IP Library Granted Patent US 10,494,696
Granted Patent B2
US 10,494,696 · App. 14/900,493 · Granted Dec 3, 2019

Metal recovery

Inventors: Narahari Pujari (Bangalore, IN); Siuli Sarkar (Bangalore, IN); Bawa Singh (Marlton, NJ); Daniel Goswami (Kolkata, IN)
Assignee: Alpha Assembly Solution Inc.
C22B25/06C01G19/00C22B25/04C23F1/30C23F1/44
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 10,494,696
App. No.
14/900,493
Granted
Dec 3, 2019
Kind
B2
Abstract

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.

Claims (35)

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.

Assignments (5)
ASSIGNMENT OF SECURITY INTEREST IN PATENT COLLATERAL Recorded Nov 17, 2022
From: BARCLAYS BANK PLC
To: CITIBANK, N.A.
Reel/Frame 061956/0643 →
SECURITY INTEREST Recorded Feb 5, 2019
From: ALPHA ASSEMBLY SOLUTIONS INC. (F/K/A ALPHA METALS, INC.)
To: BARCLAYS BANK PLC, AS COLLATERAL AGENT
Reel/Frame 048260/0683 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 2, 2017
From: PUJARI, NARAHARI; SARKAR, SIULI; SINGH, BAWA; GOSWAMI, DANIEL
To: FRY'S METALS, INC.
Reel/Frame 041157/0882 →
CHANGE OF NAME Recorded Feb 2, 2017
From: FRY'S METALS, INC.
To: ALPHA METALS, INC.
Reel/Frame 041594/0842 →
CHANGE OF NAME Recorded Feb 2, 2017
From: ALPHA METALS, INC.
To: ALPHA ASSEMBLY SOLUTIONS INC.
Reel/Frame 041595/0099 →
Continuity (2)
Provisional Application 61843595 · Jul 8, 2013
Related Publication 20160304989A1 · Oct 20, 2016