“…Economic evaluation of different commercial, piloted, or bench scale alternative processing routes, depending upon the location and mineralogy of ore, and availability of technology has also been conducted. These include smelting, reduction roasting to ferronickel and ammonia leaching (Caron process), high pressure acid leaching, strong brine leaching, atmospheric leaching, heap leaching and microbial leaching with fungi or bacteria (Kyle, 1996;Whittington and Muir, 2000;Curlook, 2004;Muir and Johnson, 2006;McDonald and Whittington, 2008a,b;Xavier and Ciminelli, 2008;Steyl et al, 2008;Simate et al, 2010;Hallberg et al, 2011;Norgate and Jahanshahi, 2011). The recovery of a mixed sulphide or hydroxide precipitate (MSP or MHP) of Ni(II) and Co(II) from leach liquors of a widened ore type and grade, which can be sold to existing refineries, is the preferred option when metal production on the minesite is not intended (Curlook, 2004;White et al, 2006;Steyl et al, 2008;Kose and Topkaya, 2011).…”