Zinc recovery method

Patent metadata

Field	Value
Publication number	US-2025154676-A1
Application number	US-202318836436-A
Country	US
Kind code	A1
Filing date	Feb 14, 2023
Priority date	Feb 15, 2022
Publication date	May 15, 2025
Grant date	—

Abstract

A zinc recovery method includes an alkali fusion step ( 102 ) of, at a temperature equal to or higher than a melting point of sodium hydroxide, bringing a material ( 1 ) and molten sodium hydroxide being sodium hydroxide ( 5 ) or ( 14 ) in a molten state into contact with each other to decompose the zinc ferrite contained in the material ( 1 ) into zinc oxide components and iron oxide components in the molten sodium hydroxide, a water leaching step ( 103 ) of, at a temperature lower than a boiling point of water, bringing water into contact with sodium hydroxide being the molten sodium hydroxide with a decreased temperature, the zinc oxide components, and the iron oxide components and leaching the zinc oxide components in a sodium hydroxide aqueous solution.

First claim

1 . A zinc recovery method comprising:
an alkali fusion step of, at a first temperature equal to or higher than a melting point of sodium hydroxide, bringing a material containing zinc oxide components and zinc ferrite or a processed material obtained by processing the material and molten sodium hydroxide being sodium hydroxide in a molten state into contact with each other to decompose the zinc ferrite contained in the material or the processed material into zinc oxide components and iron oxide components in the molten sodium hydroxide; a water leaching step of, at a second temperature lower than a boiling point of water, bringing water into contact with sodium hydroxide being the molten sodium hydroxide with a decreased temperature, the zinc oxide components, and the iron oxide components and leaching the zinc oxide components in a sodium hydroxide aqueous solution to obtain a first zinc-containing aqueous solution containing zinc components and an insoluble material containing iron oxide components not dissolved in the sodium hydroxide aqueous solution; and a zinc recovery step of recovering zinc components derived from the first zinc-containing aqueous solution.

2 . The zinc recovery method according to claim 1 , wherein at least one of hydrogen peroxide and sodium nitrate as an oxidant or at least one of sodium sulfite, sodium thiosulfate, sodium dithionite, and zinc metal as a reductant is added to the sodium hydroxide in the alkali fusion step.

3 . The zinc recovery method according to claim 1 , further comprising a halogen washing step of, prior to the alkali fusion step, washing the material with a sodium hydroxide aqueous solution having a pH value in a range of 8.5 or more and 10.5 or less to wash halogen components contained in the material.

4 . The zinc recovery method according to claim 1 , further comprising:
a magnetic separation step of, prior to the alkali fusion step, applying magnetic force to the material or the processed material via a magnet and separating a first separated material composed of components attached to the magnet and a second separated material not attached to the magnet from each other in accordance with magnetic strengths of components in the material or the processed material; and an alkali aqueous solution leaching step, to which the second separated material is sent, of leaching zinc components contained in the second separated material in a sodium hydroxide aqueous solution to selectively extract the zinc components, to obtain a second zinc-containing aqueous solution containing the zinc components, wherein the first separated material is sent to the alkali fusion step as the processed material, and the zinc ferrite in the first separated material is decomposed into the zinc oxide components and the iron oxide components.

5 . The zinc recovery method according to claim 1 , further comprising a purifying step of purifying the first zinc-containing aqueous solution, wherein the purifying step includes a deironization step of bringing potassium permanganate or hydrogen peroxide as an oxidant into contact with the first zinc-containing aqueous solution to remove solidified iron, a desiliconization, carbonate removal, and defluorination step of bringing slaked lime or quicklime into contact with the first zinc-containing aqueous solution from which the iron has been removed to remove silicate, carbonate, and fluorine each of which has been solidified, and a cementation step of bringing metal zinc into contact with the first zinc-containing aqueous solution from which the iron, the silicate, the carbonate, and the fluorine have been removed to reduce and deposit metal impurity components nobler than zinc and remove the metal impurity components.

6 . The zinc recovery method according to claim 5 , wherein the zinc recovery step includes an electrowinning step of performing electrolysis using, as an electrolyte, the first zinc-containing aqueous solution or the first zinc-containing aqueous solution purified to obtain electrolytic zinc.

7 . The zinc recovery method according to claim 5 , wherein the zinc recovery step includes a zinc carbonate separating step of separating zinc components in the first zinc-containing aqueous solution or the first zinc-containing aqueous solution purified, as zinc carbonate.

8 . The zinc recovery method according to claim 4 , further comprising a purification step of purifying the second zinc-containing aqueous solution, wherein the purifying step includes a deironization step of bringing potassium permanganate or hydrogen peroxide as an oxidant into contact with the second zinc-containing aqueous solution to remove solidified iron, a desiliconization, carbonate removal, and defluorination step of bringing slaked lime or quicklime into contact with the second zinc-containing aqueous solution from which the iron has been removed to remove silicate, carbonate, and fluorine each of which has been solidified, and a cementation step of bringing metal zinc into contact with the second zinc-containing aqueous solution from which the iron, the silicate, the carbonate, and the fluorine have been removed to reduce and deposit metal impurity components nobler than zinc and remove the metal impurity components.

9 . The zinc recovery method according to claim 8 , wherein the zinc recovery step includes an electrowinning step of performing electrolysis using, as an electrolyte, the second zinc-containing aqueous solution or the second zinc-containing aqueous solution purified to obtain electrolytic zinc.

10 . The zinc recovery method according to claim 8 , wherein the zinc recovery step includes a zinc carbonate separating step of separating zinc components in the second zinc-containing aqueous solution or the second zinc-containing aqueous solution purified, as zinc carbonate.

11 . The zinc recovery method according to claim 1 , further comprising an alkali aqueous solution leaching step of, prior to the alkali fusion step, bringing the material or the processed material into contact with a sodium hydroxide aqueous solution and leaching zinc components contained in the material or the processed material in the sodium hydroxide aqueous solution to selectively extract the zinc components, to obtain a third zinc-containing aqueous solution containing the zinc components and an insoluble material containing zinc ferrite not dissolved in the sodium hydroxide aqueous solution, wherein
the insoluble material containing the zinc ferrite is sent to the alkali fusion step as the processed material, decomposed into zinc oxide components and iron oxide components, and in the water leaching step, the zinc oxide components are dissolved in the sodium hydroxide aqueous solution to obtain a fourth zinc-containing aqueous solution containing zinc components.

12 . The zinc recovery method according to claim 11 , wherein the fourth zinc-containing aqueous solution is sent to the alkali aqueous solution leaching step, and zinc components contained in the fourth zinc-containing aqueous solution are selectively extracted and become a part of the third zinc-containing aqueous solution.

13 . The zinc recovery method according to claim 11 , further comprising a halogen washing step of, prior to the alkali aqueous solution leaching step, washing the material with a sodium hydroxide aqueous solution having a pH value in a range of 8.5 or more and 10.5 or less to wash halogen components contained in the material and obtain a processed material.

14 . The zinc recovery method according to claim 11 , further comprising a purifying step of purifying the third zinc-containing aqueous solution, wherein the purifyin

Assignees

• Kinotech Corp
• Univ Tokyo

Inventors

• Haiki Kenji
• Matsuura Hiroyuki
• Motoba Kazuhiko
• Tomonaga Sakiko
• TAMAI Yoshie
• Mori Shuji

Classifications

• C25C7/06

  Operating or servicing · CPC title

• C22B3/44

  by chemical processes (treatment or purification of solutions by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42) · CPC title

• C22B3/22

  by physical processes, e.g. by filtration, by magnetic means {, or by thermal decomposition} (treatment or purification of solutions by liquid-liquid extraction C22B3/26) · CPC title

• C22B3/12

  in inorganic alkaline solutions · CPC title

• C25C1/16 Primary

  of zinc, cadmium or mercury · CPC title