Recovery of tritium from molten lithium blanket
US-10450660-B2 · Oct 22, 2019 · US
US2018312986A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018312986-A1 |
| Application number | US-201715498909-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 27, 2017 |
| Priority date | Apr 27, 2017 |
| Publication date | Nov 1, 2018 |
| Grant date | — |
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An electrochemical cell includes a positive electrode, a negative electrode, an electrolyte disposed between the positive electrode and the negative electrode, and an ion-conducting composite membrane disposed between the positive electrode and the negative electrode. The composite membrane includes a porous substrate having pores and a porosity from about 5 vol % to about 80 vol %, and a selective ion-conductive filler disposed at least partially within the pores. The filler includes an intercalation material. Methods of making the ion-conducting composite membrane and using an electrochemical cell having the ion-conducting composite membrane are also provided.
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What is claimed is: 1 . An electrochemical cell comprising: a positive electrode; a negative electrode; an electrolyte disposed between the positive electrode and the negative electrode; and an ion-conducting composite membrane disposed between the positive electrode and the negative electrode, the composite membrane comprising: a porous substrate having pores and a porosity from about 5 vol % to about 80 vol %; and a selective ion-conductive filler disposed at least partially within the pores, the filler including an intercalation material. 2 . The electrochemical cell of claim 1 , wherein the porous substrate comprises a material selected from the group consisting of graphite, glassy carbon, nickel, tungsten, stainless steel, magnesium oxide, boron nitride, and combinations thereof. 3 . The electrochemical cell of claim 1 , wherein the intercalation material is selected from the group consisting of transition metal oxides, metal dichalcogenides, olivines, tavorites, spinels, layered materials, and combinations thereof. 4 . The electrochemical cell of claim 3 , wherein the intercalation material is selected from the group consisting of LiTiO 2 , LiMnO 2 , LiFeO 2 , LiCoO 2 , LiNiO 2 , TiS 2 , VS 2 , TiSe 2 , NbSe 2 , LiTiS 2 , LiVS 2 , LiTiSe 2 , LiNbSe 2 , LiFePO 4 , LiMnPO 4 , Li(Mn x Fe 1-x )PO 4 , Li(Mn x Co 1-x )PO4, Li(Mn x Co y Ni z )PO 4 , Li 2 FeSiO 4 , LiFeSO 4 F, LiVPO 4 F, LiMn 2 O 4 , LiNi 0.5 Mn 0.5 O 4 . Li 4 Ti 5 O 12 LiNi 0.33 Mn 0.33 Co 0.33 O 2 , LiNi 0.5 Mn 0.5 O 2 , Na x CoO 2 , Na x MnO 2 , Na x FeO 2 , Na x CrO 2 , Na[Ni 0.33 Fe 0.33 Mn 0.33 ]O 2 , NaFePO 4 , NaFe 0.5 Mn 0.5 PO 4 , NaVPO 4 F, Na 3 V 2 (PO 4 ) 2 F 3 , Na 1.5 VOPO 4 F 0.5 , and combinations thereof. 5 . The electrochemical cell of claim 1 , wherein the selective ion-conductive filler conducts an ion of an element selected from the group consisting of hydrogen, Li, Na, K, Ca, Mg, Fe, Fe, Sn, Co, Cu, Ag, Au, and combinations thereof. 6 . The electrochemical cell of claim 1 , wherein the porous substrate has an average pore diameter of about 100 nm to about 100 μm. 7 . The electrochemical cell of claim 1 , where the electrochemical cell is an energy storage device, an electrolytic cell, and/or a fuel cell. 8 . The electrochemical cell of claim 7 , wherein the electrochemical cell is a molten salt battery. 9 . The electrochemical cell of claim 8 , wherein the molten salt battery is selected from the group consisting of a sodium-sulfur battery, a sodium-nickel chloride battery, and combinations thereof. 10 . A method of operating an electrochemical cell, the method comprising: providing the electrochemical cell comprising: a positive electrode; a negative electrode; an electrolyte disposed between the positive electrode and the negative electrode; and an ion-conducting composite membrane disposed between the positive electrode and the negative electrode, the composite membrane comprising: a porous substrate having pores and a porosity from about 5 vol % to about 80 vol %; and a selective ion-conductive filler disposed at least partially within the pores, the filler including an intercalation material; establishing an electrically conductive connection between an external circuit and the positive electrode and the negative electrode; and operating the external circuit so as to convert electrical energy into chemical energy in the cell or to convert chemical energy from the cell into electrical energy by driving transfer of ions through the composite membrane. 11 . The method of claim 10 , wherein the electrochemical cell is an energy storage device, an electrolytic cell, and/or a fuel cell. 12 . The method of claim 10 , wherein the electrochemical cell is an electrolytic cell and the ions are metal ions. 13 . The method of claim 12 , wherein the metal ions are ions of a metal selected from the group consisting of Li, Na, K, Ca, Mg, Fe, Fe, Sn, Co, Cu, Ag, Au, and combinations thereof. 14 . The method of claim 10 , wherein the intercalation material is selected from the group consisting of transition metal oxides, metal dichalcogenides, olivines, tavorites, spinels, layered materials, and combinations thereof. 15 . The method of claim 10 , wherein the intercalation material is selected from the group consisting of LiTiO 2 , LiMnO 2 , LiFeO 2 , LiCoO 2 , LiNiO 2 , TiS 2 , VS 2 , TiSe 2 , NbSe 2 , LiTiS 2 , LiVS 2 , LiTiSe 2 , LiNbSe 2 , LiFePO 4 , LiMnPO 4 , Li(Mn x Fe 1-x )PO 4 , Li(Mn x Co 1-x )PO4, Li(Mn x Co y Ni z )PO 4 , Li 2 FeSiO 4 , LiFeSO 4 F, LiVPO 4 F, LiMn 2 O 4 , LiNi 0.5 Mn 0.5 O 4 . Li 4 Ti 5 O 12 LiNi 0.33 Mn 0.33 Co 0.33 O 2 , LiNi 0.5 Mn 0.5 O 2 , Na x CoO 2 , Na x MnO 2 , Na x FeO 2 , Na x CrO 2 , Na[Ni 0.33 Fe 0.33 Mn 0.33 ]O 2 , NaFePO 4 , NaFe 0.5 Mn 0.5 PO 4 , NaVPO 4 F, Na 3 V 2 (PO 4 ) 2 F 3 , Na 1.5 VOPO 4 F 0.5 , and combinations thereof. 16 . A method for manufacturing an ion-conducting composite membrane for use within an electrochemical cell, the method comprising: providing a porous substrate having pores and a porosity from about 5 vol % to about 80 vol %; contacting the porous substrate with a selective ion-conductive filler precursor; and processing the precursor to form a selective ion-conductive filler disposed at least partially within the pores, the filler including an intercalation material. 17 . The method of claim 16 , wherein the precursor is in a sol-gel solution and the processing includes gelling and curing the sol-gel solution. 18 . The method of claim 17 , wherein the sol-gel solution further comprises a viscosity adjuster. 19 . The method of claim 16 , wherein the processing further includes thermally curing the precursor. 20 . The method of claim 16 , wherein the precursor is in a vapor and the processing is chemical vapor deposition, sputter deposition, pulsed laser deposition, and/or electron beam deposition.
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