Apparatus and method for stripping solder metals during the recycling of waste electrical and electronic equipment

• US 9,649,712 B2
• Filed: 07/20/2015
• Issued: 05/16/2017
• Est. Priority Date: 12/15/2011
• Status: Expired due to Fees

• Current Assignee: Entegris Incorporated
• Original Assignee: Entegris Incorporated
• Inventors: Jiang, Ping, Chen, Tianniu, Korzenski, Michael B.
• Primary Examiner(s): STONER, KILEY SHAWN
• Application Number:
  US14/803,936
• Publication Number:
  US 20150322545A1
• Time in Patent Office: 666 Days
• Field of Search: None
• CPC Class Codes: B09B 3/00 Destroying solid waste or transforming solid waste into something useful or harmless
• CPC Class Codes: B09B 5/00 Operations not covered by a single other subclass or by a single other group in this subclass
• CPC Class Codes: B23K 1/018 Unsoldering; Removal of melted solder or other residues
• CPC Class Codes: B23K 3/08 Auxiliary devices therefor cleaning pipes or tubes or systems of pipes or tubes, e.g. before soldering, B08B9/02
• CPC Class Codes: B23K 37/00 Auxiliary devices or processes, not specially adapted to a procedure covered by only one of the preceding main groups eye-shields for welders worn on the operator's body or carried in the hand A61F9/00 , i.e. A61F9/02; applicable to metal-working machines other than soldering, welding, or flame-cutting machines B23Q; laser protective screens B23K26/706; protective shields for other welding methods F16P1/06
• CPC Class Codes: C22B 1/005 Preliminary treatment of scrap C22B1/02 - C22B1/26 take precedence
• CPC Class Codes: C22B 11/046 from manufactured products, e.g. from printed circuit boards, from photographic films, paper or baths
• CPC Class Codes: C22B 3/02 Apparatus therefor
• CPC Class Codes: C22B 3/04 by leaching C22B3/18 takes precedence
• CPC Class Codes: C22B 4/00 Electrothermal treatment of ores or metallurgical products for obtaining metals or alloys obtaining iron or steel C21B, C21C
• CPC Class Codes: C22B 7/006 Wet processes
• CPC Class Codes: C25C 1/00 Electrolytic production, recovery or refining of metals by electrolysis of solutions C25C5/00 takes precedence
• CPC Class Codes: H05K 2203/178 Demolishing, e.g. recycling, reverse engineering, destroying for security purposes; Using biodegradable materials
• CPC Class Codes: H05K 3/22 Secondary treatment of printed circuits H05K3/1283 takes precedence; embedding circuits in grooves by pressure H05K3/107
• CPC Class Codes: Y02P 10/20 Recycling
• CPC Class Codes: Y02P 70/50 Manufacturing or production processes characterised by the final manufactured product
• CPC Class Codes: Y02W 30/82 Recycling of waste of electrical or electronic equipment [WEEE]

Abstract

Apparatuses and processes for recycling printed wire boards, wherein electronic components, precious metals and base metals may be collected for reuse and recycling. The apparatuses generally include a mechanical solder removal module and/or a thermal module, a chemical solder removal module, and a precious metal leaching module, wherein the modules are attached for continuous passage of the e-waste from module to module.

Claims

1. A process for recovering at least one precious metal from printed wire boards (PWB) and/or PWB components, the process comprising,

(a) heating the PWBs in a heating module to soften solder, adhesives, epoxy, and/or glue to remove the PWB components and/or casing from the PWBs;

(b) removing at least a portion of the solder from the PWBs and/or PWB components using a chemical solder removal composition in a chemical solder removal module;

(c) contacting the PWBs and/or PWB components with a leaching composition in a precious metal leaching module to extract at least a portion of the at least one precious metal from the PWBs and/or PWB components into the leaching composition, wherein the at least one precious metal is substantially dissolved or solubilized in the leaching composition;

(d) isolating the leaching composition from the PWBs and/or PWB components;

(e) rinsing the PWBs and/or PWB components in a rinsing module; and

(f) drying the PWBs and/or PWB components in a drying module.

2. The process of claim 1, further comprising recovering the at least one precious metal from the isolated leaching composition.

3. The process of claim 1, wherein the precious metal leaching module, the rinsing module and the drying module are in series.

4. The process of claim 1, wherein the PWBs and/or PWB components moves manually or automatically from the precious metal leaching module to the rinsing module and to the drying module.

5. The process of claim 4, wherein the PWBs and/or PWB components moves manually or automatically on a conveyer belt, conveying roller or conveying wheel.

6. The process of claim 1, further comprising crushing the PWBs and/or PWB components in a crushing module prior to contacting in the precious metal leaching module.

7. The process of claim 1, wherein the isolated leaching composition comprises precious metal ions.

8. The process of claim 2, wherein the recovery of the at least one precious metal from the isolated leaching composition comprises reducing, electrowinning or electrochemically converting the precious metal ions to precious metal.

9. The process of claim 8, further comprising precipitating the at least one precious metal after reduction, electrowinning or electrochemical conversion.

10. The process of claim 1, wherein the isolation comprises filtering and/or centrifuging and/or decanting the leaching composition from the PWBs and/or PWB components.

11. The process of claim 1, wherein the leaching composition substantially leaches at least one precious metal from the PWBs and/or PWB components.

12. The process of claim 1, wherein the leaching composition is purified and recycled.

13. The process of claim 1, wherein the heating module comprises means for moving the PWBs and/or PWB components through a heating mechanism, wherein the means for moving comprise a roller chain, tracks, belts, or link chains.

14. The process of claim 1, wherein the heating module comprises agitation means for removing the PWB components and/or casing from the PWBs once the solder, adhesives, epoxy, and/or glue is softened, wherein the agitation means are selected from the group consisting of brushes, pressurized gases, pressurized liquids, rakes, sonic energy and laser energy.

15. The process of claim 1, wherein the PWB components comprises at least one of a transistor, a capacitor, a heat sink, an integrated circuit, a resistor, an integrated switch, and a processor.

16. The process of claim 1, wherein the leaching composition comprises a salt brine/acid mixture.

17. The process of claim 1, further comprising inserting the PWBs and/or PWB components into a drum prior to removing at least a portion of the solder from the PWBs and/or PWB components.

18. The process of claim 17, wherein the drum is agitated such that the chemical solder removal composition flows past the surface of the PWBs and/or PWB components.

19. The process of claim 1, wherein the rinsing is effectuated by spraying a rinsing composition on the PWBs and/or PWB components, dipping the PWBs and/or PWB components in a volume of the rinsing composition, contacting the PWBs and/or PWB components with a pad or fibrous sorbent applicator element having the rinsing composition absorbed thereon, or contacting the PWBs and/or PWB components with the rinsing composition that is recirculating.

20. The process of claim 19, wherein the rinsing composition comprises water.

21. The process of claim 1, wherein the PWBs and/or PWB components are dried using nitrogen gas, isopropanol, regenerative air, hot air, or spin process technology.

22. The process of claim 1, wherein the chemical solder removal composition selectively removes lead and/or tin-containing solder from the PWBs and/or PWB components relative to precious metals, tantalum-containing metals, and/or base metals that are simultaneously present on said PWBs and/or PWB components.

23. The process of claim 1, wherein the chemical solder removal composition comprises at least one oxidizing agent.

24. The process of claim 1, wherein the chemical solder removal composition comprises nitric acid.

25. The process of claim 1, wherein the heating module comprises a heating mechanism that is maintained at least 1°

C. to about 20°

C. below the melting point of the solder and/or epoxy.

26. The process of claim 1, wherein the at least one precious metal comprises a species selected from the group consisting of gold, silver, platinum, palladium, rhodium, iridium, osmium, rhenium, ruthenium and alloys comprising same.

27. The process of claim 1, wherein the leaching composition comprises at least one oxidizing agent selected from the group consisting of nitric acid, cyclohexylaminosulfonic acid, hydrogen peroxide, potassium peroxymonosulfate, ammonium peroxomonosulfate, ammonium chlorite, ammonium chlorate, ammonium iodate, ammonium perborate, ammonium perchlorate, ammonium periodate, ammonium persulfate, ammonium hypochlorite, sodium persulfate, sodium hypochlorite, potassium iodate, potassium permanganate, potassium persulfate, potassium hypochlorite, tetramethylammonium chlorite, tetramethylammonium chlorate, tetramethylammonium iodate, tetramethylammonium perborate, tetramethylammonium perchlorate, tetramethylammonium periodate, tetramethylammonium persulfate, tetrabutylammonium peroxomonosulfate, peroxomonosulfuric acid, urea hydrogen peroxide, peracetic acid, sodium nitrate, potassium nitrate, ammonium nitrate, sulfuric acid, methanesulfonic acid, ethanesulfonic acid, 2-hydroxyethanesulfonic acid, n-propanesulfonic acid, isopropanesulfonic acid, isobutenesulfonic acid, n-butanesulfonic acid, n-octanesulfonic acid, benzenesulfonic acid, 4-methoxybenzenesulfonic acid, 4-hydroxybenzenesulfonic acid, 4-aminobenzenesulfonic acid, 4-nitrobenzenesulfonic acid, toluenesulfonic acid, hexylbenzenesulfonic acid, heptylbenzenesulfonic acid, octylbenzenesulfonic acid, nonylbenzenesulfonic acid, decylbenzenesulfonic acid, undecylbenzenesulfonic acid, dodecylbenzenesulfonic acid, tridecylbenzenesulfonic acid, tetradecylbenzene sulfonic acid, hexadecylbenzene sulfonic acid, 3-nitrobenzenesulfonic acid, 2-nitrobenzenesulfonic acid, 2-nitronaphthalenesulfonic acid, 3-nitronaphthalenesulfonic acid, 2,3-dinitrobenzenesulfonic acid, 2,4-dinitrobenzenesulfonic acid, 2,5-dinitrobenzenesulfonic acid, 2,6-dinitrobenzenesulfonic acid, 3,5-dinitrobenzenesulfonic acid, 2,4,6-trinitrobenzenesulfonic acid, 3-aminobenzenesulfonic acid, 2-aminobenzenesulfonic acid, 2-aminonaphthalenesulfonic acid, 3-aminonaphthalenesulfonic acid, 2,3-diaminobenzenesulfonic acid, 2,4-diaminobenzenesulfonic acid, 2,5-diaminobenzenesulfonic acid, 2,6-diaminobenzenesulfonic acid, 3,5-diaminobenzenesulfonic acid, 2,4,6-triaminobenzenesulfonic acid, 3-hydroxybenzenesulfonic acid, 2-hydroxybenzenesulfonic acid, 2-hydroxynaphthalenesulfonic acid, 3-hydroxynaphthalenesulfonic acid, 2,3-dihydroxybenzenesulfonic acid, 2,4-dihydroxybenzenesulfonic acid, 2,5-dihydroxybenzenesulfonic acid, 2,6-dihydroxybenzenesulfonic acid, 3,5-dihydroxybenzenesulfonic acid, 2,3,4-trihydroxybenzenesulfonic acid, 2,3,5-trihydroxybenzenesulfonic acid, 2,3,6-trihydroxybenzenesulfonic acid, 2,4,5-trihydroxybenzenesulfonic acid, 2,4,6-trihydroxybenzenesulfonic acid, 3,4,5-trihydroxybenzenesulfonic acid, 2,3,4,5-tetrahydroxybenzenesulfonic acid, 2,3,4,6-tetrahydroxybenzenesulfonic acid, 2,3,5,6-tetrahydroxybenzenesulfonic acid, 2,4,5,6-tetrahydroxybenzenesulfonic acid, 3-methoxybenzenesulfonic acid, 2-methoxybenzenesulfonic acid, 2,3-dimethoxybenzenesulfonic acid, 2,4-dimethoxybenzenesulfonic acid, 2,5-dimethoxybenzenesulfonic acid, 2,6-dimethoxybenzenesulfonic acid, 3,5-dimethoxybenzenesulfonic acid, 2,4,6-trimethoxybenzenesulfonic acid, and combinations thereof.

28. The process of claim 27, wherein the first composition further comprises at least one lead and/or tin complexing agent, at least one organic solvent, and/or at least one passivating agent.

29. The process of claim 28, comprising the at least one complexing agent, wherein the at least one complexing agent comprises a species selected from the group consisting of glycine, serine, proline, leucine, alanine, asparagine, aspartic acid, glutamine, valine, lysine, citric acid, acetic acid, maleic acid, oxalic acid, malonic acid, succinic acid, phosphonic acid, hydroxyethylidene diphosphonic acid (HEDP), 1-hydroxyethane-1,1-diphosphonic acid, nitrilo-tris(methylenephosphonic acid), nitrilotriacetic acid, iminodiacetic acid, etidronic acid, ethylenediamine, ethylenediaminetetraacetic acid (EDTA), (1,2-cyclohexylenedinitrilo)tetraacetic acid (CDTA), uric acid, tetraglyme, pentamethyldiethylenetriamine (PMDETA), 1,3,5-triazine-2,4,6-thithiol trisodium salt solution, 1,3,5-triazine-2,4,6-thithiol triammonium salt solution, sodium diethyldithiocarbamate, disubstituted dithiocarbamates ammonium sulfate, monoethanolamine (MEA), Dequest 2000, Dequest 2010, Dequest 2060s, diethylenetriamine pentaacetic acid, propylenediamine tetraacetic acid, 2-hydroxypyridine 1-oxide, ethylendiamine disuccinic acid (EDDS), N-(2-hydroxyethyl)iminodiacetic acid (HEIDA), sodium triphosphate penta basic, ammonium chloride, sodium chloride, lithium chloride, potassium chloride, ammonium sulfate, hydrochloric acid, sulfuric acid, and combinations thereof.

30. The process of claim 27, wherein the leaching composition is substantially devoid of at least one of fluoride salts, ferric nitrate and other ferric salts, titanium (IV) salts, abrasive material, and fluoroboric acid.