Nickel Recovery From Hydroxide Slurries By Pressure Reduction

Nickel metal, in powder form, has been produced by pressure reduction, with hydrogen gas, of slurries of nickel hydroxide at temperatures up to 250°C. The nickel hydroxide was obtained by precipitation from nickel chloride and nickel sulphate solutions, using both magnesium oxide and calcium oxide. Rates of reduction and yields were determined as a function of temperature, hydrogen overpressure, seed addition, and the amount of alkali used. The mechanism of reduction of slurries obtained from the sulphate system was studied, and major differences between the sulphate system and the previously examined chloride system investigated. Specifically, in the sulphate system, contra the chloride system, no seeding was necessary, plating and densification were virtually absent and only short induction periods occurred. Grades of product are given and the use of this process in the recovery of nickel from laterites is discussed. The selective reduction of nickel from mixed hydroxide slurries and effluent treatment plant sludge has also been examined.