Process for the selective dissolution of cobalt from cobaltite-pyrite concentrates

Claim 2

A hydrometallurgical process for the recovery of cobalt from cobaltite-pyrite concentrates containing substantial amounts of cobalt, arsenic, iron and sulphur, with an excess of iron relative to arsenic of at least two to one, comprising pressure leaching of the concentrates with a sodium chloride or sodium sulphate solution at temperatures of 130°-160° C. and under oxygen partial pressures of 75-200 psi to solubilize most of the cobalt content, while simultaneously limiting the oxidation of pyrite and precipitating most of the solubilized iron and arsenic as jarosite and ferric arsenate.

Claim 3

A hydrometallurgical process as defined in claim 1, wherein the leaching temperature is about 150° C.

Claim 4

A hydrometallurgical process as defined in claim 1, wherein the oxygen partial pressure is about 175 psi.

Claim 5

A hydrometallurgical process as defined in claim 1, 2 or 3 wherein the sodium chloride or sodium sulphate slurry is 25-40% solids.

Claim 6

A hydrometallurgical process as defined in claim 1, 2 or 3, wherein pressure leaching is conducted in a sodium sulphate solution within the range of 20-75 g/L.

Claim 7

A hydrometallurgical process as defined in claim 1 or 2, wherein sulphuric acid and/or ferric iron is added at low oxygen partial pressure to overcome an initial induction period.

Claim 8

A hydrometallurgical process as defined in claim 1, wherein the cobaltite-pyrite concentrate contains about 5-7% Co, 0.1-0.4% Ni, 0.3-0.7% Cu, 9-13% As, 26-35% Fe and 28-39% S.

Claim 9

A hydrometallurgical process for the recovery of cobalt from cobaltite-pyrite concentrates, with an excess of iron relative to arsenic of at least two to one, containing substantial amounts of cobalt, arsenic, iron and sulphur, comprising the steps of: (1) pressure leaching the concentrate in an autoclave with a sodium chloride or sodium sulphate solution at 130°-160° C. and under oxygen partial pressure of 75-200 psi to solubilize at least 90% of the cobalt content, while simultaneously limiting the oxidation of pyrite and precipitating most of the soluble iron and arsenic as jarosite and ferric arsenate; (b) discharging the leach slurry from the autoclave and neutralizing the slurry to pH 1.0-1.5 at 85°-95° C. and atmospheric pressure with lime, limestone or other neutralizing agents, so as to continue iron and arsenic precipitation as jarosite and ferric arsenate; (c) conducting a liquid-solid separation with the slurry from the atmospheric jarosite precipitation step to obtain a primary filtrate for further processing for cobalt recovery; (d) washing the jarosite-ferric arsenate residue to recover entrained metal values, and recirculating the wash solution to the autoclave to form a 25-40% solids slurry with the sodium chloride or sodium sulphate addition to the autoclave.

Claim 10

A hydrometallurgical process for the recovery of cobalt from cobaltite-pyrite concentrates, with an excess of iron relative to arsenic of at least two to one, containing substantial amounts of cobalt, arsenic, iron and sulphur, comprising the steps of: (1) pressure leaching the concentrate in an autoclave with a sodium chloride or sodium sulphate solution at 130°-160° C. and under oxygen partial pressure of 75-200 psi to solubilize at least 90% of the cobalt content, while simultaneously limiting the oxidation of pyrite and precipitating most of the soluble iron and arsenic as jarosite and ferric arsenate; (b) discharging the leach slurry from the autoclave and neutralizing the slurry to pH 1.0-1.5 at 85°-95° C. and atmospheric pressure with lime, limestone or other neutralizing agents, so as to continue iron and arsenic precipitation as jarosite and ferric arsenate; (c) conducting a liquid-solid separation with the slurry from the atmospheric jarosite precipitation step to obtain a primary filtrate for further processing for cobalt recovery; (d) washing the jarosite-ferric arsenate residue to recover entrained metal values, and recirculating the wash solution to the autoclave to form a 25-40% solids slurry with the sodium chloride or sodium sulphate addition to the autoclave.

Claim 11

A process as defined in claim 8, wherein the leaching temperature is maintained at about 150° C.

Claim 12

A process as defined in claim 8, wherein the oxygen partial pressure is about 175 psi.

Claim 13

A hydrometallurgical process defined in claim 8, 9 or 10 wherein pressure leaching is conducted with sodium sulphate within the range of 20-75 g/L.

Claim 14

A hydrometallurgical process as defined in claim 8, wherein said cobaltite-pyrite concentrates contain about 5-7%, Co, 0.1-0.4% Ni, 0.3-0.7% Cu, 9-13% As, 26-35% Fe and 28-39% S.