Process for recovering cobalt, copper, zinc and manganese in manganese chloride residual liquid
A technology of manganese chloride raffinate and manganese chloride, which is applied in the field of hydrometallurgy and chemical industry, can solve the problems of long process flow, high cost, waste of resources and environment, and achieve short process flow, low production cost and high product purity Effect
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Embodiment 1
[0015] a The chloride ion concentration in the manganese chloride solution containing cobalt, copper and zinc produced in the process of processing the ore containing manganese, cobalt, copper and zinc is adjusted to 300g / L with a hydrochloric acid solution with a concentration of 24%;
[0016] b with 5% N 235 , the extractant of 5% isooctyl alcohol and 90% sulfonated kerosene is compared in O / A=1:0.5, and the cobalt, copper, and zinc ions in the manganese chloride raffinate are left in the raffinate;
[0017] C is that the sodium chloride solution that chlorine ion concentration is 60g / L compares O / A=1:0.5, strips the cobalt in the raffinate organic phase, obtains the cobalt chloride precipitate; / A=1:0.5, the copper in the back extraction raffinate is loaded in the organic phase, and the copper chloride precipitate is obtained; compared with O / A=1:0.5 with the stripping agent sodium carbonate, the back extraction raffinate is loaded with organic Zinc in the phase, a zinc pr...
Embodiment 2
[0024] When a hydrochloric acid solution with a concentration of 35% is used to leach ores containing manganese, cobalt, copper and zinc with hydrochloric acid, the chloride ion concentration in the obtained manganese chloride leach solution is adjusted to 350g / L;
[0025] b with 30% N 235 , 20% isooctyl alcohol and 50% sulfonated kerosene N 235 When the extractant is compared to O / A=1:5, the cobalt, copper, and zinc ions in the extracted manganese chloride raffinate remain in the raffinate;
[0026] c Use a hydrochloric acid solution with a chloride ion concentration of 80g / L at a ratio of O / A=1:5 to back-extract the cobalt in the organic phase of the raffinate to obtain a cobalt chloride precipitate; use pure water at a ratio of O / A =1:5, back extract the copper in the raffinate loaded organic phase, and obtain copper chloride precipitate; use the stripping agent oxalic acid to compare O / A=1:5, back extract the copper in the raffinate loaded organic phase Zinc, to obtain a...
Embodiment 3
[0033] a Use a 30% hydrochloric acid solution to adjust the concentration of chloride ions in the manganese chloride raffinate to 250g / L;
[0034] b with 20% N 235 , 15% isooctyl alcohol and 65% N of sulfonated kerosene 235 The extractant extracts cobalt, copper and zinc ions in the manganese chloride raffinate under the condition of O / A=1:3;
[0035] c Use a sodium chloride solution with a chloride ion concentration of 70g / L at a ratio of O / A=1:2 to back-extract cobalt in the organic phase; use pure water at a ratio of O / A=1:3 to back-extract Extract the copper in the loaded organic phase; use potassium hydroxide to back-extract the zinc in the loaded organic phase at a ratio of O / A=1:3.5; Cobalt chloride, copper chloride products;
[0036] d with 25% P 204 and 75% sulfonated kerosene, the saponification rate is 75% P 204 The extractant is compared to O / A=1:3, and the extraction is carried out by N 235 Manganese ions in the raffinate obtained after extraction; use 2mol / ...
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Abstract
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Application Information
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