Journal of Siberian Federal University. Engineering & Technologies / Efficiency Improvement for Platinum Concentrates Production from Electrolytic Slimes at Polar Division of OAO MMC Norilsk Nickel

Full text (.pdf)
Issue
Journal of Siberian Federal University. Engineering & Technologies. 2013 6 (7)
Authors
Lapshin, Dmitry A.; Grabchak, Eduard F.; Kuzmina, Irina S.; Goryacheva, Yuliya A.; Kozhanov, Aleksandr L.
Contact information
Lapshin, Dmitry A.:Polar Division of OAO MMC Norilsk Nickel, PO 4324, 8 Leninsky, Norilsk, 663300 Russia;E-mail: ; Grabchak, Eduard F.:Polar Division of OAO MMC Norilsk Nickel, PO 4324, 8 Leninsky, Norilsk, 663300 Russia; Kuzmina, Irina S.:Polar Division of OAO MMC Norilsk Nickel, PO 4324, 8 Leninsky, Norilsk, 663300 Russia; Goryacheva, Yuliya A.:Polar Division of OAO MMC Norilsk Nickel, PO 4324, 8 Leninsky, Norilsk, 663300 Russia; Kozhanov, Aleksandr L.:Polar Division of OAO MMC Norilsk Nickel, PO 4324, 8 Leninsky, Norilsk, 663300 Russia
Keywords
slime; concentrates; PGM
Abstract

Slime processing at PD OAO MMC Norilsk Nickel involves oxidizing-sulphatizing roasting, calcine leaching with sulphate solution, calcine cake smelting into anodes followed by electrolytic dissolution, and a number of processes designed for accompanying elements recovery. Resulting final products are platinum-palladium (60-65 % Σ Pt+Pd) and rhodium-ruthenium (2.0-3.5 % Rh) concentrates (KP-1 and KP-2, respectively), refined silver, selenium of technical grade and tellurium. Process cycle duration, considerable work-in-process amount, a great number of operations and low efficiency of individual operations are considered to be disadvantages of the slimes processing method. We determined optimal process conditions for copper slimes calcine cake repulping with sulphate (reagents, consumption and sodium hypochlorite feed rate) offering 6-7 fold increase of Pt recovery into solution and 1,5-2,0 fold that of Pd. PGMs precipitation from resulting solutions was fount to yield precipitate with Pt and Pd content amounting up to 55 %; this makes it possible to produce it as final product. The product is then sent to a final product (KP-1 concentrate) packaging section bypassing smelting and electrolysis stages with inherent high PGMs losses, resource intensity and long duration time

Pages
800-804
Paper at repository of SibFU
https://elib.sfu-kras.ru/handle/2311/10165

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