Sulfide ore leaching process
The present invention discloses a new process for leaching sulfide minerals consisting of leaching crushed ore in a vat reactor, wherein the leaching solution is fed with an ORP value close to the upper limit suitable for leaching and the exiting leaching solution leaves the reactor with an ORP above the lower limit suitable for leaching the ore. The output leaching solution that leaves the leaching reactor goes through an iron oxidation stage outside the leaching reactor, with the iron oxidation producing soluble ferric sulfate that is mixed with a recirculated portion of the output leaching solution to increase its ORP up to a value close to the upper limit of the redox potential range that is suitable for the ore leaching.
1. A process for leaching sulfide minerals, comprising:
crushed ore leaching in a vat reactor in which an input leaching solution is fed with an oxidation-reduction-potential (“ORP”) close to an upper limit of an ORP range suitable for ore leaching and from where an exiting leaching solution leaves with an ORP above a lower limit of the ORP range and less than the ORP of the input leaching solution, wherein the ORP range is about 380 to 450 mV at a temperature of 25 to 45° C. or 500 to 700 mV at a temperature of greater than 60° C.; and
where part of the exiting leaching solution that leaves the vat reactor goes through an iron oxidation stage, external to the vat reactor, with the iron oxidation producing soluble ferric sulfate that is mixed with a recirculated portion of the output leaching solution to increase its ORP up to a value close to the upper limit of the redox potential range that is suitable for the ore leaching.
2. The process according to claim 1 , wherein the crushed ore has particle sizes ranging from 2 mm to 120 mm.
3. The process according to claim 1 , wherein ore inside the vat reactor is kept substantially submerged in the leaching solution in a way that voids between the ore crushed particles are saturated and filled in with the leaching solution.
4. The process according to claim 1 , wherein iron oxidation reaction is supplemented with sulfur or pyrite to provide additional acid in order to generate heat, the additional sulfur or pyrite being controlled to achieve a desired iron and heat balance.
5. The process according to claim 1 , wherein the iron oxidation allows for precipitation of jarosite, and co-precipitation of leaching solution impurities.
6. The process according to claim 1 , wherein when an ore of interest has enough concentration for recovery, an enriched leaching solution is removed from the process and subjected to treatment for recovery of the ore of interest.
7. The process according to claim 6 , wherein a sulfide mineral present in the ore is a primary sulfide or a secondary sulfide.
8. The process according to claim 7 , wherein the primary sulfide is chalcopyrite.
9. The process according to claim 8 , wherein the secondary sulfide is chalcocite.
10. A process for leaching sulfide minerals, comprising:
crushed ore leaching in a vat reactor in which an input leaching solution is fed with an oxidation-reduction-potential (“ORP”) close to an upper limit of an ORP range suitable for ore leaching and from where an exiting leaching solution leaves with an ORP above a lower limit of the ORP range, wherein the ORP range is about 380 to 450 mV at a temperature of 25 to 45° C. or 500 to 700 mV at a temperature of greater than 60° C., wherein the crushed ore has particle sizes ranging from 2 mm to 120 mm; and
where part of the exiting leaching solution that leaves the vat reactor goes through an iron oxidation stage, external to the vat reactor, with the iron oxidation producing soluble ferric sulfate that is mixed with a recirculated portion of the output leaching solution to increase its ORP up to a value close to the upper limit of the redox potential range that is suitable for the ore leaching.
11. A process for leaching sulfide minerals, comprising:
crushed ore leaching in a vat reactor in which an input leaching solution is fed with an oxidation-reduction-potential (“ORP”) close to an upper limit of an ORP range suitable for ore leaching and from where an exiting leaching solution leaves with an ORP above a lower limit of the ORP range, wherein the ORP range is about 380 to 450 mV at a temperature of 25 to 45° C. or 500 to 700 mV at a temperature of greater than 60° C.; and
where part of the exiting leaching solution that leaves the vat reactor goes through an iron oxidation stage, external to the vat reactor, with the iron oxidation producing soluble ferric sulfate that is mixed with a recirculated portion of the output leaching solution to increase its ORP up to a value close to the upper limit of the redox potential range that is suitable for the ore leaching,
wherein iron oxidation reaction is supplemented with sulfur or pyrite to provide additional acid in order to generate heat, the additional sulfur or pyrite being controlled to achieve a desired iron and heat balance.