Process for the preconcentration of metalliferous products

Claim 2

A process for the preconcentration of metalliferous values contained in a metal-bearing ore material selected from the group consisting of an ore and a byproduct thereof, comprising: (a) subjecting the ore material to careful attrition, so that the fraction d 80 /d 20 , wherein d 80 represents the smallest mesh which permits 80% of the ore material to pass through, and d 20 represents the smallest mesh which permits 20% of the ore material to pass through increases in the course of successive attritions; and (b) recovering a cut containing the metalliferous values in concentrated form from the resulting attrited particle mixture.

Claim 3

A process for the preconcentration of metalliferous values contained in a metal-bearing ore material selected from the group consisting of an ore and a byproduct thereof, comprising: (a) subjecting the ore material to careful attrition to obtain a particle mixture consisting of fine and coarse particles so that the fraction d 80 /d 20 , wherein d 80 represents the smallest mesh which permits 80% of the ore material to pass through, and d 20 represents the smallest mesh which permits 20% of the ore material to pass through, increases in the course of successive attritions; and (b) separating the fine particles from the coarse particles; and (c) recovering from the fine particles a cut consisting essentially of particles having a particle size not exceeding about 50 microns and containing the metalliferous values in concentrated form.

Claim 4

A process for the preconcentration of metalliferous values contained in a metal-bearing ore material selected from the group consisting of an ore and a byproduct thereof, comprising: (a) subjecting the ore material to careful attrition to obtain a particle mixture consisting of fine and coarse particles so that the fraction d 80 /d 20 , wherein d 80 represents the smallest mesh which permits 80% of the ore material to pass through, and d 20 represents the smallest mesh which permits 20% of the ore material to pass through, increases in the course of successive attritions; and (b) separating the fine particles from the coarse particles; and (c) recovering from the fine particles a cut consisting essentially of particles having a particle size not exceeding about 50 microns and containing the metalliferous values in concentrated form.

Claim 5

The process of claim 2 wherein the fine cut consists essentially of particles having a particle size not exceeding about 10 microns.

Claim 6

The process of claim 2 wherein the ore is pulverized prior to being subjected to the careful attrition of step (a).

Claim 7

The process of claim 2 wherein step (b) is carried out by a classification.

Claim 8

The process of claim 2 wherein the metal-bearing ore material is a member selected from the group consisting of uranium ores with carbonized gangue, manganese ores of sedimentary origin, phosphate ores with clay and/or carbonate containing gangue, bauxite ores of breccia structure where the bauxite is accompanied by silicified limestone, talc ores associated with a schist and a granite gangue and containing fine amounts of dolomite and pyrite, factory residues of zinc, and siderurgical dusts recovered from the exhausts of blast-furnaces and steelworks.

Claim 9

The process of claim 2 wherein the metal-bearing ore material is an ore which is transformed into a pulp before being subjected to the careful attrition of step (a).

Claim 10

The process of claim 7 wherein the transformation of the ore into a pulp is directly carried out on the vein by hydraulic breakage of the ore.

Claim 11

The process of claim 7 wherein the careful attrition of the pulp is carried out by simple agitation of the pulp.

Claim 12

The process of claim 2 wherein the metal-bearing ore material is transformed into a pulp, the pulp then subjected to careful attrition to obtain a particle mixture consisting essentially of fine particles in the form of a pulp and coarse particles in the form of a pulp, separating the fine particles in the form of a pulp from the coarse particles in the form of a pulp, mixing the separated fine particles in the form of a pulp with a flocculant at a pH to thicken the pulp of the fine particles, and recovering a fine cut, consisting essentially of particles having a particle size not exceeding about 50 microns and containing the metalliferous values in concentrated form, from the thickened pulp.

Claim 13

The process of claim 10 wherein the flocculant is an organic flocculant having at least one polar group selected from the group consisting of an amide, ether, and ester group.

Claim 14

The process of claim 10 wherein the flocculant is employed in an amount of about from 100 to 2000 grams of flocculant per ton of the dry particles issuing from the careful attrition step.

Claim 15

The process of claim 10 wherein the flocculant is employed in an amount of about from 100 to 500 grams of flocculant per ton of dry particles issuing from the careful attrition step.

Claim 16

The process of claim 2 wherein the careful attrition step is carried out in a dry format.

Claim 17

The process of claim 2 wherein the careful attrition step is carried out by means of a mill.

Claim 18

The process of claim 2 wherein the attrition step is carried out by means of the particles obtained from a previous attrition of the same metal-bearing ore material as the attrition medium.

Claim 19

The process of claim 16 wherein the particles obtained from the previous attrition have a particle size of about from 100 microns to 5 mm.

Claim 20

The process of claim 2 wherein the coarse particles obtained in step (b) are subjected to at least one additional careful attrition step (a) and thereafter processed according to steps (b) and (c) until an essentially complete separation of all the metal values has been accomplished.

Claim 21

The process of claim 2 wherein the ore material is the factory residue of zinc, the fine particles obtained are concentrated in lead and silver, and the coarse particles obtained are concentrated in zinc and silica.

Claim 22

The process of claim 2 wherein the ore material is a phosphate ore with clayey and/or carbonate containing gangue, and the fine particles obtained are concentrated in calcium carbonate, magnesium carbonate, and clay, while the coarse particles are concentrated in phosphate.

Claim 23

The method of claim 2 wherein the careful attrition step is carried out in a pulp, the amount of solid in the pulp is between 40% and 80%.

Claim 24

The method of claim 21 wherein the amount of solid in the pulp is between 65% and 75%.