HCI Leaching and Acid Regeneration using MgCl2 Brines and Molten Salt Hydrates

The Minerals, Metals and Materials Society
Jan de Bakker Joshua LaMarre Vladimiros Papangelakis Boyd Davis
Organization:
The Minerals, Metals and Materials Society
Pages:
8
File Size:
737 KB
Publication Date:
Jan 1, 2011

Abstract

"HCl leaching using molten salt hydrates has the potential to improve the extraction of nickel from laterite ores. However, as in other HCl leaching applications, recovery of HCl is key to process economics. Spray pyrohydrolysis, which is used in current chloride-based flowsheets, is associated with a high energy cost. The authors have developed a proposed laterite leach circuit using an alternative HCl recovery route. The leach circuit envisions a leach by concentrated (33%) HCl in an MgCl2 molten salt hydrate (MSH) or brine medium, followed by Ni/Co recovery and iron precipitation. Magnesium and chloride are precipitated from solution as magnesium hydroxychloride; this hydroxychloride is thermally decomposed to produce HCl gas. The proposed flowsheet employs a chloride leach circuit with simpler equipment and lower energy cost than in the conventional practice of pyrohydrolysis. Laboratory work investigated key aspects of the flowsheet, including precipitation of magnesium hydroxychlorides and their composition; magnesium hydroxychloride thermal decomposition; and iron control.Introduction As sulphide nickel ores become harder to mine and more complex to process, laterite ores will increase in importance. Laterite ore deposits can be divided into two main mineralogies. Limonite ores consist mostly of hydrated iron oxide, FeOOH, with 1-3% nickel substituting for the iron. Saprolite ores consist of iron-magnesium silicates, (Fe, Mg)2Si04, again with some nickel substituting for the metal ions. Limonite ores can be treated using the HP AL (High Pressure Acid Leach) process, in which the ore is reacted with sulphuric acid at high temperature in an autoclave. HP AL, however, cannot in general be used to treat saprolite ores because the magnesium enters solution and consumes sulphuric acid, which results in excessive spending on lixiviant. It is therefore desirable to find a hydrometallurgical process specifically for saprolite ores that can provide better results than the treatment options currently available."
Citation

APA: Jan de Bakker Joshua LaMarre Vladimiros Papangelakis Boyd Davis  (2011)  HCI Leaching and Acid Regeneration using MgCl2 Brines and Molten Salt Hydrates

MLA: Jan de Bakker Joshua LaMarre Vladimiros Papangelakis Boyd Davis HCI Leaching and Acid Regeneration using MgCl2 Brines and Molten Salt Hydrates. The Minerals, Metals and Materials Society, 2011.

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