Method for extracting nickel, cobalt and copper from nickel-copper alloy chloride leaching solution
A technology of chlorination leaching and nickel-copper alloy, which is applied in the fields of cobalt, copper, and nickel extraction, can solve the problems of long treatment process, low metal recovery rate, and high production cost, and achieve broad application range, low ionic strength, and reduced loose The effect of packing density
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Embodiment 1
[0017] A method for extracting nickel, cobalt, copper from nickel-copper alloy chlorination leach solution, described preparation method comprises the steps:
[0018] (1) Heat the chlorinated leaching solution to 70°C, slowly add liquid ammonia under stirring condition to adjust the pH value of the solution to 4, control the time of adding liquid ammonia for one hour, continue stirring for half an hour, and then filter the solution to obtain filtrate, filter residue Carry out curing treatment;
[0019] (2) The filtrate uses an extractant containing 15% 2-ethylhexyl phosphate mono-2-ethylhexyl ester and 85% sulfonated kerosene, and controls the saponification rate to 80%. Under the condition of O / A=5:1 Under the condition of extracting, cobalt and copper ions in the filtrate of extraction step (1), cobalt and copper enter the organic phase to form a loaded organic phase, and nickel remains in the raffinate in the form of nickel chloride;
[0020] (3) Use dilute hydrochloric ac...
Embodiment 2
[0027] A method for extracting nickel, cobalt, copper from nickel-copper alloy chlorination leach solution, described preparation method comprises the steps:
[0028] (1) Heat the chlorinated leaching solution to 60°C, slowly add liquid ammonia under stirring conditions to adjust the pH value of the solution to 4.5, control the time of adding liquid ammonia for one hour, continue stirring for half an hour, and then filter the solution to obtain the filtrate and filter residue Carry out curing treatment;
[0029] (2) The filtrate uses an extractant containing 25% 2-ethylhexyl phosphate mono-2-ethylhexyl ester and 75% sulfonated kerosene to control the saponification rate to 65%. Under the condition of O / A=5:1 Under the condition of extracting, cobalt and copper ions in the filtrate of extraction step (1), cobalt and copper enter the organic phase to form a loaded organic phase, and nickel remains in the raffinate in the form of nickel chloride;
[0030] (3) Use dilute hydrochl...
Embodiment 3
[0037] A method for extracting nickel, cobalt, copper from nickel-copper alloy chlorination leach solution, described preparation method comprises the steps:
[0038] (1) Heat the chlorinated leaching solution to 65°C, slowly add liquid ammonia under stirring condition to adjust the pH value of the solution to 45, control the time of adding liquid ammonia for one hour, continue stirring for half an hour, then filter the solution to obtain filtrate, filter residue Carry out curing treatment;
[0039](2) The filtrate uses an extractant containing 20% 2-ethylhexyl phosphate mono-2-ethylhexyl ester and 80% sulfonated kerosene, and controls the saponification rate to 70%. Under the condition of O / A=4:1 Under the condition of extracting, cobalt and copper ions in the filtrate of extraction step (1), cobalt and copper enter the organic phase to form a loaded organic phase, and nickel remains in the raffinate in the form of nickel chloride;
[0040] (3) Use dilute hydrochloric acid...
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