The Testing Results of ACORGA, LIX Extractants and CR60 Crud Mitigation Reagent Influence during SX-EW Copper Extraction
Tatyana Chepushtanova,
Meiyrbek Yessirkegenov,
Yelena Bochevskaya,
Ainash Sharipova,
Omirserik Baigenzhenov (),
Yerik Merkibayev and
Aliya Altmyshbayeva
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Tatyana Chepushtanova: Metallurgical Process, Heat Engineering and Technology of Special Materials Department, Satbayev University, Almaty 050013, Kazakhstan
Meiyrbek Yessirkegenov: Metallurgical Process, Heat Engineering and Technology of Special Materials Department, Satbayev University, Almaty 050013, Kazakhstan
Yelena Bochevskaya: JSC Institute of Fuel, Catalysis and Electrochemistry Named after. D.V. Sokolsky, Sector of Rare Trace Elements, Almaty 050010, Kazakhstan
Ainash Sharipova: JSC Institute of Fuel, Catalysis and Electrochemistry Named after. D.V. Sokolsky, Sector of Rare Trace Elements, Almaty 050010, Kazakhstan
Omirserik Baigenzhenov: Metallurgical Process, Heat Engineering and Technology of Special Materials Department, Satbayev University, Almaty 050013, Kazakhstan
Yerik Merkibayev: Metallurgical Process, Heat Engineering and Technology of Special Materials Department, Satbayev University, Almaty 050013, Kazakhstan
Aliya Altmyshbayeva: Metallurgical Process, Heat Engineering and Technology of Special Materials Department, Satbayev University, Almaty 050013, Kazakhstan
Sustainability, 2024, vol. 16, issue 17, 1-17
Abstract:
Research analysis reveals factors influencing third-phase crud formation and composition during metal extraction, including solution composition, solid suspensions, organic compounds, colloidal compounds (e.g., silicic acid), and extractant purity. Compositional analysis of copper-containing sulfuric acid solutions (1.25 g/dm 3 copper) identifies principal sulfate-forming components. Copper extraction was studied using extractants LIX 984N, ACORGA M5774, and M5640 at different ratios of the organic phase to the aqueous O:A (from 1:2 to 1:10). Suppressive impact of 10 vol.% CR60 additive on third-phase crud formation during copper extraction with LIX 984N, ACORGA M5774, and M5640 is analyzed, with ACORGA M5774 being the most effective. Physicochemical analysis characterizes CR60’s active substance as poly(sodium 4-styrenesulfonate) with steel-suppression properties, and its structural formula is determined. Optimal copper extraction conditions establish ACORGA M5640’s 24% efficiency, followed by ACORGA M5774 at 15%. CR60 reduces crud formation, with 5 cm 3 of ACORGA CR60 added to sulfuric acid solution reducing interfacial crud formation by 2–3 times. Optimal extraction parameters include 1:2 O:A ratio, 20 ± 5 °C temperature, 5 cm 3 CR60 additive, 5 min process duration, and 1-day settling time. ACORGA M5774 (10 vol.% in kerosene) is recommended as an extractant, with 2–3 stages of countercurrent extraction.
Keywords: productive copper-containing sulfate solution; solvent extraction; extractant; crud (search for similar items in EconPapers)
JEL-codes: O13 Q Q0 Q2 Q3 Q5 Q56 (search for similar items in EconPapers)
Date: 2024
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