Recovering zinc from a material containing zinc and iron

Claim 1

The method of recovering zinc from a material containing zinc and iron, comprising (a) leaching the material with an aqueous solution of sulfuric acid, the sulfuric acid being added in a quantity to produce a pH of from about 3 to about 5.5 in the final stage of the leaching process, so as to dissolve the zinc but not the iron contained in the material, (b) adding zinc powder to the leaching solution thus obtained, in order to reduce the content of metallic impurities in the leaching solution, (c) extracting zinc from the aqueous solution thus obtained by contacting it, in a liquid-liquid extraction process, with a solution of a dialkyl phosphoric acid in an organic solvent, (d) returning the aqueous raffinate leaving the extraction process to renewed leaching, (e) re-extracting zinc from the organic solution by contacting it, in a liquid-liquid extraction process, with an aqueous solution containing from about 40 to about 600 grams per liter of sulfuric acid in such quantity that the sulfuric acid solution leaving the re-extraction process contains from about 60 to about 150 grams per liter of zinc, (f) returning the organic solution leaving the re-extraction process to renewed extraction, and (g) recovering zinc from the zinc-containing sulfuric acid solution.

Claim 2

The method of recovering zinc from a material containing zinc and iron, comprising (a) leaching the material with an aqueous solution of sulfuric acid, the sulfuric acid being added in a quantity to produce a pH of from about 3 to about 5.5 in the final stage of the leaching process, so as to dissolve the zinc but not the iron contained in the material, (b) adding zinc powder to the leaching solution thus obtained, in order to reduce the content of metallic impurities in the leaching solution, (c) extracting zinc from the aqueous solution thus obtained by contacting it, in a liquid-liquid extraction process, with a solution of a dialkyl phosphoric acid in an organic solvent, (d) returning the aqueous raffinate leaving the extraction process to renewed leaching, (e) re-extracting zinc from the organic solution by contacting it, in a liquid-liquid extraction process, with an aqueous solution containing from about 40 to about 600 grams per liter of sulfuric acid in such quantity that the sulfuric acid solution leaving the re-extraction process contains from about 60 to about 150 grams per liter of zinc, (f) returning the organic solution leaving the re-extraction process to renewed extraction, and (g) recovering zinc from the zinc-containing sulfuric acid solution.

Claim 6

A method of recovering zinc and copper from a material containing zinc, copper and iron, comprising (a) leaching the material at a pH of at most 3, (b) recovering copper from the leaching solution by means of a liquid-liquid extraction process, (c) increasing the pH of the leaching solution to from about 3 to about 5.5 by the addition of alkaline material or by the addition of more material to be leached, (d) adding zinc powder to the leaching solution thus obtained, in order to reduce the content of metallic impurities in the leaching solution, (e) extracting zinc from the aqueous solution thus obtained by contacting it, in a liquid-liquid extraction process, with a solution of a dialkyl phosphoric acid in an organic solvent, (f) returning the aqueous raffinate leaving the extraction process to renewed leaching, (g) re-extracting zinc from the organic solution by contacting it, in a liquid-liquid extraction process, with an aqueous solution containing from about 40 to about 600 grams per liter of sulphuric acid in such quantity that the sulphuric acid solution leaving the re-extraction process contains from about 60 to about 150 grams per liter of zinc, (h) returning the organic solution leaving the re-extraction process to renewed extraction, and (i) recovering zinc from the zinc-containing sulphuric acid solution.

Claim 7

A method of recovering zinc and copper from a material containing zinc, copper and iron, comprising (a) leaching the material at a pH of at most 3, (b) recovering copper from the leaching solution by means of a liquid-liquid extraction process, (c) increasing the pH of the leaching solution to from about 3 to about 5.5 by the addition of alkaline material or by the addition of more material to be leached, (d) adding zinc powder to the leaching solution thus obtained, in order to reduce the content of metallic impurities in the leaching solution, (e) extracting zinc from the aqueous solution thus obtained by contacting it, in a liquid-liquid extraction process, with a solution of a dialkyl phosphoric acid in an organic solvent, (f) returning the aqueous raffinate leaving the extraction process to renewed leaching, (g) re-extracting zinc from the organic solution by contacting it, in a liquid-liquid extraction process, with an aqueous solution containing from about 40 to about 600 grams per liter of sulphuric acid in such quantity that the sulphuric acid solution leaving the re-extraction process contains from about 60 to about 150 grams per liter of zinc, (h) returning the organic solution leaving the re-extraction process to renewed extraction, and (i) recovering zinc from the zinc-containing sulphuric acid solution.

Claim 8

A method of recovering zinc and copper from a material containing zinc, copper, and iron, comprising (a) leaching the material with an aqueous solution of sulphuric acid at a pH of at most 3, (b) extracting copper from the aqueous leaching solution, in a liquid-liquid extraction process, with a solution of a copper extractant in an organic solution, (c) re-extracting copper from the organic solution by contacting the organic solution, in a liquid-liquid extraction process with an aqueous solution containing from about 100 to about 30 grams per liter of sulphuric acid in such quantity that the sulphuric acid solution leaving the re-extraction process contains from about 10 to about 30 grams per liter of copper, returning the organic solution leaving the re-extraction process to renewed extraction of copper, (e) recovering copper from the copper-containing sulphuric acid solution, (f) adding more material to be leached, or an alkaline material, to the aqueous raffinate from the copper extraction process in order to raise the pH of the raffinate to from about 3 to about 5.5, (g) adding zinc powder to the solution thus obtained in order to reduce the content of metallic impurities in the solution, (h) recovering zinc from the solution thus obtained by contacting it, in a liquid-liquid extraction process, with a solution of a dialkyl phosphoric acid in an organic solvent, (i) returning the aqueous raffinate leaving the extraction process to renewed leaching, (j) re-extracting zinc from the organic solution by contacting it, in a liquid-liquid extraction process, with an aqueous solution containing from about 40 to about 600 grams per liter of sulphuric acid in such quantity that the sulphuric acid solution leaving the re-extraction process contains from about 60 to about 150 grams per liter of zinc, (k) returning the organic solution leaving the re-extraction process to renewed extraction, and (l) recovering zinc from the zinc-containing sulphuric acid solution.

Claim 9

A method of recovering zinc and copper from a material containing zinc, copper, and iron, comprising (a) leaching the material with an aqueous solution of sulphuric acid at a pH of at most 3, (b) extracting copper from the aqueous leaching solution, in a liquid-liquid extraction process, with a solution of a copper extractant in an organic solution, (c) re-extracting copper from the organic solution by contacting the organic solution, in a liquid-liquid extraction process with an aqueous solution containing from about 100 to about 30 grams per liter of sulphuric acid in such quantity that the sulphuric acid solution leaving the re-extraction process contains from about 10 to about 30 grams per liter of copper, returning the organic solution leaving the re-extraction process to renewed extraction of copper, (e) recovering copper from the copper-containing sulphuric acid solution, (f) adding more material to be leached, or an alkaline material, to the aqueous raffinate from the copper extraction process in order to raise the pH of the raffinate to from about 3 to about 5.5, (g) adding zinc powder to the solution thus obtained in order to reduce the content of metallic impurities in the solution, (h) recovering zinc from the solution thus obtained by contacting it, in a liquid-liquid extraction process, with a solution of a dialkyl phosphoric acid in an organic solvent, (i) returning the aqueous raffinate leaving the extraction process to renewed leaching, (j) re-extracting zinc from the organic solution by contacting it, in a liquid-liquid extraction process, with an aqueous solution containing from about 40 to about 600 grams per liter of sulphuric acid in such quantity that the sulphuric acid solution leaving the re-extraction process contains from about 60 to about 150 grams per liter of zinc, (k) returning the organic solution leaving the re-extraction process to renewed extraction, and (l) recovering zinc from the zinc-containing sulphuric acid solution.