Fluidized hydrogen reduction process for the recovery of copper

Claim 2

In a process for recovering elemental copper and copper-bearing materials selected from the group consisting of copper oxides and copper salts by means of reducing the copper-bearing materials with hydrogen in a fluidized bed reactor, the improvement comprising: performing the reduction in the presence of sufficient chemically inert, relatively smooth, generally spherical particles in order to restrain sintering of the reduced copper.

Claim 3

The process of claim 1 wherein the copper-bearing material is cuprous chloride.

Claim 4

The process of claim 1 wherein the copper-bearing material is cupric chloride.

Claim 5

The process of claim 1 wherein the reaction temperature is maintained from about 400° C. to about 600° C.

Claim 6

The process of claim 1 wherein the particles have a relatively low apparent porosity.

Claim 7

The process of claim 1 wherein the particles comprise sand.

Claim 8

The process of claim 1 wherein the melting point of the particles is greater than the maximum temperature in the reactor.

Claim 9

The process of claim 1 wherein the particles range in size from about 9 to about 150 mesh within a space velocity range of about 1 to about 5 feet per second.

Claim 10

The process of claim 1 wherein the amount of particles is from about 0.7 to about 10 times by weight of the amount of the feed material.

Claim 11

In a process for recovering elemental copper from copper-bearing materials selected from the group consisting of copper oxides and copper salts by means of reducing the copper-bearing materials with hydrogen in a fluidized bed reactor, the improvement comprising: performing the reduction at a temperature of from about 400° C. to about 600° C. in the presence of from about 0.7 to about 10 times by weight based on the amount of copper-bearing feed material of particles ranging in size from about 9 to about 150 mesh, the particles being characterized as being chemically inert with respect to the reactants in the reactor, and having relatively smooth, generally spherical surface areas with relatively low apparent porosities in order to restrain sintering of the reduced copper.

Claim 12

In a process for recovering elemental copper from copper-bearing materials selected from the group consisting of copper oxides and copper salts by means of reducing the copper-bearing materials with hydrogen in a fluidized bed reactor, the improvement comprising: performing the reduction at a temperature of from about 400° C. to about 600° C. in the presence of from about 0.7 to about 10 times by weight based on the amount of copper-bearing feed material of particles ranging in size from about 9 to about 150 mesh, the particles being characterized as being chemically inert with respect to the reactants in the reactor, and having relatively smooth, generally spherical surface areas with relatively low apparent porosities in order to restrain sintering of the reduced copper.

Claim 13

The process of claim 10 wherein the copper-bearing feed material is cuprous chloride.

Claim 14

The process of claim 10 wherein the copper-bearing feed material is cupric chloride.

Claim 15

The process of claim 10 wherein the particles comprise sand.

Claim 16

In a process for recovering elemental copper from cuprous chloride by means of reducing the cuprous chloride with hydrogen in a fluidized bed reactor, the improvement comprising: performing the reduction in the presence of from about 0.7 to about 10 times based on the weight of cuprous chloride feed material of sand ranging in size from about minus 20 to about plus 48 mesh, the sand particles possessing a relatively smooth surface area and being generally spherical in shape in order to restrain sintering of the reduced copper.

Claim 17

In a process for recovering elemental copper from cuprous chloride by means of reducing the cuprous chloride with hydrogen in a fluidized bed reactor, the improvement comprising: performing the reduction in the presence of from about 0.7 to about 10 times based on the weight of cuprous chloride feed material of sand ranging in size from about minus 20 to about plus 48 mesh, the sand particles possessing a relatively smooth surface area and being generally spherical in shape in order to restrain sintering of the reduced copper.

Claim 18

The process of claim 14 wherein the temperature of the reaction is maintained from about 400° C. to about 600° C.

Claim 19

The process of claim 14 wherein the ratio based on weight of sand to cuprous chloride feed material is from about 1 to about 5.

Claim 20

The process of claim 14 wherein at least the stoichiometric amount of hydrogen is employed in the reduction process.