Electrochemical cell for recovery of metals from solid metal oxides
US-2016032473-A1 · Feb 4, 2016 · US
US2023131891A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023131891-A1 |
| Application number | US-202117509394-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 25, 2021 |
| Priority date | Oct 25, 2021 |
| Publication date | Apr 27, 2023 |
| Grant date | — |
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A method for extracting metal and oxygen from powdered metal oxides in electrolytic cell is proposed, the electrolytic cell comprising a container, a cathode, an anode and an oxygen-ion-conducting membrane, the method comprising providing a solid oxygen ion conducting electrolyte powder into a container, providing a feedstock comprising at least one metal oxide in powdered form into the container, applying an electric potential across the cathode and the anode, the cathode being in communication with the electrolyte powder and the anode being in communication with the membrane in communication with the electrolyte powder, such that at least one respective metallic species of the at least one metal oxide is reduced at the cathode and oxygen is oxidized at the anode to form molecular oxygen, wherein the potential across the cathode and the anode is greater than the dissociation potential of the at least one metal oxide and less than the dissociation potential of the solid electrolyte powder and the membrane.
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1 . A method for extracting metal and oxygen from powdered metal oxides in an electrolytic cell, comprising a container, a cathode, an anode and an oxygen-ion-conducting membrane, the method comprising: providing a solid oxygen ion conducting electrolyte powder into a container, providing a feedstock comprising at least one metal oxide in powdered form into the container, applying an electric potential across the cathode and the anode, the cathode being in communication with the electrolyte powder and the anode being in communication with the membrane in communication with the electrolyte powder, such that at least one respective metallic species of the at least one metal oxide is reduced at the cathode and oxygen is oxidized at the anode to form molecular oxygen, wherein the potential across the cathode and the anode is greater than the dissociation potential of the at least one metal oxide and less than the dissociation potential of the solid electrolyte powder and the membrane. 2 . The method of claim 1 , further comprising mixing the electrolyte powder and the feedstock. 3 . The method of claim 1 , wherein the feedstock comprises at least one of a group of materials or a chemical compound comprising at least one of the group of materials, the group consisting of: iron, titanium, regolith. 4 . The method of claim 1 , wherein the electrolyte powder comprises at least one of a group of materials, the group consisting of rare earth or alkaline earth-doped zirconia-, ceria-, hafnia-, and thoria-based oxides. 5 . The method of claim 1 , wherein the electrolyte powder comprises mixed oxygen ion electronic conductors. 6 . The method of claim 1 , wherein the oxygen ion-conducting membrane is selected from a group of materials, the group comprising rare earth or alkaline earth-doped zirconia-, ceria-, hafnia-, and thoria-based oxides. 7 . The method of claim 6 , wherein the membrane comprises yttria-stabilized zirconia. 8 . The method of claim 1 , wherein a mean particle size of the solid electrolyte powder is less than a mean particle size of the feedstock powder. 9 . The method of claim 1 , wherein the electrolytic cell is operated at a temperature greater than about 500° C. 10 . The method of claim 1 , wherein the electrolytic cell is operated at a temperature in the range of about 500° C. to about 1300° C. 11 . The method of claim 1 , further comprising collecting molecular oxygen at the anode. 12 . The method of claim 1 , further comprising arranging a conducting structure into a space between the cathode and the anode in electrical contact with the cathode as a preparatory step before applying the electric potential. 13 . The method of claim 1 , further comprising separating obtained metal from the electrolyte powder through a separation process, the separation process being selected from a group of separation processes, the group comprising: sieving, vibration separation, magnetic separation, electrostatic separation, air classification, sedimenting, and a combination thereof. 14 . System for extracting metal and oxygen from powdered metal oxides, the system comprising: an electrolytic cell having a container, a cathode, an anode, and an oxygen-ion-conducting membrane, a solid oxygen ion conducting electrolyte powder, and a power supply, wherein the cathode and the anode are arranged at a distance to each other on the container to form a receiving space, wherein the membrane is arranged between the cathode and the anode and contacts the anode, wherein the electrolytic powder is provided in the receiving space in communication with the cathode and the membrane, wherein the power supply is connectable to the cathode and the anode to selectively apply an electric potential across the cathode and the anode, wherein the system is adapted for reducing at least one respective metallic species of at least one metal oxide of feedstock mixed into and surrounded by the electrolyte powder by applying the electric potential, wherein the potential is greater than the dissociation potential of the at least one metal oxide and less than the dissociation potential of the solid electrolyte powder and the membrane. 15 . The system of claim 14 , wherein the electrolyte powder comprises at least one of a group of materials, the group consisting of rare earth or alkaline earth-doped zirconia-, ceria-, hafnia-, and thoria-based oxides. 16 . The system of claim 14 , wherein the solid electrolyte powder comprises mixed oxygen ion electronic conductors. 17 . The system of claim 14 , wherein the oxygen ion-conducting membrane is selected from a group of materials, the group comprising rare earth or alkaline earth-doped zirconia-, ceria-, hafnia-, and thoria-based oxides, in particular yttria-stabilized zirconia. 18 . The system of claim 14 , further comprising a conducting structure, in particular pins and/or a wire mesh, in the receiving space between the cathode and the anode in electrical contact with the cathode. 19 . The system of claim 14 , further comprising an array of anodes, in particular capillary anodes, extending in direction of the cathode. 20 . The system of claim 18 and 19 , wherein the conducting structure comprises at least one wire mesh, wherein the capillary anodes are at least partially surrounded by mesh cells.
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