Comprehensive utilization method of iron ions in pressurized leaching solution of arsenic-bearing gold ore
A technology of pressurized leaching and leaching solution, which is applied in the direction of improving process efficiency, can solve problems such as increasing costs, and achieve the effects of acid balance, smooth flow, and reduction of chemical consumption.
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Embodiment 1
[0057] A gold concentrate contains 15.2% sulfur, 21% iron, 3.2% arsenic, and 41.5% carbonate (calculated as calcium carbonate). Add concentrated sulfuric acid to start, and then return the oxidative leaching solution 6 of liquid-solid separation to stir and acidify to decompose carbonate, acidify solution 3 to neutralize and remove impurities, first add lime at 180kg / t to start, and then return the remaining oxidative leaching solution 6 of liquid-solid separation to return Neutralize and remove impurities.
[0058] Adopt the method of the present invention, concrete operation steps and technological parameters are as follows:
[0059] (1) Oxidative leaching solution 6 contains H 2 SO 4 42.1g / L, with Fe 3+ 21g / L.
[0060] (2) the gold essence (middle) ore before entering the autoclave and the oxidation leaching solution 6 of step D carry out agitation acidification reaction, decompose carbonate, and the reaction is carried out in three series-connected stirring tanks, and ...
Embodiment 2
[0064] A gold concentrate (middle) ore contains 12.3% sulfur, 19.1% iron, 1.6% arsenic, and 30.06% carbonate (calculated as calcium carbonate), and the oxidized liquid after pressurized oxidation produces 150kg / t of acid, according to 144kg / t t First add concentrated sulfuric acid to start, then return the oxidative leaching solution 6 of liquid-solid separation to agitation and acidify to decompose carbonate, and acidify solution 3 to neutralize and remove impurities. 6 Return to neutralize and remove impurities.
[0065] Adopt the method of the present invention, concrete operation steps and technological parameters are as follows:
[0066] (1) Oxidative leaching solution 6 contains H 2 SO 4 34g / L, with Fe 3+ 19.1g / L.
[0067] (2) the gold essence (middle) ore before entering the autoclave and the oxidation leaching solution 6 of step D carry out agitation and acidification reaction, decompose carbonate, the reaction is carried out in three series-connected stirring tank...
Embodiment 3
[0071] A gold concentrate (medium) ore contains 10.8% sulfur, 14.4% iron, 0.9% arsenic, and 25.04% carbonate (calculated as calcium carbonate), and the oxidizing liquid produces 132kg / t of acid after pressurized oxidation, according to 113kg / t t First add concentrated sulfuric acid to start, then return the oxidative leaching solution 6 of liquid-solid separation to agitation and acidify to decompose carbonate, and acidify solution 3 to neutralize and remove impurities. 6 Return to neutralize and remove impurities.
[0072] Adopt the method of the present invention, concrete operation steps and technological parameters are as follows:
[0073] (1) The pressurized leaching solution contains H 2 SO 4 31g / L, with Fe 3+ 18.2g / L.
[0074] (2) the gold concentrate slurry before entering the autoclave and the oxidative leaching solution 6 of step D carry out agitation acidification reaction, decompose carbonate, the reaction is carried out in three series-connected stirring tanks...
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