Simultaneous extraction of metal values other than copper from manganese nodules

Claim 2

A process for selectively removing metal values from a manganese nodule ore, the ore comprising primary proportions of manganese and iron and the predominant secondary metals being nickel, copper and cobalt, the process comprising the steps of: (a) reducing the manganese nodule ore, whereby the manganese value is rendered soluble in an ammoniated aqueous solution but whereby the copper value in the ore is reduced to a state at which it cannot be leached by ammoniated solution unless the copper value is oxidized; (b) leaching the reduced ore with an aqueous ammoniated solution of an ammonium salt substantially without oxidizing the copper value so as to form an aqueous pregnant leach solution comprising the dissolved manganese, nickel and cobalt salts and a solid leached ore comprising the undissolved copper value, the pregnant leach solution being substantially free of dissolved copper salt, the leaching solution comprising at least about 150 gm/liter of total ammonium (NH 4 +) ion, the concentration of ammonium hydroxide in the leaching solution being at least about 120 gm/liter, as ammonium ion, and a concentration of ammonium salt anion of at least about 0.83 Normal; and (c) oxidizing the solid leached ore residue so as to oxidize the copper value to a valence state at which it can be leached with an ammoniated aqueous solution and releaching the oxidized leached ore with an ammoniated aqueous solution of an ammonium salt to form an aqueous pregnant releach solution comprising dissolved copper salt and a solid residue.

Claim 3

The process of claim 1, wherein the amount of ammonium salt in the leaching solution is at least about substantially the stoichiometric amount required to react with all of the manganese and iron in the ore.

Claim 4

The process of claim 2, wherein the nickel and cobalt values in the ore are reduced during reduction of the ore to a state in which they are insoluble in the ammoniated leach solution and wherein the leaching solution-ore mixture is exposed to the atmosphere under mildly oxidative conditions, whereby the nickel and cobalt are oxidized to a leachable state without oxidizing the copper.

Claim 5

The process of claim 2, wherein the ammonium salt in each of the leaching solutions and the releaching solution is selected from the group consisting of ammonium sulfate, ammonium chloride, and ammonium nitrate.

Claim 6

The process of claim 1, wherein the leaching solution comprises dissolved ammonium carbonate.

Claim 7

The process of claim 1, wherein the leached ore is simultaneously aerated and releached.

Claim 8

The process of claim 1, wherein the releaching solution comprises a concentration of NH 4 OH of at least about 0.5 mols/liter.

Claim 9

The process of claim 1, wherein the releaching solution comprises a concentration of ammonium salt of at least about 0.25 Normal.

Claim 10

The process of claim 1, wherein the nodule ore is reduced at a temperature in the range of from 300 to about 850° C.

Claim 11

The process of claim 9, comprising in addition drying the nodule ore prior to reduction.

Claim 12

The process of claim 10, wherein the nodule ore is dried at a temperature in the range of from about 150° C. to about 250° C.

Claim 13

The process of claim 9, wherein the nodule ore is reduced by being reacted with a reducing agent selected from the group consisting of a carbonaceous reducing agent and a hydrogen-containing reducing agent.

Claim 14

The process of claim 12, wherein the carbonaceous reducing agent is selected from the group consisting of carbon, hydrocarbon compounds and carbon monoxide.

Claim 15

A process for selectively extracting the metal values from a manganese nodule ore, the ore comprising a primary proportion of manganese and iron and the predominant secondary metals being nickel, copper and cobalt, the weight ratio of manganese: iron being at least about 5:1 and the ore containing from 0.8 to 1.8 percent by wt. of copper and 1 to 2 percent by wt. of nickel, the processing comprising: (a) comminuting the ore to a particle size of not greater than about 20 mesh; (b) reducing the comminuted ore, at a temperature in the range of from about 300 to about 850° C., in the presence of a reducing agent selected from the group consisting of carbonaceous materials and hydrogen, such that the manganese value is reduced to a condition in which the metal value is leachable by ammoniacal ammonium salt solutions and the copper value is reduced to a state at which it cannot be leached by ammoniacal ammonium salt solution without being oxidized; (c) leaching the reduced ore with an aqueous ammoniated solution of an ammonium salt to form a pregnant leach solution comprising dissolved manganese salt, cobalt salt, and nickel salt, but substantially free of dissolved copper salt, and a solid leached reduced ore; (d) oxidizing the leached reduced ore so as to oxidize the copper value to a valence state at which it can be leached with an ammoniated ammonium salt solution, and releaching the oxidized solid leached ore with an ammoniated aqueous solution of an ammonium salt to form an aqueous pregnant releach solution comprising dissolved copper salt, and a solid final residue; and (e) sparging the pregnant leach solution to removed sufficient ammonia to obtain the precipitation of substantially all of the iron and manganese values therefrom to form a substantially manganeseand-iron-free pregnant leach solution and solid manganese and iron compounds; and (f) extracting the nickel and cobalt values from the leach solution so as to regenerate the ammoniated ammonium salt leaching solution.

Claim 16

A process for selectively extracting the metal values from a manganese nodule ore, the ore comprising a primary proportion of manganese and iron and the predominant secondary metals being nickel, copper and cobalt, the weight ratio of manganese: iron being at least about 5:1 and the ore containing from 0.8 to 1.8 percent by wt. of copper and 1 to 2 percent by wt. of nickel, the processing comprising: (a) comminuting the ore to a particle size of not greater than about 20 mesh; (b) reducing the comminuted ore, at a temperature in the range of from about 300 to about 850° C., in the presence of a reducing agent selected from the group consisting of carbonaceous materials and hydrogen, such that the manganese value is reduced to a condition in which the metal value is leachable by ammoniacal ammonium salt solutions and the copper value is reduced to a state at which it cannot be leached by ammoniacal ammonium salt solution without being oxidized; (c) leaching the reduced ore with an aqueous ammoniated solution of an ammonium salt to form a pregnant leach solution comprising dissolved manganese salt, cobalt salt, and nickel salt, but substantially free of dissolved copper salt, and a solid leached reduced ore; (d) oxidizing the leached reduced ore so as to oxidize the copper value to a valence state at which it can be leached with an ammoniated ammonium salt solution, and releaching the oxidized solid leached ore with an ammoniated aqueous solution of an ammonium salt to form an aqueous pregnant releach solution comprising dissolved copper salt, and a solid final residue; and (e) sparging the pregnant leach solution to removed sufficient ammonia to obtain the precipitation of substantially all of the iron and manganese values therefrom to form a substantially manganeseand-iron-free pregnant leach solution and solid manganese and iron compounds; and (f) extracting the nickel and cobalt values from the leach solution so as to regenerate the ammoniated ammonium salt leaching solution.

Claim 17

The process of claim 14, wherein the regenerated ammoniated ammonium salt leaching solution is recycled and used to leach additional reduced ore.

Claim 18

The process of claim 15, wherein the sparging is carried out using air and wherein the ammonium salt is ammonium carbonate, whereby manganese carbonate and iron carbonate are precipitated and further comprising thermally decomposing the manganese and iron salts so as to form the corresponding oxides and carbon dioxide, and contacting the carbon dioxide and ammonia removed during sparging, with the regenerated ammoniated ammonium salt leaching solution to form the ammonium carbonate leaching solution and recycling the leaching solution to contact reduced nodule ore.

Claim 19

The process of claim 16, comprising in addition extracting the copper value from the pregnant releaching solution so as to regenerate the ammoniated ammonium salt releaching solution and recycling the regenerated releaching solution to contact leached reduced ore.

Claim 20

The process of claim 14, wherein the regenerated ammoniated ammonium salt leaching solution is utilized as the releaching solution to releach the leached reduced ore residue.

Claim 21

The process of claim 18, comprising in addition extracting the copper value from the pregnant releach solution so as to regenerate the ammoniated ammonium salt leaching solution and recycling the leaching solution to contact reduced nodule ore.

Claim 22

The process of claim 18, wherein the ammonium salt is ammonium carbonate and where in the sparging is carried out with air, and further comprising thermally decomposing the manganese and iron salts precipitated so as to form the corresponding oxide and carbon dioxide, and contacting the carbon dioxide and ammonia with the regenerated ammoniated ammonium salt releaching solution to form the ammonium carbonate leaching solution and recycling to contact reduced nodule ore.

Claim 23

The process of claim 14, wherein the nickel value is selectively extracted from the leach solution by contacting the leach solution with a liquid ion exchange solution selected from the group consisting of alphahydroxyoximes and 7-hydrocarbon-substituted-8-hydroxyquino lines.

Claim 24

The process of claim 14, wherein the aqueous ammoniated solution comprises at least about 260 grams/liter of total ammonium (NH 4 + ) ion, the concentration of ammonium hydroxide in the leaching solution being at least about 120 grams/liter as ammonium ion, and the concentration of ammonium salt anion is at least about 0.83 Normal.