Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
146 words
In the recovery of metallic copper from a copper-sulfide ore deposit containing pyrite, the steps of (a) mining the ore deposit; (b) smelting the higher grade ore mined from said deposit to yield a smelter slag containing relatively little copper; (c) leaching with an acidic ferric sulfate solution, of pH between about 2 and 3.5, rejected lower grade portions of the mined ore materials containing pyrite and relatively litte copper to yield a copper-bearing, acidic, ferric sulfate solution; (d) grinding or granulating said smelter slag; (e) leaching the ground or granulated smelter slag with the copper-bearing, acidic, ferric sulfate solution from step (c), which has a pH of from about 1.9 to 3.0, to recover copper values from said slag and to minimize the presence of ferric ions in said solution; and (f) recovering metallic copper from the effluent leach solution of slag leaching step (e).
Claim 2
Dependent Claim
146 words
In the recovery of metallic copper from a copper-sulfide ore deposit containing pyrite, the steps of (a) mining the ore deposit; (b) smelting the higher grade ore mined from said deposit to yield a smelter slag containing relatively little copper; (c) leaching with an acidic ferric sulfate solution, of pH between about 2 and 3.5, rejected lower grade portions of the mined ore materials containing pyrite and relatively litte copper to yield a copper-bearing, acidic, ferric sulfate solution; (d) grinding or granulating said smelter slag; (e) leaching the ground or granulated smelter slag with the copper-bearing, acidic, ferric sulfate solution from step (c), which has a pH of from about 1.9 to 3.0, to recover copper values from said slag and to minimize the presence of ferric ions in said solution; and (f) recovering metallic copper from the effluent leach solution of slag leaching step (e).
Claim 3
Dependent Claim
32 words
A process in accordance with claim 1, wherein the ferric iron concentration in the copper-bearing, acidic, ferric sulfate solution is within the range of about 0.5 to about 3.0 grams per liter.
Claim 4
Dependent Claim
152 words
An integrated process for improving overall recovery of copper values from a deposit of low-grade, iron-containing, copper ore materials comprising mining said ore materials; smelting higher grade portions of the mined ore materials to provide a slag containing relatively little copper; crushing or granulating said slag; leaching lower-grade portions of the mined ore material with an acidic, aqueous solution having a pH of between about 2 and 3.5, to produce an effluent solution having a pH of from about 1.9 to 3.0 and containing dissolved copper and ferrite iron values; separating said effluent solution from the so-leached ore material; leaching the crushed or granulated smelter slag with said effluent solution, thereby selectively leaching copper values from said slag without problems of iron hydrolysis or gel formation and, at the same time, beneficially reducing the level of ferric iron present in the solution; and recovering copper values from the resulting pregnant leach solution.
Claim 5
Dependent Claim
152 words
An integrated process for improving overall recovery of copper values from a deposit of low-grade, iron-containing, copper ore materials comprising mining said ore materials; smelting higher grade portions of the mined ore materials to provide a slag containing relatively little copper; crushing or granulating said slag; leaching lower-grade portions of the mined ore material with an acidic, aqueous solution having a pH of between about 2 and 3.5, to produce an effluent solution having a pH of from about 1.9 to 3.0 and containing dissolved copper and ferrite iron values; separating said effluent solution from the so-leached ore material; leaching the crushed or granulated smelter slag with said effluent solution, thereby selectively leaching copper values from said slag without problems of iron hydrolysis or gel formation and, at the same time, beneficially reducing the level of ferric iron present in the solution; and recovering copper values from the resulting pregnant leach solution.
Claim 6
Dependent Claim
49 words
A process in accordance with claim 3, wherein the copper values are recovered from the resulting pregnant leach solution by contacting metallic iron with the pregnant leach solution, whereby copper is precipitated from the solution and replaced therein by iron; and precipitated copper is separated from the copper-depleted solution.
Claim 7
Dependent Claim
34 words
A process in accordance with claim 4, wherein the copper-depleted solution is recycled and used as the aqueous, acidic leach solution in the leaching of the lower grade portions of the mined ore material.
Claim 8
Dependent Claim
20 words
A process in accordance with claim 3, wherein the copper values are recovered from the pregnant leach solution by electrowinning.
Claim 9
Dependent Claim
72 words
A process in accordance with claim 6, wherein the electrowinning is preceded by contacting the pregnant leach solution with a liquid exchange medium which is substantially insoluble in said leach solution and which is capable of selectively extracting copper values therefrom; and wherein the aqueous raffinate solution is separated from the thereby copper-enriched, liquid exchange medium and copper values are stripped from said liquid exchange medium with an aqueous, acidic, stripping solution.
Claim 10
Dependent Claim
34 words
A process in accordance with claim 7, wherein the raffinate solution is recycled and used as the aqueous, acidic leach solution in the leaching of the lower grade portion of the mined ore material.
Claim 11
Dependent Claim
29 words
A process in accordance with claim 3, wherein the ferric iron concentration in the effluent solution is within the range of about 0.5 to about 3.0 grams per liter.