Electrochemical cells including selectively permeable membrane and semi-solid electrodes, and method of manufacturing the same
Embodiments described herein relate generally to electrochemical cells including a selectively permeable membrane and systems and methods for manufacturing the same. In some embodiments, the selectively permeable membrane can include a solid-state electrolyte material. In some embodiments, electrochemical cells can include a cathode disposed on a cathode current collector, an anode disposed on an anode current collector, and the selectively permeable membrane disposed therebetween. In some embodiments, the cathode and/or anode can include a slurry of an active material and a conductive material in a liquid electrolyte. In some embodiments, a catholyte can be different from an anolyte. In some embodiments, the catholyte can be optimized to improve the redox electrochemistry of the cathode and the anolyte can be optimized to improve the redox electrochemistry of the anode. In some embodiments, the selectively permeable membrane can be configured to isolate the catholyte from the anolyte.
1. A method of forming an electrochemical cell, comprising:
dispensing a semi-solid cathode slurry onto a cathode current collector to form a cathode;
dispensing a first anode material onto an anode current collector to form an anode;
extruding a solid-state electrolyte powder and a polymeric powder binder to form a selectively permeable membrane;
disposing a first surface of the selectively permeable membrane onto the cathode or the anode, the selectively permeable membrane configured to chemically and/or fluidically isolate the cathode including a catholyte from the anode including an anolyte, the selectively permeable membrane not providing electrical isolation between the anode and the cathode;
disposing a conventional separator on a second surface of the selectively permeable membrane, the second surface opposite to the first surface, the conventional separator configured to provide electrical isolation between the anode and the cathode and to allow for ionic charge carriers to be transferred between the cathode and the anode, the selectively permeable membrane including a second active material configured to fill pores of the conventional separator; and
disposing the selectively permeable membrane with the conventional separator between the cathode and the anode to form the electrochemical cell,
wherein the second active material is a second anode active material such that the second active material becomes a second anode of the electrochemical cell, or the second active material is a cathode active material such that the second active material becomes a second cathode of the electrochemical cell.
2. The method of claim 1 , further comprising:
disposing a Li 2 CoO 3 layer between the selectively permeable membrane and the cathode.
3. The method of claim 1 , wherein the selectively permeable membrane includes a diffusion preventing material applied to one or both sides of the selectively permeable membrane.
4. The method of claim 1 , further comprising:
disposing a lithium metal layer between the anode current collector and the first anode material.
5. The method of claim 1 , further comprising:
disposing a metal oxide between the selectively permeable membrane and the first anode material.
6. The method of claim 1 , further comprising:
disposing a first film layer between the cathode and the selectively permeable membrane.
7. The method of claim 1 , wherein the polymeric powder binder includes at least one of polyvinylidene difluoride (PVDF), a fluorinated polymer, polyethylene terephthalate (PET), poly phenylene sulfide (PPS), polyvinyl chloride (PVC), styrene butadiene rubber (SBR), polyethylene oxide (PEO), cellulose, or polyacrylate.
8. The method of claim 1 , further comprising:
disposing a layer including self-terminated oligomers with hyperbranched architecture between the selectively permeable membrane and at least one of the first anode material or the cathode.
9. The method of claim 1 , wherein the solid-state electrolyte powder includes at least one of a garnet structure, a perovskite structure, a phosphate-based Lithium Super Ionic Conductor (LISICON) structure, La 0.51 Li 0.34 TiO 2.94 , Li 1.3 Al 0.3 Ti 1.7 (PO 4 ) 3 , Li 7 La 3 Zr 2 O 12 , Li 6.66 La 3 Zr 1.6 Ta 0.4 O 12.9 (LLZO), 50Li 4 SiO 4 ·50Li 3 BO 3 , Li 2.9 PO 3.3 N 0.46 (lithium phosphorousoxynitride, LiPON), Li 3.6 S 10.6 P 0.4 O 4 , Li 3 BN 2 , Li 3 BO 3 —Li 2 SO 4 , Li 3 BO 3 —Li 2 SO 4 —Li 2 CO 3 (LIBSCO, pseudoternary system), sulfide contained solid electrolyte materials, a thio-LISICON structure, a glassy structure, a glass-ceramic structure, Li 1.07 Al 0.69 Ti 1.46 (PO 4 ) 3 , Li 1.5 Al 0.5 Ge 1.5 (PO 4 ) 3 , Li 10 GeP 2 Si 2 (LGPS), 30Li 2 S·26B 2 S 3 ·44LiI, 63Li 2 S·36SiS 2 ·1Li 3 PO 4 , 57Li 2 S·38SiS 2 ·5Li 4 SiO 4 , 70Li 2 S·30P 2 S 5 , 50Li 2 S·50GeS 2 , Li 7 P 3 S 11 , Li 3.25 P 0.95 S 4 , Li 9.54 Si 1.74 P 1.44 S 11.7 Cl 0.3 , a closo-type complex hydride solid electrolyte, LiBH 4 —LiI, LiBH 4 —LiNH 2 , LiBH 4 —P 2 S 5 , Li(CB 9 H 10 )—LiI, a lithium electrolyte salt, bis(trifluoromethane)sulfonamide (TFSI), bis(pentalluoroethanesulfonyl)imide (BETI), bis(fluorosulfonyl)imide, lithium borate oxalato phosphine oxide (LiBOP), lithium bis(fluorosulfonyl)imide, amide-borohydride, LiBF 4 , or LiPF 6 .
10. A method of forming an electrochemical cell, comprising:
dispensing a semi-solid cathode slurry onto a cathode current collector to form a cathode;
dispensing a first anode material onto an anode current collector to form an anode;
processing at least one of a solid-state electrolyte material or a first active material with a binder to form a selectively permeable membrane, the processing including at least one of extruding or blowing;
disposing a first surface of the selectively permeable membrane onto the cathode or the anode, the selectively permeable membrane configured to chemically and/or fluidically isolate the cathode including a catholyte from the anode including an anolyte, the selectively permeable membrane not providing electrical isolation between the anode and the cathode;
disposing a conventional separator on a second surface of the selectively permeable membrane, the second surface opposite to the first surface, the conventional separator configured to provide electrical isolation between the anode and the cathode and to allow for ionic charge carriers to be transferred between the cathode and the anode, the selectively permeable membrane including a second active material configured to fill pores of the conventional separator; and
disposing the selectively permeable membrane with the conventional separator between the cathode and the anode to form the electrochemical cell,
wherein the second active material is a second anode active material such that the second active material becomes a second anode of the electrochemical cell, or the second active material is a cathode active material such that the second active material becomes a second cathode of the electrochemical cell.
11. The method of claim 10 , wherein the selectively permeable membrane includes a diffusion preventing material applied to one or both sides of the selectively permeable membrane.
12. The method of claim 10 , further comprising:
disposing a lithium metal layer between the anode current collector and the first anode material.
13. The method of claim 10 , further comprising:
disposing a first film layer between the cathode and the selectively permeable membrane.
14. The method of claim 10 , further comprising:
disposing a layer including self-terminated oligomers with hyperbranched architecture between the selectively permeable membrane and at least one of the first anode material or the cathode.
15. The method of claim 10 , wherein the solid-state electrolyte material is selected from at least one of a garnet structure, a perovskite structure, a phosphate-based Lithium Super Ionic Conductor (LISICON) structure, La 0.51 Li 0.34 TiO 2.94 , Li 1.3 Al 0.3 Ti 1.7 (PO 4 ) 3 , Li 7 La 3 Zr 2 O 12 , Li 6.66 La 3 Zr 1.6 Ta 0.4 O 12.9 (LLZO), 50Li 4 SiO 4 ·50Li 3 BO 3 , Li 2.9 PO 3.3 N 0.46 (lithium phosphorousoxynitride, LiPON), Li 3.6 S 10.6 P 0.4 O 4 , Li 3 BN 2 , Li 3 BO 3 —Li 2 SO 4 , Li 3 BO 3 —Li 2 SO 4 —Li 2 CO 3 (LIBSCO, pseudoternary system), sulfide contained solid electrolyte materials, a thio-LISICON structure, a glassy structure, a glass-ceramic structure, Li 1.07 Al 0.69 Ti 1.46 (PO 4 ) 3 , Li 1.5 Al 0.5 Ge 1.5 (PO 4 ) 3 , Li 10 GeP 2 Si 2 (LGPS), 30Li 2 S·26B 2 S 3 ·44LiI, 63Li 2 S·36SiS 2 ·1Li 3 PO 4 , 57Li 2 S·38SiS 2 ·5Li 4 SiO 4 , 70Li 2 S·30P 2 S 5 , 50Li 2 S·50GeS 2 , Li 7 P 3 S 11 , Li 3.25 P 0.95 S 4 , Li 9.54 S 11.74 P 1.44 S 11.7 Cl 0.3 , a closo-type complex hydride solid electrolyte, LiBH 4 —LiI, LiBH 4 —LiNH 2 , LiBH 4 —P 2 S 5 , Li(CB 9 H 10 )—LiI, a lithium electrolyte salt, bis(trifluoromethane)sulfonamide (TFSI), bis(pentalluoroethanesulfonyl)imide (BETI), bis(fluorosulfonyl)imide, lithium borate oxalato phosphine oxide (LiBOP), lithium bis(fluorosulfonyl)imide, amide-borohydride, LiBF 4 , or LiPF 6 .
16. The method of claim 10 , further comprising:
disposing a Li 2 CoO 3 layer between the selectively permeable membrane and the cathode.
17. The method of claim 16 , further comprising:
disposing a metal oxide between the selectively permeable membrane and the first anode material.
18. The method of claim 10 , further comprising:
disposing the electrochemical cell into a pouch; and
sealing the pouch to form the electrochemical cell.
19. The method of claim 18 , wherein the selectively permeable membrane extends substantially beyond the anode and the cathode and is sealed between a first portion of the pouch and a second portion of the pouch.
20. A method of forming an electrochemical cell, comprising:
dispensing a semi-solid cathode slurry onto a cathode current collector to form a cathode;
dispensing a first anode material onto an anode current collector to form an anode;
coating a solid-state electrolyte powder with a polymeric binder to form a selectively permeable membrane, the coating via at least one of extrusion with a hot/cold press process or extrusion process without a hot/cold press process;
disposing a first surface of the selectively permeable membrane onto the cathode or the anode, the selectively permeable membrane configured to chemically and/or fluidically isolate the cathode including a catholyte from the anode including an anolyte, the selectively permeable membrane not providing electrical isolation between the anode and the cathode;
disposing a conventional separator on a second surface of the selectively permeable membrane, the second surface opposite to the first surface, the conventional separator configured to provide electrical isolation between the anode and the cathode and to allow for ionic charge carriers to be transferred between the cathode and the anode, the selectively permeable membrane including a second active material configured to fill pores of the conventional separator; and
disposing the selectively permeable membrane with the conventional separator between the cathode and the anode to form the electrochemical cell,
wherein the second active material is a second anode active material such that the second active material becomes a second anode of the electrochemical cell, or the second active material is a cathode active material such that the second active material becomes a second cathode of the electrochemical cell.
21. The method of claim 20 , further comprising:
disposing a Li 2 CoO 3 layer between the selectively permeable membrane and the cathode.
22. The method of claim 20 , wherein the selectively permeable membrane includes a diffusion preventing material applied to one or both sides of the selectively permeable membrane.
23. The method of claim 20 , further comprising:
disposing a lithium metal layer between the anode current collector and the first anode material.
24. The method of claim 20 , further comprising:
disposing a metal oxide between the selectively permeable membrane and the first anode material.
25. The method of claim 20 , further comprising:
disposing a first film layer between the cathode and the selectively permeable membrane.
26. The method of claim 20 , wherein the polymeric binder includes at least one of polyvinylidene difluoride (PVDF), a fluorinated polymer, polyethylene terephthalate (PET), poly phenylene sulfide (PPS), polyvinyl chloride (PVC), styrene butadiene rubber (SBR), polyethylene oxide (PEO), cellulose, or polyacrylate.
27. The method of claim 20 , further comprising:
disposing a layer including self-terminated oligomers with hyperbranched architecture between the selectively permeable membrane and at least one of the first anode material or the cathode.
28. The method of claim 20 , wherein the solid-state electrolyte powder includes at least one of a garnet structure, a perovskite structure, a phosphate-based Lithium Super Ionic Conductor (LISICON) structure, La 0.51 Li 0.34 TiO 2.94 , Li 1.3 Al 0.3 Ti 1.7 (PO 4 ) 3 , Li 7 La 3 Zr 2 O 12 , Li 6.66 La 3 Zr 1.6 Ta 0.4 O 12.9 (LLZO), 50Li 4 SiO 4 ·50Li 3 BO 3 , Li 2.9 PO 3.3 N 0.46 (lithium phosphorousoxynitride, LiPON), Li 3.6 S 10.6 P 0.4 O 4 , Li 3 BN 2 , Li 3 BO 3 —Li 2 SO 4 , Li 3 BO 3 —Li 2 SO 4 —Li 2 CO 3 (LIBSCO, pseudoternary system), sulfide contained solid electrolyte materials, a thio-LISICON structure, a glassy structure, a glass-ceramic structure, Li 1.07 Al 0.69 Ti 1.46 (PO 4 ) 3 , Li 1.5 Al 0.5 Ge 1.5 (PO 4 ) 3 , Li 10 GeP 2 Si 2 (LGPS), 30Li 2 S·26B 2 S 3 ·44LiI, 63Li 2 S·36SiS 2 ·1Li 3 PO 4 , 57Li 2 S·38SiS 2 ·5Li 4 SiO 4 , 70Li 2 S·30P 2 S 5 , 50Li 2 S·50GeS 2 , Li 7 P 3 S 11 , Li 3.25 P 0.95 S 4 , Li 9.54 Si 1.74 P 1.44 S 11.7 Cl 0.3 , a closo-type complex hydride solid electrolyte, LiBH 4 —LiI, LiBH 4 —LiNH 2 , LiBH 4 —P 2 S 5 , Li(CB 9 H 10 )—LiI, a lithium electrolyte salt, bis(trifluoromethane)sulfonamide (TFSI), bis(pentalluoroethanesulfonyl)imide (BETI), bis(fluorosulfonyl)imide, lithium borate oxalato phosphine oxide (LiBOP), lithium bis(fluorosulfonyl)imide, amide-borohydride, LiBF 4 , or LiPF 6 .