Molten inorganic electrolytes for low temperature sodium batteries

Abstract

A molten sodium-based battery comprises a robust, highly Na-ion conductive, zero-crossover separator and a fully inorganic, fully liquid, highly cyclable molten cathode that operates at low temperatures.

Claims

1. An inorganic molten salt catholyte for electrochemical energy storage, comprising at least one sodium halide of the formula NaF, NaCl, NaBr, or Nal mixed with at least one gallium halide and at least one aluminum halide of the formula AlC1.sub.3, AlBr.sub.3, or AlI.sub.3, wherein the inorganic molten salt catholyte comprises between 5 and 25 mol % sodium halide and wherein the inorganic molten salt catholyte is fully liquid at a temperature less than 120° C.

2. The inorganic molten salt catholyte of claim 1, wherein the inorganic molten salt catholyte comprises NaI and GaCl.sub.3.

3. The inorganic molten salt catholyte of claim 1, wherein the inorganic molten salt catholyte comprises a binary, ternary, or quaternary mixture of the at least one sodium halide and the at least one metal halide salt.

4. The inorganic molten salt catholyte of claim 1, wherein the inorganic molten salt catholyte is fully liquid at a temperature less than 100° C.

5. A low temperature sodium battery, comprising: an anode current collector, a sodium-based liquid metal anode, a nonporous Na.sup.+-conducting separator, an inorganic molten salt catholyte comprising at least one sodium halide of the formula NaF, NaCl, NaBr, or NaI, mixed with at least one gallium halide and at least one aluminum halide of the formula AlCl.sub.3, AlBr.sub.3, or AlI.sub.3, wherein the mixture comprises between 5 and 25 mol % sodium halide and wherein the inorganic molten salt catholyte is fully liquid at a temperature less than 120° C., and an inert cathode current collector.

6. The low temperature sodium battery of claim 5, wherein the sodium-based liquid metal anode comprises molten sodium metal or an alloy of sodium and at least one other alkali metal.

7. The low temperature sodium battery of claim 5, wherein the nonporous Na.sup.+-conducting separator comprises NaSICON, β″-Al.sub.2O.sub.3, or a solid Na.sup.+ conductor, or a composite thereof.

8. The low temperature sodium battery of claim 7, wherein the nonporous Na.sup.+-conducting separator further comprises an inert material.

9. The low temperature sodium battery of claim 5, wherein the inorganic molten salt catholyte comprises NaI and GaCl.sub.3.

10. The low temperature sodium battery of claim 5, wherein the inorganic molten salt catholyte comprises a binary, ternary, or quaternary mixture of the at least one sodium halide and the at least one metal halide salt.

11. The low temperature sodium battery of claim 5, wherein the inorganic molten salt catholyte is fully liquid at a temperature less than 100° C.

12. The low temperature sodium battery of claim 5, wherein the inert cathode current collector comprises graphite, carbon felt, or a carbon powder.

13. The inorganic molten salt catholyte, further comprising at least one metal halide salt of the formula MX.sub.y, where M=Mg, Ca, Sr, Ba, Nb, Ta, Mo, W, In, Sn, Sb, or Bi, and X=F, Cl, Br, or I; and y is the number of halogen atoms in the metal halide salt.

14. The low temperature sodium battery of claim 5, wherein the inorganic molten salt catholyte further comprises at least one metal halide salt of the formula MX.sub.y, where M=Mg, Ca, Sr, Ba, Nb, Ta, Mo, W, In, Sn, Sb, or Bi, and X=F, CI, Br, or I; and y is the number of halogen atoms in the metal halide salt.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The detailed description will refer to the following drawings, wherein like elements are referred to by like numbers.

(2) FIG. 1 is a schematic illustration of an exemplary molten sodium halide battery, with anode and cathode reactions and their standard state potentials.

(3) FIGS. 2A-2B are photographs of different molten salts at 90° C. The molten salts are composed of 25 mol % NaI and 75 mol % AlCl.sub.3 or GaCl.sub.3, respectively. The photograph in FIG. 2A shows that a AlCl.sub.3 composition is still solid at 90° C. FIG. 2B shows that GaCl.sub.3 salts are fully molten at 90° C.

(4) FIG. 3 is a cyclic voltammogram from a carbon fiber microelectrode showing the oxidation of iodide starting at 3.6 V (versus a Na/Na.sup.+ reference) in the 25 mol % NaI 75 mol % GaCl.sub.3 molten salt. Scan rate was 100 mV/s and the temperature was 90° C.

DETAILED DESCRIPTION OF THE INVENTION

(5) A schematic illustration of a molten sodium halide battery is shown in FIG. 1. The low temperature, inorganic molten sodium battery comprises a sodium-based liquid metal anode, a nonporous Na.sup.+ conducting separator, an inorganic molten salt catholyte, and anode and cathode current collectors. Unlike previous sodium batteries which operate at a minimum of 120° C., and more practically 200° C., the present invention provides a molten sodium battery that can operate at <100° C. with fully inorganic active components.

(6) The sodium-based liquid metal anode can comprise pure molten sodium metal or an alloy of sodium and other alkali metal(s), such as potassium or cesium. Other alloying metals, such as zinc, indium, or antimony, which reduce the melting temperature of the sodium alloy, can also be used. Liquid sodium is a preferable anode material, due to its high energy density, electrochemical reversibility, high electrical conductivity (10.sup.5 S/cm), low melting point (98° C.), and earth abundance. See S. Ha et al., ChemPhysChem 15, 1971 (2014); K. Hueso et al., Energy Environ. Sci. 6, 734 (2013); W.-L. Pang et al., J. Power Sources 356, 80 (2017); and F. Wan et al., Nano Energy 13, 450 (2015). Moreover, liquid metal anodes can avoid dendrite growth issues that plague solid zinc and lithium metal anodes. See X. Lu et al., Nat. Commun. 5, 4578 (2014).

(7) The separator electrically isolates the two electrolytes (anode and cathode) and allows conduction of inert salt ions to maintain charge balance across the two electrolytes. Preferably, a zero-crossover separator selectively favors transport of the desired charge carrier, Na.sup.+, and prevents transport of redox-active molecules and solvents that can contribute to capacity loss. The nonporous Na.sup.+-conducting separator can comprise NaSICON (nominally Na.sub.1+xZr.sub.2Si.sub.xP.sub.3-xO.sub.12), β″-Al.sub.2O.sub.3, other solid Na.sup.+ conductors, or a composite of these conductors and an inert component. In particular, NaSICON retains significant conductivity at temperatures <200° C. and is a mechanically robust ceramic separator that is stable against liquid sodium. See A. Jolley et al., Ionics 21, 3031 (2015); A. Jolley et al., J. Amer. Ceram. Soc. 98, 2902 (2015); X. Lu et al., J. Power Sources 195, 2431 (2010); X. Lu et al., J. Power Sources 215, 288 (2012); and J. Kim et al., J. Electroanal. Chem. 759, 201 (2015).

(8) The fully liquid, molten salt cathode can comprise NaF, NaCl, NaBr, or NaI mixed with a metal halide salt of the formula MX.sub.y, where M is an alkaline earth metal, such as Mg, Ca, Sr, or Ba; an early transition metal, such as Nb, Ta, Mo, or W.sup.−; or a post-transition metal, such as Ga, In, Sn, Sb, or Bi; and X is a halogen, such as F, Cl, Br, or I; and y is the number of halogen atoms in the compound, that provides a low melting temperature (e.g., <100° C.). The molten salt catholyte can comprise binary, ternary or quaternary mixtures of the above compounds. The molten salt catholyte can further comprise mixtures of these compounds with an aluminum halide, such as AlCl.sub.3, AlBr.sub.3, or AlI.sub.3. The molten salt catholyte preferably comprises a mixture of a sodium halide and a gallium halide. Any of the other metal halides can be added to the sodium halide/gallium halide mixture in relatively small amounts to help depress melting point or improve conductivity of the mixture. The mixture preferably comprises between 5 and 25 mol % sodium halide.

(9) As an example, the catholyte can make use of the reversible iodide/triiodide redox couple to store and release charge and which has been shown to have a high energy density. See Y. Zhao et al., Nat. Commun. 4, 1896 (2013). Upon charging, Na.sup.+ is drawn from the molten salt cathode through the separator and reduced onto the molten sodium-based anode, while (for NaI-containing salts) a I.sup.−-containing complex is oxidized via two-electron transfer to I.sub.3.sup.− in the molten salt cathode. When discharging, Na.sup.0 from the molten anode is oxidized to Na.sup.+ and transported through the separator into the molten salt cathode, while I.sub.3.sup.− in the catholyte is reduced to I.sup.− at the cathode current collector, as shown in FIG. 1. Depending on the chosen chemistry and operating temperature, operating voltages of 2.8-3.6 V are expected. See A. Bard and L. Faulkner, Electrochemical Methods: Fundamentals and Applications, second. Ed., Wiley (2000). This chemistry is unique from other sodium batteries which leverage inorganic molten salts, such as ZEBRA-style batteries, in that the current collector does not react with the catholyte. Instead the cathode current collector merely oxidizes or reduces the catholyte during charging and discharging (i.e., extracts electrons from the fully liquid catholyte during charging and injects electrons into the catholyte during discharging). Thus, inert solid materials such as tungsten or graphite can be used for the cathode current collector, while electroactive materials such as Fe, Zn, or Ni can be avoided.

(10) As examples of the invention, several combinations of NaI with GaCl.sub.3 were tested. 25 mol % NaI with 75 mol % GaCl.sub.3 is fully molten at 90° C. The NaI—GaCl.sub.3 system has a fully molten capacity range of at least 5 to 25 mol % NaI. A photograph of this molten salt at 90° C. is shown in FIG. 2B and compared to a solid NaI—AlCl.sub.3 salt in FIG. 2A used in a previously demonstrated inorganic sodium battery that requires temperatures >120° C. for successful operation. In the NaI—AlCl.sub.3 system, it was found that the presence of material phases other than the molten salt liquid, especially near the electrode in the diffusion layer of the reactant, can significantly hinder mass and charge transport phenomena critical to optimal battery performance during cycling. These detrimental secondary phases can include gas phases or solid salt particle phases. In particular, if there are undissolved solids present in the liquid melt, they can impede or block reactant diffusion to the electrode surface and lock up a significant portion of the reactant, preventing its electrochemical utilization and lowering overall battery capacity. See L. J. Small et al., J. Power Sources 360, 569 (2017); and S. J. Percival et al., J. Electrochem. Soc. 165(14), A3531 (2018). The specific electrolyte compositions of the present invention enable significantly lower temperature sodium battery operation. In particular, a fully molten catholyte avoids the particle-hindered electrochemical processes and particle-related loss of capacity observed with the NaI—AlCl.sub.3 system.

(11) Electrochemical characterization for a 25 mol % NaI with 75 mol % GaCl.sub.3 salt at 90° C. was performed using cyclic voltammetry, as plotted in FIG. 3. The NaI—GaCl.sub.3 system shows good iodide electrochemical behavior. The oxidation of I.sup.− to I.sub.3.sup.− (charging) is seen above 3.6 V (versus a Na/Na.sup.+ reference). The reduction of Ga.sup.3+ to Ga.sup.0 is observed at 2.6 V (not shown). Thus, 1.0 V of overpotential is available in the catholyte during I.sub.3.sup.− reduction (discharge) without harming the cathode or reducing gallium from the electrolyte.

(12) This invention improves on three key weakness of commercial batteries: cost, safety, and lifetime. Cost is greatly reduced by using sodium, instead of lithium used in industry-standard lithium-ion batteries. While systems such as sodium-sulfur have even lower materials costs, due to the lower cost of S vs. I.sub.2, these systems operate near 300° C. and require extensive thermal management, and expensive hermetic sealing technologies. The low temperature operation of the molten sodium battery enables lower material and processing costs, reduced operation costs, and simplified heat management.

(13) The safety of these batteries is attributed to the use of fully inorganic active components. Upon simulated internal discharge of a higher operating temperature GaCl.sub.3—NaI cathode, only aluminum metal and a harmless sodium halide salt (e.g. NaCl) was formed, along with minimal heat and no recordable gas evolution. Thus, these fully inorganic active components eliminate concerns of explosion from buildup of flammable gases and the creation of a thermal runaway event. With improved safety, larger cells necessary for grid-scale storage can be fabricated, enabling further cost reductions and increasing ease of cell-level integrated power management.

(14) Finally, the low temperature molten sodium battery offers improved lifetime, due to reduced material degradation, decreased reagent volatility, and fewer side reactions. The use of fully liquid reactions precludes dendrite formation in the anode and eliminates plating or intercalation reactions in the cathode. Elimination of these failure mechanisms, common in Li-ion and Zn—MnO.sub.2 batteries, is expected to lengthen Na battery lifetime beyond 10,000 cycles and drive down the levelized cost of operation. Such long cycle life is necessary for reliable grid scale storage applications.

(15) The present invention has been described as a molten salt electrolyte for a low temperature sodium battery. It will be understood that the above description is merely illustrative of the applications of the principles of the present invention, the scope of which is to be determined by the claims viewed in light of the specification. Other variants and modifications of the invention will be apparent to those of skill in the art.