Method for recovering lead oxide from waste lead paste
US-10135100-B2 · Nov 20, 2018 · US
US2023304125A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023304125-A1 |
| Application number | US-202217883262-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 8, 2022 |
| Priority date | Mar 28, 2022 |
| Publication date | Sep 28, 2023 |
| Grant date | — |
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A method for recovering a valuable material from a perovskite solar cell includes immersing a perovskite solar cell device in an organic solvent to dissolve a monovalent metal cation, a divalent metal cation, and two halogen anions in the organic solvent, followed by adding an oxidizing agent and conducting a heating treatment to form a solid phase residue and a halogen molecule, dissolving the halogen molecule in deionized water to form a halogen solution, rinsing the solid phase residue with deionized water to obtain a solid phase and a liquid phase, calcining the solid phase into a metal oxide, or mixing the solid phase with the halogen solution to obtain a first metal halide, subjecting the liquid phase to an extraction treatment to form an oil phase layer, followed by conducting a back-extraction treatment, adding the halogen solution, and conducting a vacuum concentration treatment to obtain a second metal halide.
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What is claimed is: 1 . A method for recovering a valuable material from a perovskite solar cell, comprising: (a) immersing a perovskite solar cell device in an organic solvent to separate an absorbing layer containing at least one monovalent metal cation, at least one divalent metal cation, and at least two halogen anions, an electron transport layer, and a transparent conductive layer from the perovskite solar cell device, and to dissolve the at least one monovalent metal cation, the at least one divalent metal cation, and the at least two halogen anions of the absorbing layer in the organic solvent; (b) adding an oxidizing agent to the organic solvent to obtain a mixture containing a halogen molecule formed by oxidation of one of the two halogen anions; (c) heating the mixture until dry to form a solid phase residue containing the at least one monovalent metal cation, the at least one divalent metal cation, and the other one of the two halogen anions, and to sublime and recover the halogen molecule; (d) dissolving the recovered halogen molecule in step (c) in deionized water to form a recovered halogen solution; (e) rinsing the solid phase residue in step (c) with deionized water to obtain a solid phase containing a hydroxide of the divalent metal and a liquid phase containing the at least one monovalent metal cation, the at least one divalent metal cation, and the other one of the two halogen anions; (f) calcining the solid phase containing the hydroxide of the divalent metal in step (e) into a metal oxide, or dissolving the solid phase containing the hydroxide of the divalent metal in step (e) in an aqueous solution, followed by mixing with the recovered halogen solution in step (d), so as to obtain a first metal halide; (g) subjecting the liquid phase containing the at least one monovalent metal cation, the at least one divalent metal cation, and the other one of the two halogen anions in step (e) to an extraction treatment with an extractant diluted with an oil, so as to form an oil phase layer containing the at least one monovalent metal cation, and a water phase layer containing the at least one divalent metal cation and the other one of the two halogen anions, wherein the extractant is 4-tert-butyl-2-(α-methylbenzyl)phenol; (h) subjecting the oil phase layer containing the at least one monovalent metal cation in step (g) to a back-extraction treatment with an ammonium hydroxide solution, so as to obtain an aqueous phase solution containing the at least one monovalent metal cation; and (i) adding the recovered halogen solution in step (d) to the aqueous phase solution containing the at least one monovalent metal cation in step (h), followed by conducting a vacuum concentration treatment, so as to obtain a second metal halide. 2 . The method according to claim 1 , further comprising: (j) subjecting the water phase layer containing the at least one divalent metal cation and the other one of the two halogen anions in step (g) to a vacuum concentration treatment, so as to obtain a third metal halide. 3 . The method according to claim 1 , wherein in step (a), the absorbing layer includes a composition selected from the group consisting of a composition of formula CsPbBr X I 3-X , a composition of formula CsMAFAPb(Br X I 1-X ) 3 , and a combination thereof, and is subjected to degradation before step (a), the at least one monovalent metal cation and the at least one divalent metal cation are Cs + and Pb 2+ respectively, in step (b), the halogen molecule is formed by oxidation of I − , and in step (c), the halogen anion present in the solid phase residue is Br − . 4 . The method according to claim 3 , wherein the organic solvent in step (a) is dimethylformamide, the oxidizing agent in step (b) is hydrogen peroxide, the solid phase residue in step (c) contains Cs + , Pb 2+ , and Br − , the halogen molecule in step (c) is I 2 vapor, and the recovered halogen solution in step (d) is I 2 solution. 5 . The method according to claim 4 , wherein in step (e), the solid phase contains Pb(OH) 2 , and the liquid phase contains Cs + , Pb 2+ , and Br − . 6 . The method according to claim 5 , wherein in step (f), the metal oxide formed by calcining the solid phase in step (e) is PbO, and the first metal halide, which is obtained by dissolving the solid phase in step (e) in a nitric acid solution and then mixing with the recovered I 2 solution in step (d), is PbI 2 . 7 . The method according to claim 6 , wherein in step (g), the extractant is diluted with kerosene and has a concentration ranging from 0.001 mol/L to 0. 4 mol/L and a pH value ranging from 5 to 8, a volume ratio of the oil phase layer to the water phase layer in decimal form ranges from 0.1 to 2.0, the extraction treatment is conducted for a time period of not greater than 20 minutes, the oil phase layer contains Cs + , and the water phase layer contains Pb 2+ and Br − . 8 . The method according to claim 7 , wherein in step (h), the ammonium hydroxide solution has a concentration ranging from 0.1 mol/L to 2.0 mol/L, a volume ratio of the oil phase layer to the ammonium hydroxide solution in decimal form is not greater than 2.0, the back-extraction treatment is conducted for a time period ranging from 5 minutes to 25 minutes, the aqueous phase solution contains Cs + , and in step (i), the second metal halide is CsI. 9 . The method according to claim 7 , further comprising: (j) subjecting the water phase layer containing Pb 2+ and Br − in step (g) to a vacuum concentration treatment, so as to obtain PbBr 2 .
Recovery from waste materials · CPC title
Nitric acids or salts thereof · CPC title
using alcohols or phenols · CPC title
Obtaining alkali metals · CPC title
by acid leaching · CPC title
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