Lithium-ion batteries (LIBs) have become an integral part of numerous products, such as laptops, smartphones, electric vehicles, etc. However, a safety concern of commercial LIBs stems from the use of flammable organic electrolytes. To overcome this, solid electrolytes (SEs) have been studied. However, their commercialization has been hindered for one or more reasons, such as their low ionic conductivity and poor electrochemical stability against metallic Li and the open atmosphere.
With respect to stability against O2, H2O, and Li, oxide SEs, such as Li7La3Zr2O12, have been studied, but their commercialization has been impeded by high heating temperatures, large interfacial resistance, and/or low room temperature ionic conductivity, σRT, (≤1×10−3 S/cm). With respect to ionic conductivity, sulfide SEs show great promise.
The Li10GeP2S12 (LGPS) and argyrodite structural families represent some of the ionic conductors that have been reported, with ionic conductivities of>1×10−2 S/cm (see, e.g., Y. Kato, et al. Nat. Energy 2016, 1, 16030; M. A. Kraft, et al. J. Am. Chem. Soc. 2018, 140, 16330-16339; and N. Kamaya, et al., Nat. Mater. 2011, 10, 682). Disadvantages of these SEs include the high cost of Ge and its undesirable reduction-oxidation processes against Li during cycling.
Li3PS4 has attracted attention because of its stability against lithium and low cost (Y. Yang, et al. ACS Appl. Mater. Interfaces 2016, 8, 25229-25242), however, the increased stability comes with the disadvantage of a significant decrease in ionic conductivity (σ=10−7 S/cm)(see, e.g., K. Homma, et al. Solid State Ionics 2011, 182, 53-58; M. Tachez, et al. Solid State Ionics 1984, 14, 181-185). One cause of this may be the instability of its high ionic conducting β-phase, which may convert to β-Li3PS4 at room temperature. To stabilize β-Li3PS4 at room temperature and therefore increase the ionic conductivity, nanoporous β-Li3PS4 synthesized via thermal treatment of Li3PS4⋅3THF (tetrahydrofuran) has shown some success (σ25° C.=1.6×10−4 S/cm) (see, e.g., Z. Liu, et al. J. Am. Chem. Soc. 2013, 135, 975-978). This may be a result of an increase in surface energy from the nanoporous structure, which may cause a distortion in the lattice and therefore lower the temperature at which the phase transition occurs. Wet-chemical synthesis methods using THF, 1H, 6,7Li, and 31P solid-state nuclear magnetic resonance spectroscopy (NMR) have been utilized to identify the local structure (M. Gobet, et al. Chem. Mater. 2014, 26, 3558-3564). The decomposition of THF may cause a small amount of S—O exchange, resulting in a 31P resonance shift at 83.9 ppm, which is assigned to a glassy phase of both monomeric (PS4)3 and (PS3O)3 units.
Computational and experimental studies have explored the use of oxysulfides to combine the desirable electrochemical properties of oxide and sulfide materials individually. Recent experimental support of enhancements has been reported on Li10SiP2S12-xOx, showing an increase in ionic conductivity when x=0.7 and that a crystalline PS4-xOx unit is generated from the β-Li3PS4 impurity (K. -H. Kim, et al. Chem. Mater. 2019, 31, 3984-3991).
In Li3PS4-xOx, O has a smaller radius and greater electronegativity than S, making the P—O bond shorter in length than P—S bonds. Therefore, according to computational studies, the O ion can create an empty region near itself for Li-ions to move efficiently through (X. Wang, et al. Phys. Chem. Chem. Phys. 2016, 18, 21269-21277). Specifically, oxygen substitution may permit the connection of 2D channels, which generate a 3D Li-ion transport pathway by joining the 8d and 4b sites.
For sulfides, and their corresponding oxygenated phases, the method of synthesis may have an impact on the resulting material's overall electrochemical properties. High temperature, highly conducting metastable phases, which are stable at room temperature, can be beneficial to electrochemical performance. They also can be acquired using a quench method, however, this requires heating temperatures of >900° C. to synthesize Li3PS4 (K. Takada, et al. Solid State Ionics 2005, 176, 2355-2359).
Another possible technique is high-energy ball milling (see, e.g., T. Famprikis et al. Nat. Mater. 2019, 18, 1278-1291; A. Düvel, et al. J. Phys. Chem. C 2011, 115, 23784-23789; and K. Kanazawa et al. Inorg. Chem. 2018, 57, 9925-9930), which can access high temperature metastable phases in a manner similar to quenching. Kinetic energy of zirconia balls that collide with the chemical precursors may cause rapid heating and cooling, therefore yielding a glass with a “frozen” high-temperature atomic configuration. This may result in a metastable phase that can be crystallized from the glass matrix, usually from optimized thermal treatment, which typically gives a glass-ceramic material.
There remains a need for improved solid electrolytes, lithium-ion batteries that include solid electrolytes, and methods for producing solid electrolytes, including solid electrolytes having improved conductivity, stability, and safety when used in lithium-ion batteries.
Provided herein are electrolytes, such as solid electrolytes, lithium-ion batteries, and methods for producing solid electrolytes that overcome one or more of the foregoing disadvantages. The electrolytes provided herein, which may include glass-ceramic electrolytes, may have improved activation energies, conductivities, stability, or a combination thereof.
In one aspect, electrolytes are provided. The electrolytes may be solid electrolytes. The electrolytes may be glass-ceramic electrolytes. In some embodiments, the electrolytes include a material of formula (I): Li3PS4-xOx, wherein x is 0<x≤1.
In another aspect, lithium-ion batteries are provided. In some embodiments, the lithium-ion batteries include an electrolyte described herein, such as an electrolyte comprising a composition of formula (I).
In yet another aspect, methods of forming electrolytes are provided. In some embodiments, the methods of forming the electrolytes include contacting Li2S, P2S5, and P2O5 to form the electrolytes. The contacting of Li2S, P2S5, and P2O5 may include (i) mixing Li2S, P2S5, and P2O5, (ii) homogenizing Li2S, P2S5, and P2O5 under vacuum, or (iii) a combination thereof.
Additional aspects will be set forth in part in the description which follows, and in part will be obvious from the description, or may be learned by practice of the aspects described herein. The advantages described herein may be realized and attained by means of the elements and combinations particularly pointed out in the appended claims. It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are not restrictive.
Provided herein are electrolytes, batteries, and methods for making electrolytes, such as the electrolytes described herein.
In some embodiments, the electrolytes provided herein include a material of formula (I):
Li3PS4-xOx formula (I);
wherein x is 0<x≤1.
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.
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.
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.
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.
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.
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.
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.
In some embodiments, the electrolyte consists of a material of formula (I).
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/cm3 to about 3 g/cm3, about 1.5 g/cm3 to about 2.5 g/cm3, or about 1.5 g/cm3 to about 2 g/cm3.
In some embodiments, x is greater than 0, and the electrolye has an activation energy that is less than an activation energy of β-Li3PS4. 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-Li3PS4.
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-Li3PS4.
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.
Also provided herein are methods of forming electrolytes. In some embodiments, the methods include contacting Li2S, P2S5, and P2O5 to form an electrolyte. When the methods are used to produce electrolytes that include a composition of formula (I), the ratios of Li2S, P2S5, and P2O5 that are contacted may be selected to achieve a desired value for “x” of formula (I).
The Li2S, P2S5, and P2O5 may be contacted using any known technique. In some embodiments, the contacting of Li2S, P2S5, and P2O5 includes (i) mixing Li2S, P2S5, and P2O5, (ii) homogenizing Li2S, P2S5, and P2O5 under vacuum, or (iii) a combination thereof.
The homogenizing of Li2S, P2S5, and P2O5 under vacuum may include milling Li2S, P2S5, and P2O5 with a milling media, wherein a weight ratio of the milling media to the total weight of Li2S, P2S5, and P2O5 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.
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.
The following listing provides non-limiting embodiments of the electrolytes, batteries, and methods provided herein:
An electrolyte comprising a material of formula (I):
Li3PS4-xOx formula (I);
wherein x is 0<x≤1.
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.
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.
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.
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.
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.
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.
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.
The electrolyte of any one of Embodiments 1 to 8, wherein the electrolyte consists of the material of formula (I).
The electrolyte of any one of Embodiments 1 to 9, wherein the electrolyte is a solid electrolyte.
The electrolyte of Embodiment 10, wherein the solid electrolyte is a glass-ceramic electrolyte.
The electrolyte of Embodiment 10 or 11, wherein the electrolye is in the form of a powder.
The electrolyte of any of Embodiments 1 to 12, wherein the electrolye is in the form of a pellet.
The electrolyte of Embodiment 13, wherein the pellet has a density of about 1 g/cm3 to about 3 g/cm3, about 1.5 g/cm3 to about 2.5 g/cm3, or about 1.5 g/cm3 to about 2 g/cm3.
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-Li3PS4.
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-Li3PS4.
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-Li3PS4.
A battery including an electrolyte of any of Embodiments 1 to 17.
The battery of Embodiment 18, wherein the battery is a lithium-ion battery.
A method forming an electrolyte, such as an electrolyte of any of Embodiments 1 to 17, wherein the method includes contacting Li2S, P2S5, and P2O5 to form the electrolyte.
The method of Embodiment 20, wherein the contacting of Li2S, P2S5, and P2O5 comprises (i) mixing Li2S, P2S5, and P2O5, (ii) homogenizing Li2S, P2S5, and P2O5 under vacuum, or (iii) a combination thereof.
The method of Embodiment 20 or 21, wherein the homogenizing of Li2S, P2S5, and P2O5 under vacuum comprises milling Li2S, P2S5, and P2O5 with a milling media.
The method of Embodiment 22, wherein a weight ratio of the milling media to the total weight of Li2S, P2S5, and P2O5 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.
The method of any of Embodiments 20 to 23, wherein the method further comprises pressing the electrolyte into a pellet.
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.
The method of Embodiment 25, wherein the electrolyte is subjected to the pressure and the temperature simultaneously, sequentially, or a combination thereof.
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.
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.
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.
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.
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.
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.
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/cm3 to about 2 g/cm3. This range should be interpreted as encompassing about 1.5 g/cm3 to about 2 g/cm3, and further encompasses “about” each of 1.6 g/cm3, 1.7 g/cm3, 1.8 g/cm3, and 1.9 g/cm3, including any ranges and sub-ranges between any of these values.
As used herein, the term “about” means plus or minus 10% of the numerical value of the number with which it is being used.
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.
This example provides a solid-state synthesis of Li3PS4-xOx, wherein x=0.31, which yielded a sevenfold increase in ionic conductivity and a lower activation energy compared to experimental β-Li3PS4. Detailed variable temperature electrochemical impedance spectroscopy (EIS) analysis was implemented to probe the short-range and long-range Li-ion motion and Arrhenius prefactor.
In addition, the Jonscher-type power law exponent was computed to confirm the enhanced dimensionality of Li-ion motion in Li3PS4-xOx compared to the experimental β-Li3PS4. Li3PS4-xOx were investigated using PXRD to confirm the β-Li3PS4 phase at room temperature in addition to 6Li and 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.
In this example, Li3PS369O0.31 was synthesized, and the Li3PS369O0.31 had an ionic conductivity of 1.38 mS/cm at 25° C., which was 7 times greater than that of pristine β-Li3PS4.
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 (PS3xOx)3− unit.
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.
All chemicals were used as received. Stoichiometric amounts of Li2S (Alfa Aesar, 99.9%), P2S5 (Sigma-Aldrich, 99.9%), and P2O5 (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; ∅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/cm3. Sample handling and heat treatment were all performed under Ar (H2O<1 ppm and O2<1 ppm) in glovebox.
Materials Characterization. Impedance measurements on Li3PS4-xOx 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.
All the measurements were performed in a Cincinnati Sub-Zero Temperature Chamber under dry air atmosphere to prevent H2O contamination. PXRD measurements were conducted with a PANalytical X′Pert Pro-MPD Powder Diffractometer with Cu-Kα radiation. KAPTON® film was employed to reduce reactions of Li3PS4-xOx with moist air. MAS NMR measurements on Li3PS4-xOx were performed on a Bruker Avance III 500 MHz NMR spectrometer with a spinning rate of 25 kHz at room temperature. 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 6Li (Larmor frequency=73.58 MHz) NMR spectra using a recycle delay of 200 s). 7Li spin-lattice relaxation time was performed using an inversion recovery pulse sequence. 6Li and 31P chemical shift were referenced to solid LiCl (−1.1 ppm) and to 85% H3PO4 (0 ppm), respectively.
The structure of β-Li3PS4 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 Li3PS4 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 6/7Li (+90.5 ppm) and 31P (+254 ppm) were estimated from the difference between experimental and calculated isoshift of pristine β-Li3PS4. 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:
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+ ion exchange reduced line width of NMR peaks.
The broadening in diffraction peaks with low intensity indicated that Li3PS4-xOx was glass-ceramic. When x was higher than 0.31 in Li3PS4-xOx, 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 Li3PS4-xOx could be explained by the enthalpy of mixing, ΔHmix calculations. As shown in
To understand the structural evolution of local environment due to oxygen substitution in Li3PS4-xOx, 6Li and 31P solid-state NMR was employed. As shown at
Since there was a large loss of crystallinity for higher oxygenated samples, deconvolution was only performed on Li3PS4, Li3PS3.9O0.1, Li3PS3.75O0.25, and Li3P3.69O0.31 as shown at
For Li3PS4, 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.
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 6Li integral % of the combined Li ½ assignment increased with a maximum for Li3P3.69O0.31. A decrease in the 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 6Li chemical shifts were simulated using perturbation theory for Li3PS4, Li3PS3.875O0.125, and Li3PS3.75O0.25 from DFT optimized structures of the same composition (
To study the change in Li-ion mobility upon oxygen substitution, 7Li spin-lattice relaxation time, T1, for Li3PS4, Li3PS3.9O0.1, Li3PS3.75O0.25, and Li3P3.69O0.31 was performed as depicted at
The local environment of the anionic sublattice in Li3PS4-xOx was investigated with 31P NMR and the results are shown at
The 31P resonances at 88 ppm and at 93 ppm were assigned to the (γ-PS4)3− unit and the (P2S7)4− unit, respectively. Li3P3.69O0.31 showed a minimum 31P integral % of the (γ-PS4)3 unit and a maximum for that of the (P2S7)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 (POS2)− (PS2O2)3−, (PSO3)3−, (PO4)3− and (P2O7)4−, respectively, as seen in
To relate the structure of Li3PS4-xOx to the electrochemical performance, EIS was performed. The conductivity isotherms of Li3PS3.69O0.31 are shown at
For the conductivity isotherms of Li3PS4-xOx (x=0, 0.1, 0.25, 0.31, 0.5, and 1;
The obtained σDC of Li3PS3.69O0.31 reached a maximum of 1.38 mS/cm, giving greater than a sevenfold enhancement in ionic conductivity compared to the experimental Li3PS4, which had a σDC of 0.19 mS/cm. Substituting O for S with x>0.31 in Li3PS4-xOx lead to a reduction of ionic conductivity (see table below). The energy barrier of aDc could be quantified with Ea,DC using the Arrhenius law, σDCT=σ0 exp(−Ea,DC/(kBT)), where T is temperature in kelvin, σ0 is the Arrhenius pre-factor, and kB is the Boltzmann constant. As illustrated at
To better understand the EIS results, AIMD simulations were carried out at 600-1300 K for Li3PS4-xOx: x=0.0, 0.125, 0.25, and 1.0. With O2− doping, Li+ conductivity increased substantially. Optimal Oxygen concentration (x=0.25) lead to the highest conductivity and least Li-migration barrier (Ea). 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.
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
Li probability density was plotted for three compositions of x in Li3PS4-xOx, 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, Li3PS3O, localized Li-hopping occurred with interrupted long-range diffusion. This coincided well with the experimental power law exponent measurements as discussed above.
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, Li3PS3O, despite the higher dimensionality.
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 Li3PS4-xOx (0x (
This suggested a change in dimensionality of Li-ion conduction from 2D (Li3PS4; n=0.62) to 3D (Li3PS3.69O0.31; n=0.87). The improved dimensionality of conducting space was attributed to greater correlated ion motion.
This explained the lowering in ionic conductivity for Li3PS3.5O0.5 and Li3PS3O 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+—Li+ and the Li+—O2− pairs may have caused a rise in the backward hopping rate, that is, an unsuccessful hopping for Li+ to jump through the potential minima.
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 Li3PS3.69O0.31 as an example (
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 ωmax was identified on each isotherm to calculate the electrical relaxation rate, τM″−1 (⋅max/2π=fmax=τM″−1). As the temperature increased, the ωmax shifts to higher frequency; therefore, faster relaxation. Then, the activation energy Ea,M″ (
The pre-factor could be understood according to the following equation:
Where z was the geometric factor, kB was the Boltzmann constant, N was the number of charge carriers, q was the charge of the ions, ΔSm was the migration entropy, a was the jump distance between sites, and v0 was the jump frequency. The number of charge carriers was not expected to largely contribute to the change in σ0, 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, ωc, was calculated according to:
The crossover frequency, where the transition from the σDC plateau to the high-frequency dispersive region occurred, was used as an rough approximation for v0. The results given in
From this, the change in jump frequency was not expected to contribute largely to the change in σ0 either, otherwise the trend would have followed that of the Arrhenius prefactor. Moreover, the migration entropy (ΔSm), as illustrated in the Meyer-Neldel rule, was increased because more activated sites became available for Li+ to visit (
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
This feature resembled the NMR T1 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 Li3PS4-xOx (x=0, 0.1, 0.25, 0.31, 0.5, and 1) were collectively compared. As displayed at
The overall evolution of Li-ion conduction in Li3PS4-xOx (x=0, 0.1, 0.25, 0.31, 0.5, and 1) is summarized at
1) The change in the characteristic temperature, Tmax,ρ′, shared a similar pattern with the Ea,DC but related to σDC with an opposite fashion. All these physical parameters showed that Li3PS3.69O0.1 possessed the highest Li-ion conduction, which was in accordance with the Meyer-Neldel rule 2) Both the pre-factors (vρ′0 and ρ0) 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 (Ea,DC and Ea,ρ′). Consequently, the balanced factors in Li3PS3.69O0.31 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.
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.
How the Li-ion number density surrounding S and O within the 1st coordination sphere evolved are shown in at
To isolate the effect of relative position of O-content for the chemical stoichiometry, x=1, two structural configurations of Li3PS3O: (i) Dispersed: PS3O units (ii) Localized: both PS4 and PS2O2 units were examined. Specifically, Li-distribution in Li3PS3O with two different O-distribution patterns: localized and dispersed O-atoms containing PS2O2 and PS3O moiety, respectively, at a particular oxygen concentration, x=1. The Li chemical environment (
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 (
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 Li3PS3.75O0.25. Criticality arose because for sufficiently low oxygen concentration (0≤x≤0.25 in Li3PS4-xOx) 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.
This application claims priority to U.S. patent application Ser. No. 63/149,818, filed Feb. 16, 2021, which is incorporated herein by reference.
This invention was made with government support under grant no. DMR-1847038 awarded by the National Science Foundation. The government has certain rights in this invention.
Number | Date | Country | |
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63149818 | Feb 2021 | US |