Method for treating lead-zinc sulfide ore production wastewater and recycling zinc from wastewater
A technology for the production of wastewater and sulfide ore, which is applied in mining wastewater treatment, zinc sulfide, chemical instruments and methods, etc., can solve the problems of secondary heavy metal pollution, regional surface water pollution, difficult treatment, etc., and achieve the effect of good pH buffering characteristics
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Embodiment 1
[0057] 1) Take 6L of lead-zinc mine production wastewater (including Zn837mg / L, Fe593mg / L, Cd4.15mg / L, pH value 2.8), put it in the stirring tank, add natural calcium carbonate ore with a particle size of 3-5mm ( CaCO 3 Content is 90%) 0.5kg, stir 1h, the pH value of waste water at this moment is 6.3, filter, the isolated unreacted natural calcium carbonate ore stays for next use, in the separated filtrate, add the concentration that is 1% PAM aqueous solution (PAM molecular weight is 3,000,000, and its solid dosage is calculated by adding 5 grams per ton of waste water), stirred for 1 min to form iron hydroxide flocculation precipitation, filtered to obtain iron removal waste water and iron hydroxide slag respectively;
[0058] 2) Add 10% Na simultaneously in step 1) in the iron removal waste water of gained 2 150ml of S aqueous solution and 1% concentration of flocculated PAM aqueous solution (PAM molecular weight is 3 million, and its solid dosage is calculated by adding 5...
Embodiment 2
[0061] 1) Take 40L of waste water from lead-zinc mine production (including Zn54mg / L, Fe136mg / L, Cd0.17mg / L, pH 4.3), put it in a stirring tank and add 0.5-1.0mm calcium carbonate ore (CaCO 3 Content is 90%) 5kg, stir 5h, the pH value of waste water at this moment is 6.5, filter, and the separated unreacted natural calcium carbonate ore stays for next use, in the separated filtrate, add the concentration and be 1%PAM aqueous solution (PAM molecular weight is 3,000,000, and its solid dosage is calculated by adding 10 grams per ton of waste water), stirring for 3 minutes, forming iron hydroxide flocculation precipitation, filtering, and obtaining iron removal waste water and iron hydroxide slag respectively;
[0062] 2) Add 5% Na in the iron removal waste water of step 1) gained 2 S aqueous solution 150ml, after 2 minutes, add concentration again and be 1% PAM aqueous solution (PAM molecular weight is 3,000,000, its solid consumption is calculated by adding 2 grams per ton of wa...
Embodiment 3
[0065] 1) Take 1000L of waste water from lead-zinc mine production (including Zn688mg / L, Fe786mg / L, Cd3.62mg / L, pH 2.6), put it in a stirring tank and add 5-20mm calcium carbonate ore (CaCO 3 Content is 65%) 60kg, stir 15h, the pH value of waste water at this moment is 6.5, filter, and the natural calcium carbonate ore that isolates has not reacted and stays for next use, in the separated filtrate, add the concentration and be 1% PAM aqueous solution (PAM molecular weight is 5,000,000, and its solid dosage is calculated by adding 10 grams per ton of waste water), stirred for 10 minutes, formed iron hydroxide flocculation precipitation, filtered, and obtained iron removal waste water and iron hydroxide slag respectively;
[0066] 2) Add 4000ml of 15% NaHS aqueous solution to the iron removal wastewater obtained in step 1), and then add 1% PAM aqueous solution after 8 minutes (the molecular weight of PAM is 5 million, and the solid dosage is calculated by adding 8 grams per ton o...
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