Reactor systems and processes for light hydrocarbon catalytic cracking to produce high value hydrogen and solid carbon
US-2026062299-A1 · Mar 5, 2026 · US
US10494696B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10494696-B2 |
| Application number | US-201414900493-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 2, 2014 |
| Priority date | Jul 8, 2013 |
| Publication date | Dec 3, 2019 |
| Grant date | Dec 3, 2019 |
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A method for recovering tin and/or tin alloy from a substrate comprising providing a substrate having tin and/or tin alloy thereon; contacting the tin and/or tin alloy with a stripping solution comprising an inorganic acid and a persulfate compound; recovering tin salt and/or tin alloy salt precipitated from the stripping solution; and recovering tin and/or tin alloy from the tin salt and/or tin alloy salt, respectively.
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The invention claimed is: 1. A method for recovering tin and/or tin alloy from a substrate comprising: providing a substrate having tin and/or tin alloy thereon; contacting the tin and/or tin alloy with a stripping solution consisting essentially of an inorganic acid and a persulfate compound; adding a flocculant to the stripping solution; recovering tin salt and/or tin alloy salt precipitated from the stripping solution; and recovering tin and/or tin alloy from the tin salt and/or tin alloy salt, respectively, wherein the inorganic acid is selected from sulfuric acid, hydrochloric acid and alkane sulfonic acid; and wherein the persulfate compound is selected from ammonium persulfate, sodium persulfate, barium persulfate, lithium persulfate and combinations of two or more thereof; and wherein the persulfate compound is present in a concentration from about 100 to about 500 g/l. 2. The method of claim 1 , wherein the substrate comprises copper and/or copper alloy. 3. The method of claim 1 , wherein the tin and/or tin alloy is recovered from the tin salt and/or tin alloy salt by smelting. 4. The method of claim 1 wherein the substrate is part of a photovoltaic interconnection ribbon, busbar, or electronic waste. 5. The method of claim 1 wherein the tin and/or tin alloy is contacted with the stripping solution for at least about 1 minute. 6. The method of claim 1 wherein the tin salt and/or tin alloy salt is recovered from the stripping solution by filtration or centrifugation. 7. The method of claim 1 wherein the concentration of the inorganic acid is between about 10 to about 500 g/l. 8. The method of claim 1 wherein the stripping solution further consists essentially of one or more of imidazole, pyridine, triazine, triazole and derivatives thereof. 9. The method of claim 8 wherein the triazole derivative is benzotriazole and benzotriazole is present in the stripping solution from about 0.1 to about 10 g/l. 10. The method of claim 1 wherein the stripping solution further consists essentially of a surfactant. 11. The method according to claim 10 , wherein the stripping solution consists essentially of: 10 g/L to 500 g/L an inorganic acid selected from sulfuric acid, hydrochloric acid and alkane sulfonic acid; 100 g/L to 500 g/L of a persulfate compound selected from ammonium persulfate, sodium persulfate, barium persulfate, lithium persulfate and combinations of two or more thereof; 0.1 g/L to 10 g/L benzotriazole; and 2.0 wt. % of less of a surfactant. 12. The method of claim 1 wherein contacting the tin and/or tin alloy with a stripping solution comprises immersing the tin and/or tin alloy in the stripping solution. 13. The method of claim 1 wherein the solution further consists essentially of an aqueous solvent. 14. The method of claim 1 wherein the method is a batch method and the method further comprises re-cycling the stripping solution between batches. 15. The method according to claim 1 , wherein the method for recovering tin and/or tin alloy does not require subsequent electrowinning and/or a pH precipitation step. 16. A method of removing tin and/or tin alloy from a copper substrate comprising: providing a copper substrate having tin and/or tin alloy thereon; and contacting the tin and/or tin alloy with a stripping solution consisting essentially of an inorganic acid and a persulfate compound, wherein the inorganic acid is selected from sulfuric acid, hydrochloric acid and alkane sulfonic acid; and wherein the persulfate compound is selected from ammonium persulfate, sodium persulfate, barium persulfate, lithium persulfate and combinations of two or more thereof; and adding a flocculant to the stripping solution. 17. The method of claim 16 further comprising recovering the copper substrate from the stripping solution.
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