| CPC C22B 7/007 (2013.01) [C22B 3/04 (2013.01); C22B 15/0065 (2013.01); G01F 1/363 (2013.01); G01F 1/42 (2013.01); G01F 15/003 (2013.01); G01F 15/005 (2013.01); G01F 15/066 (2013.01); G05D 16/20 (2013.01); G08B 21/182 (2013.01); C22B 3/02 (2013.01); C22B 3/22 (2013.01); C22B 3/44 (2013.01); E21B 43/28 (2013.01); G01F 1/34 (2013.01); G01F 1/74 (2013.01); G01F 15/006 (2013.01); G05D 16/101 (2019.01); G05D 16/2024 (2019.01); Y02P 10/20 (2015.11); Y10T 137/86574 (2015.04)] | 20 Claims |

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1. A method for recovering a metal from chalcopyrite, comprising:
delivering a leaching solution from a leaching solution source to a leaching solution regulating system, wherein the leaching solution comprises a combination of an effective amount of citric acid and hydrogen peroxide, wherein the citric acid keeps iron in the leaching solution and allows the hydrogen peroxide to interact with the chalcopyrite;
regulating a pressure, a mass flow rate and a volumetric flow rate of the leaching solution to achieve a target operational condition, wherein the target operational condition is selected to optimize a set of operational parameters to allow options of preventing plugging of a subsurface leaching distribution system, minimizing locking up of the leaching solution in the heap and maximizing recovery of the recoverable metal in the chalcopyrite;
delivering the leaching solution at the target operational condition from the leaching solution regulating system to the subsurface leaching distribution system; and
delivering the leaching solution at the target operational condition from the subsurface leaching distribution system to a location of the recoverable metal in the chalcopyrite under a surface of the heap to leach and recover the recoverable metal from the chalcopyrite.
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