Process for the treatment of complex lead-zinc concentrates

Claim 2

A process for treating sulfide concentrates containing lead, copper, zinc and silver to selectively recover said metals therefrom, comprising the steps of: a. contacting said concentrate with sulfuric acid in the presence of oxygen at elevated temperature and pressure to extract copper and zinc materials from said concentrate; b. thereafter contacting said concentrate with lime to remove elemental sulfur therefrom; and c. thereafter by contacting said concentrate with a mixture of calcium chloride and ferric chloride to extract lead and silver materials therefrom.

Claim 3

The process of claim 1 wherein said extraction of copper and zinc is conducted at an oxygen pressure in the range of about 60 to about 80 psig and a temperature of at least about 100° C.

Claim 4

The process of claim 1 wherein said contacting with lime is conducted at a temperature of about 95° C.

Claim 5

The process of claim 3 wherein said contacting with lime is conducted in the presence of sulfide ions.

Claim 6

The process of claim 1 wherein said extraction of lead and silver is conducted at a pH of less than about 1.5.

Claim 7

The process of claim 1 further comprising treating the extracted copper and zinc materials to recover metallic copper and zinc therefrom.

Claim 8

The process of claim 6 wherein the treatment of said extracted copper material to recover metallic copper comprises contacting said copper materials with finely-divided zinc metal to cement copper metal on said zinc.

Claim 9

The process of claim 6 wherein the treatment of said zinc material to recover metallic zinc therefrom comprises electrolytically reducing zinc contained in said materials to its elemental state.

Claim 10

The process of claim 1 further comprising treating the extracted lead and silver materials to recover metallic lead and silver.

Claim 11

The process of claim 9 wherein said treatment of extracted silver materials to recover metallic silver therefrom comprises contacting said silver materials with finely-divided metallic lead to cement silver metal on said lead.

Claim 12

The process of claim 9 wherein said treatment of extracted lead material to recover metallic lead therefrom comprises recovering lead chloride and thereafter electrolytically reducing lead chloride in a fused chloride salt electrolyte to produce lead metal and chlorine gas for the regeneration of ferric chloride.

Claim 13

A process for treating sulfide concentrates containing lead, copper, zinc and silver to selectively recover said metals therefrom, comprising the steps of: a. contacting said concentrate with sulfuric acid in the presence of oxygen at a pressure of about 60 to 80 psi and a temperature of at least about 100° C; b. dividing the concentrate treated in a) into a first residue fraction and a first supernatant fraction; c. treating said first supernatant fraction to recover metallic copper and zinc therefrom; d. contacting said first residue fraction with lime at a temperature of about 95° C; e. dividing the material resulting from (d) into a second residue fraction and a second supernatant fraction; f. treating said second supernatant fraction to remove elemental sulfur therefrom; g. contacting said second residue fraction with a mixture of ferric chloride and calcium chloride and removing a third supernatant fraction from the material resulting from said contacting; and h. treating said third supernatant to recover metallic lead and silver therefrom.

Claim 14

A process for treating sulfide concentrates containing lead, copper, zinc and silver to selectively recover said metals therefrom, comprising the steps of: a. contacting said concentrate with sulfuric acid in the presence of oxygen at a pressure of about 60 to 80 psi and a temperature of at least about 100° C; b. dividing the concentrate treated in a) into a first residue fraction and a first supernatant fraction; c. treating said first supernatant fraction to recover metallic copper and zinc therefrom; d. contacting said first residue fraction with lime at a temperature of about 95° C; e. dividing the material resulting from (d) into a second residue fraction and a second supernatant fraction; f. treating said second supernatant fraction to remove elemental sulfur therefrom; g. contacting said second residue fraction with a mixture of ferric chloride and calcium chloride and removing a third supernatant fraction from the material resulting from said contacting; and h. treating said third supernatant to recover metallic lead and silver therefrom.

Claim 15

A process for treating sulfide concentrates containing lead, copper, zinc and silver to selectively recover said metals therefrom, and in which the gangue mineral pyrite remains substantially inert at all stages of the process, comprising the steps of: a. contacting said concentrate with sulfuric acid in the presence of oxygen at elevated temperature and pressure to extract copper and zinc materials from said concentrate; b. thereafter contacting said concentrate with lime to remove elemental sulfur therefrom; and c. thereafter by contacting said concentrate with a mixture of calcium chloride and ferric chloride to extract lead and silver materials therefrom.

Claim 16

A process for treating sulfide concentrates containing lead, copper, zinc and silver to selectively recover said metals therefrom, and in which the gangue mineral pyrite remains substantially inert at all stages of the process, comprising the steps of: a. contacting said concentrate with sulfuric acid in the presence of oxygen at elevated temperature and pressure to extract copper and zinc materials from said concentrate; b. thereafter contacting said concentrate with lime to remove elemental sulfur therefrom; and c. thereafter by contacting said concentrate with a mixture of calcium chloride and ferric chloride to extract lead and silver materials therefrom.

Claim 17

A process for treating sulfide concentrates containing lead, copper, zinc and silver to selectively recover said metals therefrom, and in which the gangue mineral pyrite remains substantially inert at all stages of the process, comprising the steps of: a. contacting said concentrate with sulfuric acid in the presence of oxygen at elevated temperature and pressure to extract copper and zinc materials from said concentrates; b. thereafter contacting said concentrate with lime and/or sulfide containing solution to remove elemental sulfur therefrom and to activate refractory silver-containing minerals in the concentrate; and c. thereafter by contacting said concentrate with a mixture of calcium chloride and ferric chloride to extract lead and silver materials therefrom.

Claim 18

A process for treating sulfide concentrates containing lead, copper, zinc and silver to selectively recover said metals therefrom, and in which the gangue mineral pyrite remains substantially inert at all stages of the process, comprising the steps of: a. contacting said concentrate with sulfuric acid in the presence of oxygen at elevated temperature and pressure to extract copper and zinc materials from said concentrates; b. thereafter contacting said concentrate with lime and/or sulfide containing solution to remove elemental sulfur therefrom and to activate refractory silver-containing minerals in the concentrate; and c. thereafter by contacting said concentrate with a mixture of calcium chloride and ferric chloride to extract lead and silver materials therefrom.