Recovery of precious metal values from refractory ores

Claim 2

A hydrometallurgical process for recovery of precious metals from an ore which is refractory to treatment by lixiviating agents comprising: a. crushing the ore to no finer than about a nominal 1/4 inch size, b. treating the crushed ore with a mineral acid in amounts to being the resulting mixture of a pH of about 2 or below, c. treating the acidified ore with from about 5% to about 200% of the stoichiometric amount of nitric acid required to react with the ore, and recovering any NO x gas evolved from the ore, d. placing the thus-treated ore in a heap permeable ore bed on top of an impermeable collector, e. heap treating the permeable ore bed by dispersing continuously or intermittently an aqueous nitric acid solution through the bed, f. separating residual acid liquor from the heap permeable ore bed, g. water washing the heap permeable ore bed to remove nitric acid solution therefrom, and separating the washings from the ore bed, h. introducing any NO x gases recovered from step c. into a nitric acid generator for conversion of the NO x into nitric acid and recycling said nitric acid for use in treating said ore, i. treating the heap permeable ore bed by dispersing continuously or intermittently a lixiviate for precious metals through the bed, j. separating the lixiviate solution containing dissolved precious metals from the heap permeable ore bed and recovering said precious metals from the lixiviate.

Claim 3

Process of claim 1 wherein said ore is crushed to a nominal 1/4 inch up to a nominal 3/4 inch.

Claim 4

Process of claim 1 wherein said mineral acid in step b. is sulfuric acid.

Claim 5

Process of claim 1 wherein said nitric acid in step c. has a concentration of from about 20% to about 70% by weight HNO 3 .

Claim 6

Process of claim 1 wherein said aqueous nitric acid in step e. has a concentration of from about 6% to about 20% by weight HNO 3 .

Claim 7

Process of claim 1 wherein said calcium, sodium or magnesium ions are supplied by using Ca(OH) 2 , CaO, CaCO 3 , NaOH, or Mg(OH) 2 .

Claim 8

Process of claim 1 wherein said lixiviate is an aqueous solution of sodium cyanide.

Claim 9

Process of claim 1 wherein said ore is treated in steps b. through i. at ambient temperatures and under atmospheric pressures.

Claim 10

Process of claim 1 wherein said residual acid liquor separated from said heap permeable ore bed in step f. is passed through an ion exchange unit and HNO 3 separated from the remaining liquor.

Claim 11

Process of claim 9 wherein said separated HNO 3 is recycled for use in treating said ore.

Claim 12

Process of claim 1 wherein said residual acid liquor separated from said heap permeable ore bed in step f. is passed through a carbon column and soluble precious metal values are selectively adsorbed in the carbon column separate from other metal values in said liquor.

Claim 13

A hydrometallurgical process for recovery of precious metals form an ore which is refractory to treatment by lixiviating agents comprising: a. crushing the ore to a nominal size of from about 1/4 inch to about 1 inch, b. treating the crushed ore with sulfuric acid to a pH of about 2 or below, c. treating the acidified ore with from about 5% to about 200% of the stoichiometric amount of nitric acid required to react with the ore wherein the nitric acid has a concentration of from about 20 weight percent to about 70 weight percent HNO 3 , and recovering andy NO x gas evolved from the ore, d. placing the thus-treated ore in a heap permeable ore bed on top of an impermeable collector, e. heap treating the permeable ore bed by dispersing continuously or intermittently and aqueous nitric acid solution through the bed having a concentration of about 6 weight percent to about 20 weight HNO 3 , f. separating residual acid liquor from the heap permeable ore bed, g. water washing the heap permeable ore bed to remove nitric acid solution therefrom, and separating the washings from the ore bed, h. separating nitric acid values from said residual acid liquor of step f. and recycling the nitric acid for use in treating said ore, i. introducing any NO x gases recovered from steps . into a nitric acid generator for conversion of the NO x into nitric acid and recycling said nitric acid of use in treating said ore, j. treating the heap permeable ore bed with sufficient calcium, sodium or magnesium ions under alkaline conditions to increase the pH of the liquor removed from the bed to about 10 or above, k. treating the heap permeable ore bed by dispersing continually or intermittently a sodium cyanide lixiviating solution for precious metals through the bed, l. separating the lixiviating solution containing dissolved precious metals from the heap permeable ore bed and recovering said precious metals from the lixiviating solution.

Claim 14

A hydrometallurgical process for recovery of precious metals form an ore which is refractory to treatment by lixiviating agents comprising: a. crushing the ore to a nominal size of from about 1/4 inch to about 1 inch, b. treating the crushed ore with sulfuric acid to a pH of about 2 or below, c. treating the acidified ore with from about 5% to about 200% of the stoichiometric amount of nitric acid required to react with the ore wherein the nitric acid has a concentration of from about 20 weight percent to about 70 weight percent HNO 3 , and recovering andy NO x gas evolved from the ore, d. placing the thus-treated ore in a heap permeable ore bed on top of an impermeable collector, e. heap treating the permeable ore bed by dispersing continuously or intermittently and aqueous nitric acid solution through the bed having a concentration of about 6 weight percent to about 20 weight HNO 3 , f. separating residual acid liquor from the heap permeable ore bed, g. water washing the heap permeable ore bed to remove nitric acid solution therefrom, and separating the washings from the ore bed, h. separating nitric acid values from said residual acid liquor of step f. and recycling the nitric acid for use in treating said ore, i. introducing any NO x gases recovered from steps . into a nitric acid generator for conversion of the NO x into nitric acid and recycling said nitric acid of use in treating said ore, j. treating the heap permeable ore bed with sufficient calcium, sodium or magnesium ions under alkaline conditions to increase the pH of the liquor removed from the bed to about 10 or above, k. treating the heap permeable ore bed by dispersing continually or intermittently a sodium cyanide lixiviating solution for precious metals through the bed, l. separating the lixiviating solution containing dissolved precious metals from the heap permeable ore bed and recovering said precious metals from the lixiviating solution.

Claim 15

Process of claim 12 wherein said ore is treated in steps b. through k. at ambient temperatures and atmospheric pressures.

Claim 16

Process of claim 12 wherein said residual acid liquor separated from said heap permeable ore bed in step f. is passed through a carbon column and soluble precious metal values are selectively adsorbed in the carbon column separate from other metal values in said liquor.

Claim 17

Process of claim 12 wherein nitric acid values are separated from residual acid liquor in step h. by use of an ion exchange unit.

Claim 18

Process of claim 12 wherein the nitric acid generator employed for conversion of the recovered NO x into nitric acid in step i. is an air absorption type generator.

Claim 19

Process of claim 1 wherein an acid resistant binder is added to the nitric acid-treated ore from step c. to form ore agglomerates capable of maintaining a porous bed of ore, maintaining the binder and ore in contact with one another for a sufficient curing time to permit the ore agglomerates to maintain their particulate form, and recovering any NO x evolved from the ore.

Claim 20

Process of claim 1 wherein the heap permeable ore bed of step g. is treated with sufficient calcium, sodium or magnesium ions under alkaline conditions to increase the pH of the liquor removed form the bed to about 10 or above.

Claim 21

Process of claim 17 wherein any NO x gases recovered during the formation of the ore agglomerates are sent to a nitric acid generator for conversion of the NO x into nitric acid and recycling the nitric acid for use in treating said ore.

Claim 22

Process of claim 12 wherein an acid resistant binder is added to the nitric acid-treated ore from step c. to form ore agglomerates capable of maintaining a porous bed of ore, maintaining the binder and ore in contact with one another for a sufficient curing time to permit the ore agglomerates to maintain their particulate form, and recovering any NO x evolved from the ore.

Claim 23

Process of claim 20 wherein any NO x gases recovered during the formation of the ore agglomerates are sent to a nitric acid generator for conversion of the NO x into nitric acid and recycling the nitric acid for use in treating said ore.

Claim 24

A hydrometallurgical process for recovery of precious metals from an ore which is refractory to treatment by lixiviating agents comprising: a. crushing the ore to no finer than about a nominal 1/4 inch size, b. treating the crushed ore with a mineral acid in amounts to bring the resulting mixture to a pH of about 2 or below, c. treating the acidified ore with from about 5% to about 200% of the stoichiometric amount of nitric acid required to react with the ore, and recovering any NO x gas evolved from the ore, d. adding an acid resistant binder to the nitric acid-treated ore to form ore agglomerates capable of maintaining a porous bed of ore, maintaining the binder and ore in contact with one another for a sufficient curing time to permit the ore agglomerates to maintain their particulate form, and recovering any NO x evolved from the ore, e. placing the thus-treated ore in a heap permeable ore bed on top of an impermeable collector, f. heap treating the permeable ore bed by dispersing continuously or intermittently and aqueous nitric acid solution through the bed, g. separating residual acid liquor from the heap permeable ore bed, h. water washing the heap permeable ore bed to remove nitric acid solution therefrom, and separating the washings from the ore bed, i. introducing any NO x gases recovered from any of steps c. and d. into a nitric acid generator for conversion of the NO x into nitric acid recycling said nitric acid for use in treating said ore, j. treating the heap permeable ore bed with sufficient calcium, sodium or magnesium ions under alkaline conditions to increase the pH of the liquor removed from the bed to about 10 or above, k. treating the heap permeable ore bed by dispersing continuously or intermittently a lixiviate for precious metals through the bed, l. separating the lixiviate solution containing dissolved precious metals from the heap permeable ore bed and recovering said precious metals from the lixiviate.

Claim 25

A hydrometallurgical process for recovery of precious metals from an ore which is refractory to treatment by lixiviating agents comprising: a. crushing the ore to no finer than about a nominal 1/4 inch size, b. treating the crushed ore with a mineral acid in amounts to bring the resulting mixture to a pH of about 2 or below, c. treating the acidified ore with from about 5% to about 200% of the stoichiometric amount of nitric acid required to react with the ore, and recovering any NO x gas evolved from the ore, d. adding an acid resistant binder to the nitric acid-treated ore to form ore agglomerates capable of maintaining a porous bed of ore, maintaining the binder and ore in contact with one another for a sufficient curing time to permit the ore agglomerates to maintain their particulate form, and recovering any NO x evolved from the ore, e. placing the thus-treated ore in a heap permeable ore bed on top of an impermeable collector, f. heap treating the permeable ore bed by dispersing continuously or intermittently and aqueous nitric acid solution through the bed, g. separating residual acid liquor from the heap permeable ore bed, h. water washing the heap permeable ore bed to remove nitric acid solution therefrom, and separating the washings from the ore bed, i. introducing any NO x gases recovered from any of steps c. and d. into a nitric acid generator for conversion of the NO x into nitric acid recycling said nitric acid for use in treating said ore, j. treating the heap permeable ore bed with sufficient calcium, sodium or magnesium ions under alkaline conditions to increase the pH of the liquor removed from the bed to about 10 or above, k. treating the heap permeable ore bed by dispersing continuously or intermittently a lixiviate for precious metals through the bed, l. separating the lixiviate solution containing dissolved precious metals from the heap permeable ore bed and recovering said precious metals from the lixiviate.