final copper products, however, most SX plants produce copper cathode.
The descriptions, designs, data and information contained herein are presented in good faith, and are based on BASF’s current knowledge and experience. They are provided for guidance only, and do not constitute the agreed contractual quality of the product or a part of BASF’s terms and conditions of sale. Because many factors may affect processing or application /use of the product, BASF recommends that the reader carry out its own investigations and tests to determine the suitability of a product for its particular purpose prior to use. It is the responsibility of the recipient of product to ensure that any proprietary rights and existing laws and legislation are observed. No warranties of any kind, either express or implied, including, but not limited to, warranties of merchantability or fitness for a particular purpose, are made regarding products described or designs, data or information set forth herein, or that the products, descriptions, designs, data or information may be used without infringing the intellectual property rights of others. Any descriptions, designs, data and information given in this publication may change without prior information. The descriptions, designs, data, and information furnished by BASF hereunder are given gratis and BASF assumes no obligation or liability for the descriptions, designs, data or information given or results obtained, all such being given and accepted at the reader’s risk. ( 10/ 2017) ® = registered trademark of BASF SE