SULFIDE-BASED SOLID COMPOSITE ELECTROLYTE FILM
The present invention relates to a process for manufacturing a free-standing solid composite electrolyte film, comprising the steps of a) mixing (i) at least one sulfide-based solid ionic conducting inorganic particle and (ii) at least one tetrafluoroethylene (TFE) (co)polymer to form a paste and b) calendaring or extruding the paste to produce a film. The invention also relates to a free-standing solid composite electrolyte film comprising (i) at least one sulfide-based solid ionic conducting inorganic particle and (ii) at least one TFE (co)polymer, wherein an amount of the (ii) at least one TFE (co)polymer is from 1.0 to 20.0 wt %, preferably from 2.0 to 15.0 wt % and more preferably from 3.0 to 10.0 wt %, based on the total weight of the film.
1 - 18 . (canceled)
19 . A process for manufacturing a free-standing solid composite electrolyte film, comprising the steps of
a) mixing (i) at least one sulfide-based solid ionic conducting inorganic particle and (ii) at least one tetrafluoroethylene (TFE) (co)polymer to form a paste; and
b) calendaring or extruding the paste to produce a film,
wherein the step a) mixing comprises a1) homogenizing the (i) at least one sulfide-based solid ionic conducting inorganic particle and (ii) at least one TFE (co)polymer into powders and a2) blending the powders into a paste.
20 . The process according to claim 19 , wherein the a1) homogenizing is performed at a temperature of 19° C. or lower and the a2) blending is performed at a temperature of 30° C. or higher.
21 . The process according to claim 19 , wherein the step b) calendaring or extruding is performed at a temperature between 30° C. and 150° C.
22 . The process according to claim 19 , further comprising a step of adding (iii) at least one lubricant in a2) blending to form a paste.
23 . The process according to claim 22 , additionally comprising a step of c) drying the film obtained from the step b) to remove the lubricant.
24 . The process according to claim 19 , further comprising an additional step of d) calendaring.
25 . The process according to claim 19 , wherein an amount of the (ii) at least one TFE (co)polymer is from 1.0 to 20.0 wt %, based on the total weight of the mixture.
26 . The process according to claim 19 , wherein the (ii) at least one TFE (co)polymer is selected from the group consisting of (a) a TFE homopolymer; (b) a TFE copolymer comprising from 0.01 to 25% moles, with respect to the total moles of the recurring units of the TFE copolymer, of recurring units derived from at least one per(halo)fluoroolefin different from TFE; and (c) blends thereof.
27 . The process according to claim 26 , wherein the at least one per(halo)fluoroolefin different from the TFE is hexafluoropropylene.
28 . The process according to claim 19 , wherein the (i) at least one sulfide-based solid ionic conducting inorganic particle comprises crystalline, glass-ceramic and glassed Li 3 PS 4 , Li 7 P 3 S 11 , Li 7 PS 6 , Li 9.6 P 3 S 12 , Li 4 P 2 S 6 and other glasses in the system of Li 2 S—P 2 S 5 , Argyrodite-type Li 6 PS 5 X (X=Cl, Br, or I), (Li 2 S) x -(P 2 S 5 ) y , wherein x+y=1 and 0≤x≤1, Li 10 SnP 2 S 12 , Li 10 GeP 2 S 12 , Li 10 SiP 2 S 12 , Li 0.8 Si 0.8 S 2 , Li 2 S—P 2 S 5 —SiS 2 , Li 2 S—P 2 S 5 —SiS 2 —LiCl, Li 2 S—P 2 S 5 —SnS, Li 2 S—SiS 2 —P 2 S 5 , Li 2 S—SiS 2 —P 2 S 5 —LiI, Li 2 S—SiS 2 —LiI, Li 2 S—SiS 2 , Li 9.54 Si 1.74 P 1.44 S 11.7 Cl 0.3 , doped Li—P—S, doped Li—P—S—X, Li 2 CuPS 4 , Li 1+2x Zn 1-x PS 4 , wherein 0≤x≤1, Li 3.33 Mg 0.33 P 2 S 6 , Li 4-3x Sc x P 2 S 6 , wherein 0≤x≤1, Li 2 S—GeS 2 —ZnS, Li 2 S—SiS 2 —Al 2 S 3 , Li 3 SbS 4 , Ge-substituted Li 3 AsS 4 , Li 3.833 Sn 0.833 As 0.166 S 4 , Li 3 AsS 4 —Li 4 SnS 4 , Na 3 PS 4 , Na 10 SnP 12 S 12 , Na 11 Sn 2 PS 12 , oxysulfides thereof, and blends thereof.
29 . The process according to claim 22 , wherein the (iii) at least one lubricant is selected from the group consisting of isoparaffinic hydrocarbon compounds and petroleum fractions.
30 . The process according to claim 22 , wherein an amount of (iii) at least one lubricant is from 5.0 to 35.0 parts by weight (pbw), with respect to the total weight of the mixture of (i) at least one sulfide-based solid ionic conducting inorganic particle, (ii) at least one TFE (co)polymer and (iii) at least one lubricant.
31 . A free-standing solid composite electrolyte film comprising
(i) at least one sulfide-based solid ionic conducting inorganic particle; and
(ii) at least one TFE (co)polymer,
wherein an amount of the (ii) at least one TFE (co)polymer is from 1.0 to 20.0 wt %, based on the total weight of the film.
32 . The free-standing solid composite electrolyte film according to claim 31 , wherein the (ii) at least one TFE (co)polymer has a three-dimensional (3-D) structure consisting of nodes, fibrils interconnecting the nodes, and the free spaces between the fibrils and the nodes, and the (i) at least one sulfide-based solid ionic conducting inorganic particle is positioned inside the free spaces.
33 . The free-standing solid composite electrolyte film according to claim 31 , wherein the (ii) at least one TFE (co)polymer is selected from the group consisting of (a) a TFE homopolymer; (b) a TFE copolymer comprising from 0.01 to 0.25% moles, with respect to the total moles of the recurring units of the TFE copolymer, recurring units derived from at least one per(halo)fluoroolefin different from TFE; and (c) blends thereof.
34 . The free-standing solid composite electrolyte film according to claim 31 , wherein the thickness of the film is from 10 to 150 μm.
35 . A solid state battery comprising the free-standing solid composite electrolyte film according to claim 31 .
36 . A method for improving ionic conductivity and mechanical properties of a solid state battery, the method comprising using the free-standing solid composite electrolyte film according to claim 31 in a solid state battery.