Methods and apparatus for extracting metals from materials
The present disclosure relates to an apparatus and method for selectively recovering target metals or minerals from a metal or mineral containing mixture/solution.
1 . An electrochemical reactor for extracting a target metal or mineral from a metal or mineral containing solution, the electrochemical reactor comprising:
a flow cell, the flow cell comprising a plurality of silicon electrodes comprising two or more anodes and two or more cathodes; and
a voltage source configured to apply a voltage between the one two or more anodes and the two or more cathodes,
wherein the two or more cathodes and anodes form an array of alternating anodes and cathodes,
wherein the metal or mineral containing solution is acidic,
wherein the flow cell is configured to extract the target metal or mineral from the metal or mineral containing solution, and
wherein the plurality of silicon electrodes are coated with a coating material comprising Pt/N, Pt/Pb/Sb, Pt/Pb/Sb/Ca, Pt/Ir, Pt/Ru, Pt/Bi, Pt/Hf, or Pt/W.
2 . The electrochemical reactor of claim 1 , wherein the flow cell is a closed loop or partially closed loop configuration.
3 . The electrochemical reactor of claim 1 , wherein the metal or mineral containing solution passes between or through the plurality of silicon electrodes.
4 . The electrochemical reactor of claim 3 , wherein flow of the metal or mineral containing solution is orthogonal to the applied voltage.
5 . The electrochemical reactor of claim 1 , wherein the metal or mineral containing solution is from a lithium-ion battery recycling stream, a mining production stream, a mining waste stream, a refining stream, or a mining-affected water source.
6 . The electrochemical reactor of claim 1 , wherein the target metal or mineral is selected from the group consisting of lithium, manganese, cobalt, nickel, copper, lead, zinc, silver, cadmium, gold, silver, lanthanum, cerium, praseodymium, neodymium, promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, scandium, yttrium, platinum, palladium, iridium, ruthenium, rhodium, osmium, rhenium, mercury, thallium, selenium, bismuth, lead, uranium, polonium, combinations thereof, and oxides or hydroxides thereof.
7 . The electrochemical reactor of claim 1 , wherein the plurality of silicon electrodes are reusable.
8 . The electrochemical reactor of claim 1 , wherein the coating has a thickness of 0.5 nm to 500 nm.
9 . The electrochemical reactor of claim 1 , wherein the coating material is deposited by physical vapor deposition, magnetron sputtering, electron beam evaporation, thermal evaporation, pulsed laser deposition, electroplating, ion implantation, thermal spray deposition, or chemical vapor deposition, and further refined by thermal annealing.
10 . The electrochemical reactor of claim 1 , wherein a surface of at least one of the plurality of silicon electrodes is prepared prior to coating with ion-beam etching or with immersion in hydrofluoric acid at 0.1 wt % to 50 wt % HF in water.
11 . The electrochemical reactor of claim 1 , wherein the electrode material is non-porous.
12 . The electrochemical reactor of claim 1 , wherein the electrode material is porous.
13 . The electrochemical reactor of claim 1 , wherein a surface of the electrode material is roughened via mechanical, chemical, thermal, or ion plasma-based methods such as sanding, sand blasting, or ion etching.
14 . The electrochemical reactor of claim 1 , wherein the plurality of electrodes are in series or parallel flow configurations, wherein the metal or mineral containing solution flows through porous the plurality of silicon electrodes when the plurality of silicon electrodes are porous or around the plurality of silicon electrodes when the plurality of silicon electrodes are non-porous.
15 . The electrochemical reactor of claim 1 , wherein distance between the plurality of silicon electrodes ranges from 1 mm to 100 cm.
16 . The electrochemical reactor of claim 1 , wherein the plurality of silicon electrodes have a thickness ranging from 200 μm to 1 cm.
17 . The electrochemical reactor of claim 1 , wherein the coating material comprises Pt/Ir.
18 . The electrochemical reactor of claim 1 , wherein the metal or mineral containing solution has a pH less than 3.
19 . The electrochemical reactor of claim 1 , wherein the metal or mineral containing solution comprises sulfuric acid, hydrochloric acid, nitric acid, or combinations thereof.
20 . The electrochemical reactor of claim 19 , wherein the metal or mineral containing solution comprises sulfuric acid.
21 . The electrochemical reactor of claim 1 , wherein the plurality of silicon electrodes comprise monolithic silicon.
22 . The electrochemical reactor of claim 1 , wherein the coating has a thickness of about 0.5 nm to about 500 nm.
23 . An electrochemical reactor for extracting a target metal or mineral from a metal or mineral containing solution, the electrochemical reactor comprising:
a flow cell, the flow cell comprising a plurality of silicon electrodes comprising two or more anodes and two or more cathodes; and
a voltage source configured to apply a voltage between the two or more anodes and the two or more cathodes,
wherein the two or more cathodes and anodes form an array of alternating anodes and cathodes,
wherein the metal or mineral containing solution is acidic,
wherein the flow cell is configured to extract the target metal or mineral from the metal or mineral containing solution, and
wherein the plurality of silicon electrodes are coated with a coating material comprising Au/Ni, Au/Pb/Sb, Au/Pb/Sb/Ca, Au/Ir, Au/Ru, Au/W, Au/Hf, or Au/Bi.
24 . The electrochemical reactor of claim 23 , wherein the plurality of silicon electrodes comprise monolithic silicon.
25 . The electrochemical reactor of claim 23 , wherein the coating has a thickness of about 0.5 nm to about 500 nm.
26 . An electrochemical reactor for extracting a target metal or mineral from a metal or mineral containing solution, the electrochemical reactor comprising:
a flow cell, the flow cell comprising a plurality of silicon electrodes comprising two or more anodes and two or more cathodes; and
a voltage source configured to apply a voltage between the two or more anodes and the two or more cathodes,
wherein the two or more cathodes and anodes form an array of alternating anodes and cathodes,
wherein the metal or mineral containing solution is acidic,
wherein the flow cell is configured to extract the target metal or mineral from the metal or mineral containing solution, and
wherein the plurality of silicon electrodes are coated with a coating material comprising C/Ni, Cu/Pb/Sb, C/Pb/Sb/Ca, C/Ir, C/Ru, C/W, or C/Bi.
27 . The electrochemical reactor of claim 26 , wherein the plurality of silicon electrodes comprise monolithic silicon.
28 . The electrochemical reactor of claim 26 , wherein the coating has a thickness of about 0.5 nm to about 500 nm.
29 . An electrochemical reactor for extracting a target metal or mineral from a metal or mineral containing solution, the electrochemical reactor comprising:
a flow cell, the flow cell comprising a plurality of silicon electrodes comprising two or more anodes and two or more cathodes; and
a voltage source configured to apply a voltage between the two or more anodes and the two or more cathodes,
wherein the two or more cathodes and anodes form an array of alternating anodes and cathodes,
wherein the metal or mineral containing solution is acidic,
wherein the flow cell is configured to extract the target metal or mineral from the metal or mineral containing solution, and
wherein the plurality of silicon electrodes are coated with a coating material comprising Hf/Pb, Hf/Sb, Hf/Ca, Hf/Ru, Hf/Rh, Ti/Hf, Ni/Hf, Co/Hf, Cu/Hf, Ag/Hf, Pt/Hf, Pd/Hf, or Ir/Hf.
30 . The electrochemical reactor of claim 29 , wherein the plurality of silicon electrodes comprise monolithic silicon.
31 . The electrochemical reactor of claim 29 , wherein the coating has a thickness of about 0.5 nm to about 500 nm.