A method for enriching and separating lead-zinc mixed concentrate from gold concentrate cyanidation tailings
A technology for cyaniding tailings and mixed concentrates, applied in separation methods, chemical instruments and methods, filtration and separation, etc., can solve the problems of not obtaining copper concentrates, zinc concentrates, copper-zinc concentrates, etc., and achieve improvement The effect of comprehensive utilization and reduction of waste of resources
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Embodiment 1
[0024] 1) Slurry the gold concentrate cyanidation tailings containing 8wt% lead and 10wt% zinc with system water, the slurry concentration is 10wt%, and add a compound leaching agent to the slurry to further extract the gold concentrate cyanide tailings The gold, silver and copper in the compound type leaching agent is made of ammonia water, ammonium carbonate, and ammonium bicarbonate in a weight ratio of 2:2:1. The addition amount of the compound type leaching agent is 0.40% of the filter cake mass, and the leaching temperature is controlled at 40 ℃, the leaching time is 8 hours. After the leaching is completed, the system passes through a plate and frame filter press to obtain filtrate and filter cake. After the filtrate is replaced by zinc powder to recover valuable metals, it is system water, and it is returned to the pulping process for recycling. The filter cake is Cyanide tailings after extraction of gold, silver and copper;
Embodiment 2
[0028]1) Slurry the gold concentrate cyanidation tailings containing 9wt% lead and 13wt% zinc with system water at a concentration of 10wt%, and add a compound leaching agent to the slurry to further extract the gold concentrate cyanide tailings The gold, silver and copper in the compound type leaching agent is prepared from ammonia water, ammonium carbonate, and ammonium bicarbonate in a weight ratio of 2:2:1. The addition amount of the compound type leaching agent is 0.50% of the filter cake mass, and the leaching temperature is controlled at 50 ℃, the leaching time is 10 hours. After the leaching is completed, the system passes through a plate and frame filter press to obtain filtrate and filter cake. After the filtrate is replaced by zinc powder to recover valuable metals, it is system water, and it is returned to the pulping process for recycling. The filter cake is Cyanide tailings after extraction of gold, silver and copper;
[0029] 2) Slurry the cyanide tailings after...
Embodiment 3
[0032] 1) Slurry the gold concentrate cyanidation tailings containing 10wt% lead and 15wt% zinc with system water, the slurry concentration is 30wt%, and add a compound leaching agent to the slurry to further extract the gold concentrate cyanide tailings The gold, silver and copper in the compound type leaching agent is made of ammonia water, ammonium carbonate, and ammonium bicarbonate in a weight ratio of 2:2:1. The addition amount of the compound type leaching agent is 0.60% of the filter cake mass, and the leaching temperature is controlled at 60 ℃, the leaching time is 12 hours. After the leaching is completed, the system passes through a plate and frame filter press to obtain filtrate and filter cake. After the filtrate is replaced by zinc powder to recover valuable metals, it becomes system water, and it is returned to the pulping process for recycling. The filter cake is Cyanide tailings after extraction of gold, silver and copper;
[0033] 2) Slurry the cyanide tailin...
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