The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Jun. 15, 2021

Filed:

Jul. 29, 2019
Applicant:

Battelle Energy Alliance, Llc, Idaho Falls, ID (US);

Inventors:

Tedd E. Lister, Lewisville, ID (US);

Jacob A. Parkman, Fuquay-Varina, NC (US);

Luis A. Diaz Aldana, Idaho Falls, ID (US);

Gemma Clark, Idaho Falls, ID (US);

Eric J. Dufek, Ammon, ID (US);

Philip Keller, Knoxville, TN (US);

Assignee:

Battelle Energy Alliance, LLC, Idaho Falls, ID (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C22B 3/00 (2006.01); C22B 3/08 (2006.01); C22B 3/10 (2006.01); C22B 3/44 (2006.01); C25C 1/06 (2006.01); C25C 1/08 (2006.01); C25C 1/12 (2006.01); C25C 1/14 (2006.01); C25C 1/16 (2006.01); C25C 1/18 (2006.01); C25C 1/20 (2006.01); C25C 1/22 (2006.01); C25C 7/02 (2006.01); C25C 7/06 (2006.01); C22B 11/00 (2006.01);
U.S. Cl.
CPC ...
C22B 11/046 (2013.01); C22B 3/08 (2013.01); C22B 3/10 (2013.01); C22B 3/44 (2013.01); C25C 1/06 (2013.01); C25C 1/08 (2013.01); C25C 1/12 (2013.01); C25C 1/14 (2013.01); C25C 1/16 (2013.01); C25C 1/18 (2013.01); C25C 1/20 (2013.01); C25C 1/22 (2013.01); C25C 7/02 (2013.01); C25C 7/06 (2013.01); Y02P 10/20 (2015.11);
Abstract

A method of recovering metals from electronic waste comprises providing a powder comprising electronic waste in at least a first reactor and a second reactor and providing an electrolyte comprising at least ferric ions in an electrochemical cell in fluid communication with the first reactor and the second reactor. The method further includes contacting the powders within the first reactor and the second reactor with the electrolyte to dissolve at least one base metal from each reactor into the electrolyte and reduce at least some of the ferric ions to ferrous ions. The ferrous ions are oxidized at an anode of the electrochemical cell to regenerate the ferric ions. The powder within the second reactor comprises a higher weight percent of the at least one base metal than the powder in the first reactor. Additional methods of recovering metals from electronic waste are also described, as well as an apparatus of recovering metals from electronic waste.


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