SOLID ELECTROLYTES, BATTERIES, AND METHODS
20220263124 · 2022-08-18
Inventors
Cpc classification
Y02E60/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C01P2002/72
CHEMISTRY; METALLURGY
H01M10/0525
ELECTRICITY
C01B25/14
CHEMISTRY; METALLURGY
International classification
C01B25/14
CHEMISTRY; METALLURGY
Abstract
Electrolytes, methods of preparing electrolytes, and batteries include electrolytes. Electrolytes may include a material of formula (I), Li.sub.3PS.sub.4-xO.sub.x, wherein x is 0<x≤1. The electrolytes may be glass-ceramic electrolytes. Batteries including electrolytes may be lithium-ion batteries.
Claims
1. An electrolyte comprising a material of formula (I):
Li.sub.3PS.sub.4-xO.sub.x formula (I); wherein 0<x≤1.
2. The electroyte of claim 1, wherein 0<x<1.
3. The electrolyte of claim 1, wherein 0<x≤0.5.
4. The electrolyte of claim 1, wherein 0<x≤0.35.
5. The electrolyte of claim 1, wherein 0<x≤0.31.
6. The electrolyte of claim 1, wherein x is (i) 0.1, (ii) 0.25, (iii) 0.31, or (iv) 0.5.
7. The electrolyte of claim 1, wherein the electrolyte consists of the material of formula (I).
8. The electrolyte of claim 1, wherein the electrolye is in the form of a powder.
9. The electrolyte of claim 1, wherein the electrolye is in the form of a pellet, the pellet having a density of about 1.5 g/cm.sup.3 to about 2 g/cm.sup.3.
10. The electrolyte of claim 1, wherein x is greater than 0, and the electrolye has an activation energy that is less than an activation energy of β-Li.sub.3PS.sub.4.
11. The electrolyte of claim 10, wherein the activation energy is at least 5% less than the activation energy of β-Li.sub.3PS.sub.4.
12. The electrolyte of claim 1, wherein x is greater than 0, and the electrolyte has an ionic conductivity that is at least 5 times greater than an ionic conductivity of β-Li.sub.3PS.sub.4.
13. A lithium-ion battery comprising the electrolyte of claim 1.
14. A method for forming the electrolyte of claim 1, the method comprising: contacting Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 to form the electrolyte.
15. The method of claim 14, wherein the contacting of Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 comprises (i) mixing Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5, (ii) homogenizing Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 under vacuum, or (iii) a combination thereof.
16. The method of claim 14, wherein the homogenizing of Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 under vacuum comprises milling Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 with a milling media, wherein a weight ratio of the milling media to the total weight of Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 is about 10:1 to about 20:1.
17. The method of claim 14, wherein the electrolye is a powder, and the method further comprises pressing the powder into a pellet.
18. The method of claim 17, wherein the pressing of the powder into the pellet comprises subjecting the powder to a pressure of at least 200 MPa, and a temperature of at least 200° C.
19. The method of claim 18, wherein the powder is subjected to the pressure and the temperature simultaneously.
20. An electrolyte comprising a material of formula (I):
Li.sub.3PS.sub.4-xO.sub.x formula (I); wherein x is 0.1<x≤0.31.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0017]
[0018]
[0019]
[0020]
[0021]
[0022]
[0023]
[0024]
[0025]
[0026]
[0027]
[0028]
[0029]
[0030]
[0031]
[0032]
[0033]
[0034]
[0035]
[0036]
[0037]
[0038]
[0039]
[0040]
[0041]
[0042]
[0043]
[0044]
[0045]
[0046]
[0047]
[0048]
[0049]
[0050]
[0051]
[0052]
[0053]
[0054]
[0055]
DETAILED DESCRIPTION
[0056] Provided herein are electrolytes, batteries, and methods for making electrolytes, such as the electrolytes described herein.
Electrolytes and Batteries
[0057] In some embodiments, the electrolytes provided herein include a material of formula (I):
Li.sub.3PS.sub.4-xO.sub.x formula (I);
wherein x is 0<x≤1.
[0058] In some embodiments, the electrolyes provided herein include a material of formula (I), wherein 0<x<1, 0<x<0.9, 0<x<0.8, 0<x<0.7, 0<x<0.6, 0<x<0.5, 0<x<0.4, 0<x<0.35, 0<x<0.31, 0<x<0.3, 0<x<0.25, 0<x<0.2, 0<x<0.15, or 0<x<0.1.
[0059] In some embodiments, the electrolyes provided herein include a material of formula (I), wherein 0<x≤1, 0<x≤0.9, 0<x≤0.8, 0<x≤0.7, 0<x≤0.6, 0<x≤0.5, 0<x≤0.4, 0<x≤0.35, 0<x≤0.31, 0<x≤0.3, 0<x≤0.25, 0<x≤0.2, 0<x≤0.15, or 0<x≤0.1.
[0060] In some embodiments, the electrolyes provided herein include a material of formula (I), wherein 0.1<x<1, 0.15<x<1, 0.2<x<1, 0.25<x<1, 0.3<x<1, 0.31<x<1.
[0061] In some embodiments, the electrolyes provided herein include a material of formula (I), wherein 0.1<x≤1, 0.15<x≤1, 0.2<x≤1, 0.25<x≤1, 0.3<x≤1, or 0.31<x≤1.
[0062] In some embodiments, the electrolyes provided herein include a material of formula (I), wherein 0.1<x<0.5, 0.15<x<0.5, 0.2<x<0.5, 0.25<x<0.5, 0.3<x<0.5, 0.31<x<0.5.
[0063] In some embodiments, the electrolyes provided herein include a material of formula (I), wherein 0.1<x≤0.5, 0.15<x≤0.5, 0.2<x≤0.5, 0.25<x≤0.5, 0.3<x≤0.5, 0.31<x≤0.5.
[0064] In some embodiments, the electrolytes provided herein include a material of formula (I), wherein x is 0.1, 0.11, 0.12, 0.13, 0.14, 0.15, 0.16, 0.17, 0.18, 0.19, 0.2, 0.21, 0.22, 0.23, 0.24, 0.25, 0.26, 0.27, 0.28, 0.29, 0.30, 0.31, 0.32, 0.33, 0.34, 0.35, 0.36, 0.37, 0.38, 0.39, 0.4, 0.41, 0.42, 0.43, 0.44, 0.45, 0.46, 0.47, 0.48, 0.49, 0.5, 0.51, 0.52, 0.53, 0.54, 0.55, 0.56, 0.57, 0.58, 0.59, 0.6, 0.61, 0.62, 0.63, 0.64, 0.65, 0.66, 0.67, 0.68, 0.69, 0.7, 0.71, 0.72, 0.73, 0.74, 0.75, 0.76, 0.77, 0.78, 0.79, 0.8, 0.81, 0.82, 0.83, 0.84, 0.85, 0.86, 0.87, 0.88, 0.89, 0.9, 0.91, 0.92, 0.93, 0.94, 0.95, 0.96, 0.97, 0.98, or 0.99.
[0065] In some embodiments, the electrolyte consists of a material of formula (I).
[0066] The electrolytes provided herein may be in any physical form. The electrolytes, for example, may be solid electrolytes. The solid electrolytes may be glass-ceramic electrolytes. As used herein, the phrase “glass-ceramic electrolyte” refers to an electrolyte having at least one type of functional crystalline phase and a residual glass. The solid electrolytes may be in the form of a powder. The solid electrolytes may be in the form of a pellet. The pellet may have any density that is suitable for a desired application, such as lithium-ion batteries. In some embodiments, the solid electrolytes, such as the solid electrolytes in the form of a pellet, have a density of about 1 g/cm.sup.3 to about 3 g/cm.sup.3, about 1.5 g/cm.sup.3 to about 2.5 g/cm.sup.3, or about 1.5 g/cm.sup.3 to about 2 g/cm.sup.3.
[0067] In some embodiments, x is greater than 0, and the electrolye has an activation energy that is less than an activation energy of β-Li.sub.3PS.sub.4. The activation energy, for example, may be at least 1%, at least 3%, at least 5%, at least 10%, at least 20%, or at least 25% less than an activation energy of β-Li.sub.3PS.sub.4.
[0068] In some embodiments, x is greater than 0, and the electrolyte has an ionic conductivity that is at least 3 times, at least 4 times, at least 5 times, at least 6 times, at least 7 times, or at least 10 times greater than an ionic conductivity of β-Li.sub.3PS.sub.4.
[0069] Also provided herein are batteries that include one or more electrolytes provided herein. In some embodiments, the battery is a lithium-ion battery. The batteries may include an anode, a cathode, and an electrolyte described herein. The electrolyte may be arranged between the anode and the cathode.
Methods
[0070] Also provided herein are methods of forming electrolytes. In some embodiments, the methods include contacting Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 to form an electrolyte. When the methods are used to produce electrolytes that include a composition of formula (I), the ratios of Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 that are contacted may be selected to achieve a desired value for “x” of formula (I).
[0071] The Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 may be contacted using any known technique. In some embodiments, the contacting of Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 includes (i) mixing Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5, (ii) homogenizing Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 under vacuum, or (iii) a combination thereof.
[0072] The homogenizing of Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 under vacuum may include milling Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 with a milling media, wherein a weight ratio of the milling media to the total weight of Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 is about 10:1 to about 20:1, about 12:1 to about 18:1, about 12:1 to about 16:1, about 13:1 to about 15:1, or about 14:1. As used herein, the term “milling” refers to crushing, grinding, or a combination thereof, and the phrase “milling media” refers object(s) used to crush and/or grind. Non-limiting examples of milling media that may be used in the methods herein include one or more three-dimensional objects, such as balls, cylinders, etc., which may be formed of metal, ceramic, glass, etc.
[0073] In some embodiments, the methods also include pressing an electrolyte, such as an electrolyte in powder form, into a pellet. The pressing of the elecrolyte, such as an electrolyte in powder form, into a pellet includes subjecting the electrolyte to a pressure of at least 100 MPa, at least 150 MPa, at least 200 MPa, at least 250 MPa, or at least 300 MPa, and a temperature of at least 100° C., at least 150° C., at least 200° C., at least 250° C., or at least 300° C. The electrolyte may be subjected to the pressure and the temperature simultaneously, sequentially, or a combination thereof.
EMBODIMENTS
[0074] The following listing provides non-limiting embodiments of the electrolytes, batteries, and methods provided herein:
Embodiment 1
[0075] An electrolyte comprising a material of formula (I):
Li.sub.3PS.sub.4-xO.sub.x formula (I);
wherein x is 0<x≤1.
Embodiment 2
[0076] The electrolyte of Embodiment 1, wherein 0<x<1, 0<x<0.9, 0<x<0.8, 0<x<0.7, 0<x<0.6, 0<x<0.5, 0<x<0.4, 0<x<0.35, 0<x<0.31, 0<x<0.3, 0<x<0.25, 0<x<0.2, 0<x<0.15, or 0<x<0.1.
Embodiment 3
[0077] The electrolyte of Embodiment 1, wherein 0<x≤1, 0<x≤0.9, 0<x≤0.8, 0<x≤0.7, 0<x≤0.6, 0<x≤0.5, 0<x≤0.4, 0<x≤0.35, 0<x≤0.31, 0<x≤0.3, 0<x≤0.25, 0<x≤0.2, 0<x≤0.15, or 0<x≤0.1.
Embodiment 4
[0078] The electrolyte of Embodiment 1, wherein 0.1<x<1, 0.15<x<1, 0.2<x<1, 0.25<x<1, 0.3<x<1, 0.31<x<1.
Embodiment 5
[0079] The electrolyte of Embodiment 1, wherein 0.1<x≤1, 0.15<x≤1, 0.2<x≤1,0.25<x≤1,0.3<x≤1, or 0.31<x≤1.
Embodiment 6
[0080] The electrolyte of Embodiment 1, wherein 0.1<x<0.5, 0.15<x<0.5, 0.2<x<0.5, 0.25<x<0.5, 0.3<x<0.5, 0.31<x<0.5.
Embodiment 7
[0081] The electrolyte of Embodiment 1, wherein 0.1<x≤0.5, 0.15<x≤0.5, 0.2<x≤0.5, 0.25<x≤0.5, 0.3<x≤0.5, 0.31<x≤0.5.
Embodiment 8
[0082] The electrolyte of Embodiment 1, wherein x is 0.1, 0.11, 0.12, 0.13, 0.14, 0.15, 0.16, 0.17, 0.18, 0.19, 0.2, 0.21, 0.22, 0.23, 0.24, 0.25, 0.26, 0.27, 0.28, 0.29, 0.30, 0.31, 0.32, 0.33, 0.34, 0.35, 0.36, 0.37, 0.38, 0.39, 0.4, 0.41, 0.42, 0.43, 0.44, 0.45, 0.46, 0.47, 0.48, 0.49, 0.5, 0.51, 0.52, 0.53, 0.54, 0.55, 0.56, 0.57, 0.58, 0.59, 0.6, 0.61, 0.62, 0.63, 0.64, 0.65, 0.66, 0.67, 0.68, 0.69, 0.7, 0.71, 0.72, 0.73, 0.74, 0.75, 0.76, 0.77, 0.78, 0.79, 0.8, 0.81, 0.82, 0.83, 0.84, 0.85, 0.86, 0.87, 0.88, 0.89, 0.9, 0.91, 0.92, 0.93, 0.94, 0.95, 0.96, 0.97, 0.98, or 0.99.
Embodiment 9
[0083] The electrolyte of any one of Embodiments 1 to 8, wherein the electrolyte consists of the material of formula (I).
Embodiment 10
[0084] The electrolyte of any one of Embodiments 1 to 9, wherein the electrolyte is a solid electrolyte.
Embodiment 11
[0085] The electrolyte of Embodiment 10, wherein the solid electrolyte is a glass-ceramic electrolyte.
Embodiment 12
[0086] The electrolyte of Embodiment 10 or 11, wherein the electrolye is in the form of a powder.
Embodiment 13
[0087] The electrolyte of any of Embodiments 1 to 12, wherein the electrolye is in the form of a pellet.
Embodiment 14
[0088] The electrolyte of Embodiment 13, wherein the pellet has a density of about 1 g/cm.sup.3 to about 3 g/cm.sup.3, about 1.5 g/cm.sup.3 to about 2.5 g/cm.sup.3, or about 1.5 g/cm.sup.3 to about 2 g/cm.sup.3.
Embodiment 15
[0089] The electrolyte of any of Embodiments 1 to 14, wherein x is greater than 0, and the electrolye has an activation energy that is less than an activation energy of β-Li.sub.3PS.sub.4.
Embodiment 16
[0090] The electrolyte of Embodiment 15, wherein the activation energy is at least 1%, at least 3%, at least 5%, at least 10%, at least 20%, or at least 25% less than an activation energy of β-Li.sub.3PS.sub.4.
Embodiment 17
[0091] The electrolyte of any of Embodiments 1 to 16, wherein x is greater than 0, and the electrolyte has an ionic conductivity that is at least 3 times, at least 4 times, at least 5 times, at least 6 times, at least 7 times, or at least 10 times greater than an ionic conductivity of β-Li.sub.3PS.sub.4.
Embodiment 18
[0092] A battery including an electrolyte of any of Embodiments 1 to 17.
Embodiment 19
[0093] The battery of Embodiment 18, wherein the battery is a lithium-ion battery.
Embodiment 20
[0094] A method forming an electrolyte, such as an electrolyte of any of Embodiments 1 to 17, wherein the method includes contacting Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 to form the electrolyte.
Embodiment 21
[0095] The method of Embodiment 20, wherein the contacting of Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 comprises (i) mixing Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5, (ii) homogenizing Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 under vacuum, or (iii) a combination thereof.
Embodiment 22
[0096] The method of Embodiment 20 or 21, wherein the homogenizing of Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 under vacuum comprises milling Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 with a milling media.
Embodiment 23
[0097] The method of Embodiment 22, wherein a weight ratio of the milling media to the total weight of Li.sub.2S, P.sub.2S.sub.5, and P.sub.2O.sub.5 is about 10:1 to about 20:1, about 12:1 to about 18:1, about 12:1 to about 16:1, about 13:1 to about 15:1, or about 14:1.
Embodiment 24
[0098] The method of any of Embodiments 20 to 23, wherein the method further comprises pressing the electrolyte into a pellet.
Embodiment 25
[0099] The method of Embodiment 24, wherein the pressing of the elecrolyte, such as an electrolyte in powder form, into a pellet includes subjecting the electrolyte to a pressure of at least 100 MPa, at least 150 MPa, at least 200 MPa, at least 250 MPa, or at least 300 MPa, and a temperature of at least 100° C., at least 150° C., at least 200° C., at least 250° C., or at least 300° C.
Embodiment 26
[0100] The method of Embodiment 25, wherein the electrolyte is subjected to the pressure and the temperature simultaneously, sequentially, or a combination thereof.
[0101] All referenced publications are incorporated herein by reference in their entirety. Furthermore, where a definition or use of a term in a reference, which is incorporated by reference herein, is inconsistent or contrary to the definition of that term provided herein, the definition of that term provided herein applies and the definition of that term in the reference does not apply.
[0102] While certain aspects of conventional technologies have been discussed to facilitate disclosure of various embodiments, applicants in no way disclaim these technical aspects, and it is contemplated that the present disclosure may encompass one or more of the conventional technical aspects discussed herein.
[0103] The present disclosure may address one or more of the problems and deficiencies of known methods and processes. However, it is contemplated that various embodiments may prove useful in addressing other problems and deficiencies in a number of technical areas. Therefore, the present disclosure should not necessarily be construed as limited to addressing any of the particular problems or deficiencies discussed herein.
[0104] In this specification, where a document, act or item of knowledge is referred to or discussed, this reference or discussion is not an admission that the document, act or item of knowledge or any combination thereof was at the priority date, publicly available, known to the public, part of common general knowledge, or otherwise constitutes prior art under the applicable statutory provisions; or is known to be relevant to an attempt to solve any problem with which this specification is concerned.
[0105] In the descriptions provided herein, the terms “includes,” “is,” “containing,” “having,” and “comprises” are used in an open-ended fashion, and thus should be interpreted to mean “including, but not limited to.” When methods or apparatuses are claimed or described in terms of “comprising” various steps or components, the methods or apparatuses can also “consist essentially of” or “consist of” the various steps or components, unless stated otherwise.
[0106] The terms “a,” “an,” and “the” are intended to include plural alternatives, e.g., at least one. For instance, the disclosure of “an electrolyte,” “a pellet,” “a powder”, and the like, is meant to encompass one, or mixtures or combinations of more than one electrolyte, pellet, powder, and the like, unless otherwise specified.
[0107] Various numerical ranges may be disclosed herein. When Applicant discloses or claims a range of any type, Applicant's intent is to disclose or claim individually each possible number that such a range could reasonably encompass, including end points of the range as well as any sub-ranges and combinations of sub-ranges encompassed therein, unless otherwise specified. Moreover, all numerical end points of ranges disclosed herein are approximate. As a representative example, Applicant discloses, in some embodiments, that the pellet may have a density of about 1.5 g/cm.sup.3 to about 2 g/cm.sup.3. This range should be interpreted as encompassing about 1.5 g/cm.sup.3 to about 2 g/cm.sup.3, and further encompasses “about” each of 1.6 g/cm.sup.3, 1.7 g/cm.sup.3, 1.8 g/cm.sup.3, and 1.9 g/cm.sup.3, including any ranges and sub-ranges between any of these values.
[0108] As used herein, the term “about” means plus or minus 10% of the numerical value of the number with which it is being used.
EXAMPLES
[0109] The present invention is further illustrated by the following examples, which are not to be construed in any way as imposing limitations upon the scope thereof. On the contrary, it is to be clearly understood that resort may be had to various other aspects, embodiments, modifications, and equivalents thereof which, after reading the description herein, may suggest themselves to one of ordinary skill in the art without departing from the spirit of the present invention or the scope of the appended claims. Thus, other aspects of this invention will be apparent to those skilled in the art from consideration of the specification and practice of the invention disclosed herein.
Example 1
Synthesis of Li.SUB.3.PS.SUB.4-x.O.SUB.x
[0110] This example provides a solid-state synthesis of Li.sub.3PS.sub.4-xO.sub.x, wherein x=0.31, which yielded a sevenfold increase in ionic conductivity and a lower activation energy compared to experimental β-Li.sub.3PS.sub.4. Detailed variable temperature electrochemical impedance spectroscopy (EIS) analysis was implemented to probe the short-range and long-range Li-ion motion and Arrhenius prefactor.
[0111] In addition, the Jonscher-type power law exponent was computed to confirm the enhanced dimensionality of Li-ion motion in Li.sub.3PS.sub.4-xO.sub.x compared to the experimental β-Li.sub.3PS.sub.4. Li.sub.3PS.sub.4-xO.sub.x were investigated using PXRD to confirm the β-Li.sub.3PS.sub.4 phase at room temperature in addition to .sup.6Li and .sup.31P MAS NMR to elucidate the change in local structure. Computational studies using AIMD simulations were also carried out to understand the cause of the enhanced conductivity and decreased activation energy. These results, as explained below, showed that optimal amounts of oxygen substitution with respect to electrochemical performance could yield 3D Li-ion transport pathways and an intrinsic concentration gradient of Li, giving widened Li channels.
[0112] In this example, Li.sub.3PS.sub.369O.sub.0.31 was synthesized, and the Li.sub.3PS.sub.369O.sub.0.31 had an ionic conductivity of 1.38 mS/cm at 25° C., which was 7 times greater than that of pristine β-Li.sub.3PS.sub.4.
[0113] Detailed analysis of variable-temperature EIS and solid-state NMR showed that the enhanced Li-ion conduction could likely be ascribed to a transition from 2D to 3D Li-ion motion upon oxygen substitution, due to the formation of a (PS.sub.3xO.sub.x).sup.3− unit.
[0114] Further oxygen substitution likely caused the evolution of lithium phosphate impurities, which probably contributed to a decline in ionic conductivity. Computational studies to understand the origin of this enhancement supported the enhancement in dimensionality of Li-ion motion also, likely due to a wider Li channel attributed to the intrinsic Li concentration gradient up to a critical oxygen concentration.
[0115] All chemicals were used as received. Stoichiometric amounts of Li.sub.2S (Alfa Aesar, 99.9%), P.sub.2S.sub.5 (Sigma-Aldrich, 99.9%), and P.sub.2O.sub.5 (Alfa Aesar, 99.99%) were gently mixed using Agar mortar and pestle for 10 m and then homogenized for 10 h under vacuum using a SPEX 8000M high energy mixer. The ratio of the milling media (two zirconia balls; ∅.sub.OD=10 mm) to the total weight of precursors was roughly 14:1. The mixed powders were pressed into a 6-mm diameter pellet (Across International) under a pressure of ˜400 MPa and then heated at 230° C. for 2 h (ramping rate of 1° C./minute) followed by natural cooling. The approximate pellet density used was 1.8 g/cm.sup.3. Sample handling and heat treatment were all performed under Ar (H.sub.2O<1 ppm and O.sub.2<1 ppm) in glovebox.
[0116] Materials Characterization. Impedance measurements on Li.sub.3PS.sub.4-xO.sub.x were carried out using a Gamry Ref 600′ and home-built PEEK cylindrical cell with indium foil as blocking electrodes. Variable-temperature Nyquist spectra were collected from −40° C. to 120° C. (increment of 10° C. per measurement, except 25° C.) within a scanning frequency range from 5 MHz to 1 Hz under a biased potential of 100 mV.
[0117] All the measurements were performed in a Cincinnati Sub-Zero Temperature Chamber under dry air atmosphere to prevent H.sub.2O contamination. PXRD measurements were conducted with a PANalytical X′Pert Pro-MPD Powder Diffractometer with Cu-K.sub.α radiation. KAPTON® film was employed to reduce reactions of Li.sub.3PS.sub.4-xO.sub.x with moist air. MAS NMR measurements on Li.sub.3PS.sub.4-xO.sub.x were performed on a Bruker Avance III 500 MHz NMR spectrometer with a spinning rate of 25 kHz at room temperature. .sup.31P (Larmor frequency=202.404 MHz) NMR spectra were acquired using a Hahn Echo pulse sequence with a pulse length of 4.200 μs and a recycle delay of 200 s. A single pulse with a pulse length of 4.750 μs was employed to obtain .sup.6Li (Larmor frequency=73.58 MHz) NMR spectra using a recycle delay of 200 s). .sup.7Li spin-lattice relaxation time was performed using an inversion recovery pulse sequence. .sup.6Li and .sup.31P chemical shift were referenced to solid LiCl (−1.1 ppm) and to 85% H.sub.3PO.sub.4 (0 ppm), respectively.
Example 2
Calculations
[0118] The structure of β-Li.sub.3PS.sub.4 was taken from Materials Project (ID: mp-985583). Vienna ab initio simulation package (VASP) was used for density functional theory (DFT) energy calculations with the projector-augmented-wave method (see, e.g., P. E. Blöchl, Physical Review B 1994, 50, 17953-17979; G. Kresse, J. Furthmüller, Physical Review B 1996, 54, 11169-11186) in Perdew-Burke-Ernzerhof generalized-gradient approximation (PBE-GGA) (J. P. Perdew, K. Burke, M. Ernzerhof, Physical Review Letters 1996, 77, 3865-3868). An energy cutoff of 520 eV and a k-point density of around 800 per number of atoms in the unit cell were used for all computations. The software suite pymatgen was employed to order the 25 structures of O-substituted Li.sub.3PS.sub.4 at different substitution levels with the lowest energy determined by electrostatic interaction (S. P. Ong, W. D. Richards, A. Jain, G. Hautier, M. Kocher, S. Cholia, D. Gunter, V. L. Chevrier, K. A. Persson, G. Ceder, Computational Materials Science 2013, 68, 314-319). The energy above hull for each structure was calculated based on the database of Materials Project after DFT energy was obtained from the geometry optimization on VASP. All the other parameters involved were the same as default settings in pymatgen. The isotropic chemical shifts were calculated by magnetic shieldings using perturbation theory (linear response) (C. J. Pickard, F. Mauri, Phys. Rev. B 2001, 63, 245101; and J. R. Yates, C. J. Pickard, F. Mauri, Phys. Rev. B 2007, 76, 024401). The calibration factors of .sup.6/7Li (+90.5 ppm) and .sup.31P (+254 ppm) were estimated from the difference between experimental and calculated isoshift of pristine β-Li.sub.3PS.sub.4. All the configurations that were selected for NMR calculations had the lowest total energy among all the DFT-optimized structures of the same O doping level. An energy cutoff of 600 eV was applied to the system to meet the high-accuracy criterion for such calculations. For better visualization, Lorenzen line-broadening was conducted with broadening factors listed in the following table:
TABLE-US-00001 Summary of simulated Lorenzen line-broadening factors of different peaks in Li.sub.3PS.sub.4-xO.sub.x (x = 0, 0.125, 0.25). Modified Sample Li½ Li3 Li □-PS.sub.4.sup.3− PS.sub.3O.sup.3− Li.sub.3PS.sub.4 0.9 0.5 0.95 1 N/A Li.sub.3PS.sub.3.875O.sub.0.125 0.9 0.5 0.95 2 4.2 Li.sub.3PS.sub.3.75O.sub.0.25 0.9 0.5 0.95 10.5 8
[0119] Line-broadening was more significant for calculated results since they were determined at 0 K and no ion exchange was simulated. At room temperature, rapid Li.sup.+ ion exchange reduced line width of NMR peaks.
[0120]
[0121]
[0122] The broadening in diffraction peaks with low intensity indicated that Li.sub.3PS.sub.4-xO.sub.x was glass-ceramic. When x was higher than 0.31 in Li.sub.3PS.sub.4-xO.sub.x, a further reduction of crystallinity lead to an almost featureless powder pattern, which made the phase identification challenging. The change in long-range order from glass-ceramic to nearly glass in Li.sub.3PS.sub.4-xO.sub.x could be explained by the enthalpy of mixing, ΔH.sub.mix calculations. As shown in
[0123] To understand the structural evolution of local environment due to oxygen substitution in Li.sub.3PS.sub.4-xO.sub.x, .sup.6Li and .sup.31P solid-state NMR was employed. As shown at
[0124] Since there was a large loss of crystallinity for higher oxygenated samples, deconvolution was only performed on Li.sub.3PS.sub.4, Li.sub.3PS.sub.3.9O.sub.0.1, Li.sub.3PS.sub.3.75O.sub.0.25, and Li.sub.3P.sub.3.69O.sub.0.31 as shown at
[0125] For Li.sub.3PS.sub.4, there were three peaks assigned, one was the combined Li1/Li2 site which corresponded to the 8d and 4b Wyckoff sites respectively and were assigned together due to their close distance and fast exchange (H. Stöffler, T. Zinkevich, M. Yavuz, A. Senyshyn, J. Kulisch, P. Hartmann, T. Adermann, S. Randau, F. H. Richter, J. Janek, et al., J. Phys. Chem. C 2018, 122, 15954-15965). The other was the Li3 site, which corresponded to the 4c Wyckoff site.
[0126] The last peak was at 1.5 ppm and was assigned to an unknown impurity, comprising 4% integral total. With increasing oxygen substitution, the impurity decreased to a negligible amount. In addition, the .sup.6Li integral % of the combined Li ½ assignment increased with a maximum for Li.sub.3P.sub.3.69O.sub.0.31. A decrease in the .sup.6Li integral % of the Li3 site occurred and the emergence of a new Li site (modified Li site) could be seen. This modified Li site was expected to promote long-range 3D Li-ion conduction and composed of Li in an off-centered tetrahedral site due to its bond with O. Isotropic .sup.6Li chemical shifts were simulated using perturbation theory for Li.sub.3PS.sub.4, Li.sub.3PS.sub.3.875O.sub.0.125, and Li.sub.3PS.sub.3.75O.sub.0.25 from DFT optimized structures of the same composition (
[0127]
[0128] To study the change in Li-ion mobility upon oxygen substitution, .sup.7Li spin-lattice relaxation time, T.sub.1, for Li.sub.3PS.sub.4, Li.sub.3PS.sub.3.9O.sub.0.1, Li.sub.3PS.sub.3.75O.sub.0.25, and Li.sub.3P.sub.3.69O.sub.0.31 was performed as depicted at
[0129] The local environment of the anionic sublattice in Li.sub.3PS.sub.4-xO.sub.x was investigated with .sup.31P NMR and the results are shown at
[0130] The .sup.31P resonances at 88 ppm and at 93 ppm were assigned to the (γ-PS.sub.4).sup.3− unit and the (P.sub.2S.sub.7).sup.4− unit, respectively. Li.sub.3P.sub.3.69O.sub.0.31 showed a minimum .sup.31P integral % of the (γ-PS.sub.4).sup.3 unit and a maximum for that of the (P.sub.2S.sub.7).sup.4 unit. In addition, an unknown sulfide impurity peak became apparent at 91 ppm, beginning when x=0.5. Since the unknown appeared small by intensity and likely did not contribute much to the changes in conductivity, it was not further studied. Upon greater oxygen introduction, lithium phosphate impurity peaked at 75 ppm, 70 ppm, 37 ppm, 9 ppm, and −3 ppm were increasingly formed, which were assigned to (POS.sub.2).sup.− (PS.sub.2O.sub.2).sup.3−, (PSO.sub.3).sup.3−, (PO.sub.4).sup.3− and (P.sub.2O.sub.7).sup.4−, respectively, as seen in
[0131] To relate the structure of Li.sub.3PS.sub.4-xO.sub.x to the electrochemical performance, EIS was performed. The conductivity isotherms of Li.sub.3PS.sub.3.69O.sub.0.31 are shown at
[0132] For the conductivity isotherms of Li.sub.3PS.sub.4-xO.sub.x (x=0, 0.1, 0.25, 0.31, 0.5, and 1;
[0133]
[0134] The obtained σ.sub.DC of Li.sub.3PS.sub.3.69O.sub.0.31 reached a maximum of 1.38 mS/cm, giving greater than a sevenfold enhancement in ionic conductivity compared to the experimental Li.sub.3PS.sub.4, which had a σ.sub.DC of 0.19 mS/cm. Substituting O for S with x>0.31 in Li.sub.3PS.sub.4-xO.sub.x lead to a reduction of ionic conductivity (see table below). The energy barrier of a.sub.Dc could be quantified with E.sub.a,DC using the Arrhenius law, σ.sub.DCT=σ.sub.0 exp(−E.sub.a,DC/(k.sub.BT)), where T is temperature in kelvin, σ.sub.0 is the Arrhenius pre-factor, and k.sub.B is the Boltzmann constant. As illustrated at
[0135] To better understand the EIS results, AIMD simulations were carried out at 600-1300 K for Li.sub.3PS.sub.4-xO.sub.x: x=0.0, 0.125, 0.25, and 1.0. With O.sup.2− doping, Li.sup.+ conductivity increased substantially. Optimal Oxygen concentration (x=0.25) lead to the highest conductivity and least Li-migration barrier (E.sub.a). Gradual oxygenation and resulting faster diffusion behavior till x=0.25 were associated with widening of Li-diffusion channel. At higher oxygen concentration, say x=1, channel width dropped and so did the conductivity.
[0136] Although computational prediction of optimal value of x to maximize the Li-conductivity had close agreement with the experiment, it was noted that AIMD results depicted the diffusion behavior at high temperature (>600K), shown at
[0137] Li probability density was plotted for three compositions of x in Li.sub.3PS.sub.4-xO.sub.x, and the results showed that when near the optimal amount of oxygen substitution with respect to ionic conductivity, a change from quasi-2D to 3D Li-diffusion paths was observed. Also, at the upper limits of oxygen substitution, Li.sub.3PS.sub.3O, localized Li-hopping occurred with interrupted long-range diffusion. This coincided well with the experimental power law exponent measurements as discussed above.
[0138] This explained the enhanced three-dimensional diffusion at x=0.25. However, loss of interconnection among the Li-domains lead to lowering in the long-range ionic conductivity for higher x, Li.sub.3PS.sub.3O, despite the higher dimensionality.
TABLE-US-00002 Calculated activation energy, conductivtiy, and Li channel width for Li.sub.3PS.sub.4, Li.sub.3PS.sub.3.875O.sub.0.125, Li.sub.3PS.sub.3.75O.sub.0.25, and Li.sub.3PS.sub.3O from ab initio molecular dynamics simulations x E.sub.a, eV σ, mS/cm l, Å 0 (β) 0.33 ± 0.02 0.60-1.16 1.82 0.125 0.31 ± 0.02 1.32-2.51 1.83 0.25 0.28 ± 0.01 4.76-6.76 1.84 1 0.31 ± 0,02 1.05-1.81 1.71
[0139] The power law exponent, n, is an empirical indicator to describe the effective dimensionality for conducting solids. 3D conduction was typically correlated with n≥0.7. Through analyzing the conductivity isotherm (−20° C.) for Li.sub.3PS.sub.4-xO.sub.x (0.sub.x (
TABLE-US-00003 Summary of EIS analysis on Li.sub.3PS.sub.4−xO.sub.x (x = 0, 0.1, 0.25, 0.31, 0.5, and 1). σ.sub.DC @ E.sub.a, DC 25° C. Ln σ.sub.0 E.sub.a, M′′ E.sub.ρ′, LT E.sub.ρ′, HT Sample (eV) (mS/cm) (S/cm*K) n (eV) (eV) (eV) Li.sub.3PS.sub.4 0.39 0.19 12.50 0.62 0.34 0.20 0.34 Li.sub.3PS.sub.3.9O.sub.0.1 0.38 0.51 12.69 0.65 0.35 0.19 0.33 Li.sub.3PS.sub.3.75O.sub.0.25 0.35 1.20 12.45 0.85 0.35 0.17 0.30 Li.sub.3PS.sub.3.69O.sub.0.31 0.34 1.38 12.09 0.87 0.34 0.18 0.28 Li.sub.3PS.sub.3.5O.sub.0.5 0.37 0.76 12.66 0.88 0.38 0.19 0.31 Li.sub.3PS.sub.3O.sub.1 0.39 0.20 12.55 0.95 0.39 0.23 0.33 E.sub.a, $ denotes activation energies obtained via EIS analysis under various conditions, in which $ = DC (direct current), M′′ (imaginary part of the complex electric modulus), and ρ′ (real part of resistivity), σ.sub.0 is Arrhenius pre-exponential factor. n is the Jonscher-type power law exponent. LT and HT denote low-temperature and high temperature, respectively.
[0140] This suggested a change in dimensionality of Li-ion conduction from 2D (Li.sub.3PS.sub.4; n=0.62) to 3D (Li.sub.3PS.sub.3.69O.sub.0.31; n=0.87). The improved dimensionality of conducting space was attributed to greater correlated ion motion.
[0141] This explained the lowering in ionic conductivity for Li.sub.3PS.sub.3.5O.sub.0.5 and Li.sub.3PS.sub.3O despite higher n. In fact, the exponent n represented the ratio of the backward hopping rate of ion motion to the site relaxation rate. Therefore, assuming the site relaxation rate was nearly the same, the stronger correlation among Li.sup.+—Li.sup.+ and the Li.sup.+—O.sup.2− pairs may have caused a rise in the backward hopping rate, that is, an unsuccessful hopping for Li.sup.+ to jump through the potential minima.
[0142] The physical picture of this behavior was localized ion hopping without any macroscopic Li-ion conduction. Also examined was whether the observed response of ion dynamics to frequency was coupled with grain boundary, i.e., low frequency response. Thus, the EIS data was analyzed with imaginary component of the complex electric modulus, M″. Take Li.sub.3PS.sub.3.69O.sub.0.31 as an example (
[0143] The single peak confirmed that bulk process was likely exclusively responsible for the observed Li-ion conduction; otherwise, another shoulder associated with the grain boundary should have emerged at the lower scanning frequency. The broad and slightly asymmetric lineshape indicated that the bulk process involved a distribution of macroscopic diffusion in different pathways. The ω.sub.max was identified on each isotherm to calculate the electrical relaxation rate, τ.sub.M″.sup.−1 (⋅.sub.max/2π=f.sub.max=τ.sub.M″.sup.−1). As the temperature increased, the ω.sub.max shifts to higher frequency; therefore, faster relaxation. Then, the activation energy E.sub.a,M″ (
[0144] The pre-factor could be understood according to the following equation:
[0145] Where z was the geometric factor, k.sub.B was the Boltzmann constant, N was the number of charge carriers, q was the charge of the ions, ΔS.sub.m was the migration entropy, a was the jump distance between sites, and v.sub.0 was the jump frequency. The number of charge carriers was not expected to largely contribute to the change in σ.sub.0, because the amount of Li per formula remained constant for all the compositions. To determine the contribution of the jump frequency to the pre-factor, the crossover frequency, ω.sub.c, was calculated according to:
[0146] The crossover frequency, where the transition from the σ.sub.DC plateau to the high-frequency dispersive region occurred, was used as an rough approximation for v.sub.0. The results given in
TABLE-US-00004 Crossover frequency and normalized values for x in Li.sub.3PS.sub.4-xO.sub.x (x = 0, 0.1, 0.25, 0.31, 0.5, and 1). Normalized Sample ω.sub.c (Hz) ω.sub.c Li.sub.3PS.sub.4 2.08 × 10.sup.7 0.32 Li.sub.3PS.sub.3.9O.sub.0.1 2.33 × 10.sup.7 0.36 Li.sub.3PS.sub.3.75O.sub.0.25 5.53 × 10.sup.7 0.86 Li.sub.3PS.sub.3.69O.sub.0.31 6.44 × 10.sup.7 1.00 Li.sub.3PS.sub.3.5O.sub.0.5 1.69 × 10.sup.7 0.26 Li.sub.3PS.sub.3O.sub.1 7.11 × 10.sup.6 0.11
[0147] From this, the change in jump frequency was not expected to contribute largely to the change in σ.sub.0 either, otherwise the trend would have followed that of the Arrhenius prefactor. Moreover, the migration entropy (ΔS.sub.m), as illustrated in the Meyer-Neldel rule, was increased because more activated sites became available for Li.sup.+ to visit (
[0148] To study ion dynamics on a different time-scale, the real part of resistivity (ρ′=M″/ω) as a function of temperature was examined. As seen at
[0149] This feature resembled the NMR T.sub.1 relaxation rate, which permitted the ion dynamics on different length scale, i.e., short-range vs. long-range, to be probed. To characterize ion dynamics on both scales with activation energy, ρ′-peaks (1 MHz) of all Li.sub.3PS.sub.4-xO.sub.x (x=0, 0.1, 0.25, 0.31, 0.5, and 1) were collectively compared. As displayed at
[0150] The overall evolution of Li-ion conduction in Li.sub.3PS.sub.4-xO.sub.x (x=0, 0.1, 0.25, 0.31, 0.5, and 1) is summarized at
[0151] 1) The change in the characteristic temperature, T.sub.max,ρ′, shared a similar pattern with the E.sub.a,DC but related to σ.sub.DC with an opposite fashion. All these physical parameters showed that Li.sub.3PS.sub.3.69O.sub.0.1 possessed the highest Li-ion conduction, which was in accordance with the Meyer-Neldel rule 2) Both the pre-factors (v.sub.ρ′0 and ρ.sub.0) experienced a similar dependence on temperature, in which the smallest value of the pre-factors was found as in the case of the activation energies (E.sub.a,DC and E.sub.a,ρ′). Consequently, the balanced factors in Li.sub.3PS.sub.3.69O.sub.0.31 lead to the optimal performance as revealed by EIS. 3) short-range and long-range experimentally determined energy barriers aligned well with that from simulations and showed that a low long-range energy barrier appeared to be important for obtaining high overall conductivity.
[0152] Also analyzed was the Li-A (A=O, S) bonding characteristics in order to investigate the origin of the tunable Li-diffusion path after oxygenation.
[0153] How the Li-ion number density surrounding S and O within the 1.sup.st coordination sphere evolved are shown in at
[0154] To isolate the effect of relative position of O-content for the chemical stoichiometry, x=1, two structural configurations of Li.sub.3PS.sub.3O: (i) Dispersed: PS.sub.3O units (ii) Localized: both PS.sub.4 and PS.sub.2O.sub.2 units were examined. Specifically, Li-distribution in Li.sub.3PS.sub.3O with two different O-distribution patterns: localized and dispersed O-atoms containing PS.sub.2O.sub.2 and PS.sub.3O moiety, respectively, at a particular oxygen concentration, x=1. The Li chemical environment (
TABLE-US-00005 Calculated NMR shift for Li.sub.48P.sub.16S.sub.48O.sub.16 (localized) and Li.sub.12P.sub.4S.sub.12O.sub.4 (dispersed). The experimental NMR results support that the dispersed structure was synthesized. Relative Composition Ion Span Skew Chemical Shift Li.sub.48P.sub.16S.sub.48O.sub.16; x = 1 Li 6.91 −0.45 −0.34 Li 7.85 −0.05 −0.08 Li 6.77 −0.25 1.48 Li 7.85 −0.05 −0.08 P 80.47 0.44 75.12 Li.sub.12P.sub.4S.sub.12O.sub.4; x = 1 Li 5.99 −0.06 0.32 Li 7.39 0.18 1.79 Li 7.69 0.56 0.83 Li 3.33 −0.04 1.01 P 48.09 0.8 43.47 P 116.64 0.66 86.27
[0155] Dispersed O-arrangement exhibited more downfield Li-chemical shift compared to the localized O-arrangement, associated with a much lower Li-migration barrier for the former, 0.31±0.02 meV versus 0.46±0.03 meV (
[0156] Thus, varying oxygen concentration tuned the Li-ion redistribution surrounding S and O, leading to maximum or increased widening of the Li-diffusion channel at a critical composition of Li.sub.3PS.sub.3.75O.sub.0.25. Criticality arose because for sufficiently low oxygen concentration (0≤x≤0.25 in Li.sub.3PS.sub.4-xO.sub.x) oxygenated thiophosphates motifs were well dispersed, which in combination with inhomogeneous Li-distribution surrounding S and O resulted in a gradual increase in the free volume. However, further increase in the O-content resulted in close proximity of the O-domains and overall shrinkage of the lattice (hence channel width) due to shorter Li-O bonds which attributed to sluggish Li-diffusion.