Large-scale synthesis of powders of solid-state electrolyte material particles for solid-state batteries, systems and methods thereof
Various solid-state electrolyte materials having a desired chemical composition as well as method and apparatus of producing the solid-state electrolyte (SSE) materials are provided. The method includes drying a gas-liquid mixture to form a gas-solid mixture, obtaining powdered particles, and annealing the powdered particles to obtain crystalline products of the SSE material. The liquid mixture is prepared using stoichiometrically amounts of lithium-containing salt and one or more inorganic salts and then mixed with a gas. The salts are prepared in solutions and the molar ratio of the solutions of lithium-containing salt and the one or more inorganic metal salt are digitally controlled, thereby obtaining large scale synthesis of the SSE materials. The processing apparatus generally includes a mist generator, a power jetting chamber, one or more gas-solid separators, and one or more reactors. Various types of SSE materials can then be prepared and obtained.
1 . A method of producing a solid-state electrolyte (SSE) material, comprising,
flowing a first flow of a first gas to be mixed with a liquid mixture of digitally-controlled stoichiometrically amounts of a lithium-containing salt, one or more inorganic salts containing one or more metals D 1 , D 2 , . . . , D N ;
forming a gas-liquid mixture and jetting a mist of the liquid mixture into a power jetting chamber;
delivering a second gas flow of a heated gas into the power jetting chamber;
drying the gas-liquid mixture for a first reaction time period of less than 20 min to undergo one or more oxidation reactions in the presence of the second gas flow and form a gas-solid mixture;
deliver the gas-solid mixture out of the power jetting chamber;
separate the gas-solid mixture into one or more solid particles of the SSE material;
deliver the one or more solid particles into an annealing chamber; and
annealing the one or more solid particles of the SSE material for a second reaction time period of more than 2 hours to undergo a dynamic crystallization process in the presence of a third gas flow and obtain crystalline products, wherein the crystalline products of the SSE material are in spherical clusters under scanning electronic microscopy (SEM) analysis.
2 . The method of claim 1 , further comprising:
milling the crystalline products of the SSE material to obtain nano-sized particles.
3 . The method of claim 1 , wherein the one or more solid particles are annealed in the dynamic crystallization process in the presence of an oxygen gas flow.
4 . The method of claim 1 , wherein the first reaction time is less than 3 minutes.
5 . The method of claim 1 , wherein the ionic conductivity (c) of the crystalline products of the SSE material is larger than 10 −4 S per centimeter at 25° C.
6 . The method of claim 1 , wherein the tap density of the SSE material is more than 1.0 g/ml.
7 . The method of claim 1 , wherein the tap density of the SSE material is more than 1.4 g/ml after annealing the SSE material at more than 900° C. for more than 8 hours.
8 . The method of claim 1 , wherein the crystalline products is a garnet type ceramic material with a cubic structure as measured by X-ray diffraction (XRD) analysis.
9 . The method of claim 1 , wherein the liquid mixture comprises the lithium-containing salt, a lanthanum-containing salt, a zirconium-containing salt, and wherein the crystalline products of the SSE material as measured by X-ray diffraction (XRD) analysis are garnet type ceramic material with a cubic structure.
10 . The method of claim 1 , wherein the liquid mixture comprises the lithium-containing salt, a lanthanum-containing salt, a zirconium-containing salt, and an aluminum-containing salt, and wherein the crystalline products of the SSE material as measured by X-ray diffraction (XRD) analysis are garnet type ceramic material with a cubic structure.
11 . The method of claim 1 , wherein the liquid mixture comprises the lithium-containing salt, a lanthanum-containing salt, a zirconium-containing salt, and wherein the crystalline products of the SSE material as measured by X-ray diffraction (XRD) analysis are garnet type ceramic material with a tetragonal structure.
12 . The method of claim 1 , wherein the liquid mixture comprises the lithium-containing salt, a lanthanum-containing salt, a tantalum-containing salt, and wherein the crystalline products of the SSE material as measured by X-ray diffraction (XRD) analysis are garnet type ceramic material with a cubic structure.
13 . The method of claim 1 , wherein the liquid mixture comprises the lithium-containing salt, a lanthanum-containing salt, a titanium-containing salt, and wherein the crystalline products of the SSE material are perovskite type ceramic material.
14 . The method of claim 1 , wherein the liquid mixture comprises the lithium-containing salt, an aluminum-containing salt, a phosphorus-containing salt, and wherein the crystalline products of the SSE material as measured by X-ray diffraction (XRD) analysis are sodium superionic conductor (NASICON) type ceramic material with a hexagonal structure.
15 . The method of claim 1 , wherein the liquid mixture comprises the lithium-containing salt, a germanium-containing salt, and wherein the SSE material is a ceramic material.
16 . The method of claim 1 , wherein the liquid mixture comprises the lithium-containing salt, a sulfur-containing salt, and wherein the SSE material is a sulfide material.
17 . The method of claim 1 , wherein D 1 , D 2 , . . . , DN is selected from the group consisting of La, Zr, Al, Ta, Ti, Ge, Mg, Mn, Zr, Zn, Nb, Ce, Sn, Ga, Ba, Ac, Ca, Sc, V, Cr, Fe, Cu, B, As, Hf, Mo, W, Re, Ru, Rh, Pt, Ag, Os, Ir, Au, F, CI, I, Br, and combinations thereof.
18 . The method of claim 1 , wherein the SSE material is selected from the group consisting of Li 7 La 3 Zr 2 O 12 , Li 6.75 La 3 Zr 1.75 Ta 0.25 O 12 , Li 6.5 La 3 Zr 2 Al 0.25 O 12 , Li 6.5 La 3 Zr 2 Al 0.24 O 12 , Li 6.5 La 3 Zr 2 Al 0.22 O 12 , Li 6.76 La 2.87 Zr 2.0 Al 0.24 O 12.35 , Li 6.74 La 2.96 Zr 2.0 Al 0.25 O 12.45 , Li 6.27 La 3.22 Zr 2.0 Al 0.3 O 12.39 , Li 6.4 La 2.86 Zr 2.0 Al 0.24 O 11.98 , Li 6.43 La 2.93 Zr 2.0 Al 0.24 O 12.08 , Li 6.32 La 3.2 Zr 2.0 Al 0.46012.9 , Li 6.57 La 2.99 Zr 2.0 Al 0.22 O 12.22 , Li 6.54 La 2.82 Zr 2.0 Al 0.24 O 12.08 , Li 6.49 La 3.28 Zr 2.0 Al 0.31 O 12.7 , Li 6.4 La 3 Zr 2 Al 0.2 O 12 , Li 6.49 La 3.02 Zr 2.0 Al 0.23 O 12.2 , Li 6.28 La 3 Zr 2 Al 0.24 O 12 , Li 6.25 La 3.01 Zr 2.0 Al 0.22 O 11.92 , Li 6.25 La 3 Zr 2 Al 0.25 O 12 , Li 6.5 La 3 Zr 1.5 Ta 0.5 O 12 , Li 6.15 La 3 Zr 1.75 Ta 0.25 Al 0.2 O 12 , Li 6.15 La 3 Zr 1.75 Ta 0.25 Ga 0.2 O 12 , Li 6.25 La 3 Zr 2 Ta 0.25 Ga 0.2 O 12 , Li 6.4 La 3 Zr 2 Ga 0.2 O 12 , Li 6.4 La 3 Zr 1.4 Ta 0.6 O 12 , and combinations thereof.
19 . The method of claim 1 , further comprising:
sintering the crystalline products of the SSE material at an annealing temperature of 900° C. or higher to further process the SSE material; and
measuring the ionic conductivity of the SSE material.
20 . A method of producing a solid-state electrolyte material, comprising,
forming a liquid mixture of digitally-controlled stoichiometrically amounts of a lithium-containing salt, a lanthanum-containing salt, a zirconium-containing salt, and one or more inorganic salts containing one or more metals D 1 , D 2 , . . . , D N to be mixed with a first gas flow to form a gas-liquid mixture;
jetting a mist of the liquid mixture into a power jetting chamber;
drying the gas-liquid mixture for a first reaction time period of less than 20 min to undergo one or more oxidation reactions in the presence of a second gas flow of a heated gas and form a gas-solid mixture;
delivering the gas-solid mixture out of the power jetting chamber;
separating the gas-solid mixture into one or more solid particles of the SSE material;
delivering the one or more solid particles into an annealing chamber; and
annealing the one or more solid particles of the SSE material for a second reaction time period of more than 2 hours to undergo a dynamic crystallization process in the presence of a third gas flow and obtain crystalline products, wherein the final crystalline products of the SSE materials is a ceramic material having a measured ionic conductivity (σ) of larger than 10 −4 S per centimeter at 25° C., and a chemical composition of Li a La b Zr c D1 d D2 e . . . DN n O v , wherein 6.25≤a≤7.2, 2.8≤b≤3.5, 1.2≤c≤2.2, 2.0 ≤v≤12, and wherein at least one of D 1 , D 2 , . . . , D N is a metal, N≥0, 0≤d≤0.8, 0≤e≤0.8, and 0 ≤n≤0.8.
21 . The method of claim 20 , wherein the SPAN value (D 90 −D 10 )/D 50 of the crystalline products after annealing is 0.8<SPAN≤1.0.
22 . The method of claim 20 , wherein the SPAN value (D 90 −D 10 )/D 50 of the crystalline products after annealing is 0.8<SPAN≤1.7.
23 . The method of claim 20 , wherein the D 50 of the crystalline products after annealing is between 10 μm and 18 um.
24 . The method of claim 20 , wherein the D 90 of the crystalline products after annealing are at between 20 μm and 40 μm, the D 10 are between 3 μm and 10 μm, the D 99 are between 35 μm and 60 μm, and the D 1 are between 0.1 μm and 3 μm.
25 . A method of producing a solid-state electrolyte (SSE) material, comprising,
flowing a first flow of a first gas to be mixed with a liquid mixture of digitally-controlled stoichiometrically amounts of a lithium-containing salt, one or more inorganic salts containing one or more metals D 1 , D 2 , . . . , D N ;
forming a gas-liquid mixture and jetting a mist of the liquid mixture into a power jetting chamber;
delivering a second gas flow of a heated gas into the power jetting chamber;
drying the gas-liquid mixture for a first reaction time period of less than 20 min to undergo one or more oxidation reactions in the presence of the second gas flow and form a gas-solid mixture;
deliver the gas-solid mixture out of the power jetting chamber;
separate the gas-solid mixture into one or more solid particles of the SSE material;
deliver the one or more solid particles into an annealing chamber;
annealing the one or more solid particles of the SSE material for a second reaction time period of more than 2 hours to undergo a dynamic crystallization process in the presence of a third gas flow and obtain crystalline products; and
milling the crystalline products of the SSE material to obtain nano-sized particles, wherein the crystalline products of the SSE material are in spherical clusters under scanning electronic microscopy (SEM) analysis.