COMPOSITE ELECTRODE MATERIALS FOR FLUORIDE-ION ELECTROCHEMICAL CELLS

Abstract

The present disclosure relates to a method of making core-shell and yolk-shell nanoparticles, and to electrodes comprising the same. The core-shell and yolk-shell nanoparticles and electrodes comprising them are suitable for use in electrochemical cells, such as fluoride shuttle batteries. The shell may protect the metal core from oxidation, including in an electrochemical cell. In some embodiments, an electrochemically active structure includes a dimensionally changeable active material forming a particle that expands or contracts upon reaction with or release of fluoride ions. One or more particles are at least partially surrounded with a fluoride-conducting encapsulant and optionally one or more voids are formed between the active material and the encapsulant using sacrificial layers or selective etching. When the electrochemically active structures are used in secondary batteries, the presence of voids can accommodate dimensional changes of the active material.

Description

TECHNICAL FIELD

The present disclosure relates to electrochemically active materials, and more particularly to fluoride ion battery systems that include electrode materials with tailored structures and compositions to improve batter performance. More specifically, this disclosure relates to core-shell nanoparticles, methods for making the same, and use of the same in electrochemical cells.

BACKGROUND

Metal nanoparticles are highly desirable for use in a number of applications including as catalysts, and as electrode materials for batteries. However, the use of metal nanoparticles may be limited by the system operating conditions or other factors. For example, fluoride shuttle batteries are of growing interest as an alternative to lithium-ion batteries. However, the materials available for use in fluoride shuttle battery systems are limited, due in part to operating conditions that are detrimental to many materials that could otherwise be included in the fluoride shuttle battery electrodes.

Fluoride-ion batteries are electrochemical cells that operate via fluoride-mediated electrode reactions (i.e. accommodation or release of fluoride ions at the electrode upon charge or discharge, often through a conversion-type reaction). Such electrochemical cells can offer greater energy density, lower cost and/or improved safety characteristics compared to lithium and lithium-ion batteries. Fluoride-ion systems have been demonstrated in the solid state, for example, in U.S. Pat. No. 7,722,993 to Potanin, which describes an embodiment of a secondary electrochemical cell where fluoride ions are reversibly exchanged between anode and cathode during charge-discharge cycles, with these electrodes in contact with a solid-state fluoride-conducting electrolyte. Potanin describes solid state electrolytes containing fluorides of La, Ce or the compound fluorides based on them, together with an alloying additives, such as fluoride/fluorides of alkaline-earth metals (CaF₂, SrF2, BaF2) and/or fluorides of alkaline metals (LiF, KF, NaF) and/or alkaline metal chlorides (LiCl, KCl, NaCl), as well as a wide range of other compound fluorides. However, such electrochemical cells operate usefully only above room temperature (e.g. 150° C.) due to the limited conductivity of the solid-state electrolyte.

Attempts have also been made to provide fluoride ion-based electrochemical systems capable of using liquid electrolytes. For example, US 2011-0143219 A1 by Weiss et al. and U.S. Pat. No. 9,166,249 by Darolles et al. disclose fluoride-ion battery configurations selected to include a solvent-borne fluoride salt that is at least partially present in a dissolved state in the electrolyte. However, for many applications the chemical reactivity of the electrode materials with the liquid electrolyte is significant, and these liquid electrolyte systems do not provide sufficiently reliable high discharge and/or high capacity operation.

SUMMARY

The following presents a simplified summary of one or more aspects of the present disclosure in order to provide a basic understanding of such aspects. This summary is not an extensive overview of all contemplated aspects and is intended to neither identify key or critical elements of all aspects nor delineate the scope of any or all aspects. Its purpose is to present some concepts of one or more aspects in a simplified form as a prelude to the more detailed description that is presented later.

In some embodiments, the present disclosure is directed to an electrochemically active structure comprising: a core comprising an active material; and a fluoride-containing shell at least partially surrounding the active material.

In other embodiments, the present disclosure is directed to a method of making coated metal nanoparticles, the method comprising: a) providing a water/metal nanoparticle mixture; b) exposing the water/metal nanoparticle mixture to an inert atmosphere; and c) forming a fluoride-containing shell around a metal nanoparticle core.

These and other aspects of the invention will become more fully understood upon a review of the detailed description, which follows.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1A shows a cross section of a core-shell nanoparticle including a core comprising a metal nanoparticle, and a shell comprising a metal halide or a metal oxyhalide in an aspect of the present disclosure.

FIG. 1B outlines a general route to “yolk-shell” composites using a sacrificial inorganic “middle” layer.

FIG. 1C describes a route to “yolk-shell” composites using a sacrificial polymer “middle” layer.

FIG. 1D delineates an alternative route a route to “yolk-shell” composites in the absence of a sacrificial “middle” layer.

FIG. 1E depicts a variation on “sacrificial” syntheses of “yolk-shell” composites, whereby nanoparticles of the active material are grown on the surface of a “sacrificial” material

FIG. 1F outlines the growth of active material in the internal structure or pores of a preformed “sacrificial” material

FIG. 1G outlines the growth of active material in the internal structure or pores of a pre-formed “sacrificial” material where the shell constituents are chosen to be electrochemically-inactive at the electrochemical reaction potentials of interest.

FIG. 2 is a schematic illustration of a fluoride ion electrochemical cell in an aspect of the present disclosure.

FIG. 3 shows an XRD spectrum of isolated copper nanoparticles of Comparative Example 1, with no shell, immediately after synthesis and isolation (“as-made”).

FIG. 4 shows stacked XRD spectra of isolated copper nanoparticles of Comparative Example 1, with no shell, as-made and after exposure to air for 4 days and 9 days.

FIG. 5 shows an XRD spectrum of Cu-LaF₃ core-shell nanoparticles of Experimental Example 1 as synthesized in an aspect of the present disclosure.

FIG. 6 shows stacked XRD spectra of Cu-LaF₃ core-shell nanoparticles of Experimental Example 1 after exposure to air for 9, 16, and 23 days.

FIGS. 7A and 7B are transmission electron microscopy (TEM) images of Cu-LaF₃ core-shell nanoparticles of Experimental Example 1, as-made.

FIG. 8A shows a high-resolution TEM image of Cu-LaF₃ core-shell nanoparticles of Experimental Example 1, indicating the Cu (core) and LaF₃ (shell) areas. FIGS. 8B and 8C show zoomed-out images of the same nanoparticles.

FIG. 9 is a schematic of illustration of a fluoride ion electrochemical cell including the Cu-LaF₃ core-shell nanoparticle of Experimental Example 1 as an active material in the negative electrode (anode) in an aspect of the present disclosure.

FIG. 10A is a plot of voltage as a function of specific capacity for electrochemical tests of a half cell battery including the Cu-LaF₃ core-shell nanoparticle of Experimental Example 1 as an active material in an electrode in an aspect of the present disclosure.

FIG. 10B is an X-ray diffraction spectrum of the electrode of the half cell battery test of FIG. 10A, measured under initial conditions, after discharge, and after charge.

FIG. 11 shows an XRD spectrum of nanoparticles of Comparative Example 2 as synthesized.

FIG. 12 shows stacked XRD spectra of nanoparticles of Comparative Example 2 after exposure to air for 8, 15, and 22 days.

FIG. 13 is a TEM image of the nanoparticles of Comparative Example 2 showing inhomogeneous, partial coverage of copper nanoparticles with LaF₃, as well as LaF₃ that is not associated with copper nanoparticles.

FIG. 14 shows LaF₃/Cu and Cu thin-film configurations and cyclic voltammetry data.

FIG. 15A shows a cyclic voltammogram for a LaF₃/Cu double-layered thin film. FIGS. 15B and 15C show x-ray photoelectron spectroscopy (XPS) data for C, La, O, F, and Cu at various length of etching times at the voltages 1 and 2 indicated in FIG. 15A.

DETAILED DESCRIPTION

In general, the present disclosure is related to electrochemically active materials, and fluoride-ion battery systems that include electrode materials with tailored structures and compositions to improve battery performance. In some aspects, the present disclosure is related to core-shell nanoparticles, devices incorporating the core-shell nanoparticles, as well as methods of making and using the core-shell nanoparticles and devices including the core-shell nanoparticles.

Primary and secondary electrochemical cells, such as batteries, utilizing fluoride ion charge carriers, active electrode materials, and suitable liquid electrolytes can provide an alternative to conventional state of the art lithium batteries and lithium ion batteries. Such fluoride-ion battery (FIB) systems can operate usefully at room temperature while utilizing fluoride anions carried in a liquid electrolyte as at least some of the charge carriers in an electrochemical cell. The FIB system has an anode and cathode physically separated from each other, but in common contact with a fluoride ion conducting electrolyte. The anode is typically a low potential element or compound, and can be a metal, metal fluoride, or intercalating composition. Similarly, the cathode can be element or composition, and can be a metal, metal fluoride, or intercalating composition that has a higher potential than the anode. Fluoride ions (F⁻) in the fluoride conducting electrolyte go from the cathode to the anode during discharge and from the anode to the cathode during the charge of the battery:

Discharge:

Anode: MF_x+nF-→MF_x+n+ne- (Fluoride ion accommodation, oxidation)

Cathode: MF_y+ne-→MF_y−n+nF-(Fluoride ion release, reduction)

During charge, the reverse reactions occur.

For example, a FIB cell reaction based on fluoride anion transfer between Ca and Cu, both metals capable of forming metal fluorides, might be:

Discharge:

Ca+CuF₂→CaF₂+Cu

Charge:

CaF₂+Cu→Ca+CuF₂

Two major challenges exist to enable stable, reliable long-term cycling of FIB electrodes. Firstly, reversibility of the electrochemical reactions above is observed when the metal or metal fluoride active materials are nano-sized (i.e. at least one of the particle size dimensions is less than 1 μm). However, particles with such small dimensions have high surface energies and are often reactive with the electrolyte components (e.g. F⁻) to give undesirable side-reactions including “self-discharge” (i.e. a chemical reaction such as M+nF⁻MF_n that does not general electrical current). What is needed is formation of a coating, shell, layer or the like to encapsulate the active material particles while still permitting passage of F⁻ ions when desired (i.e. during electrochemical charge or discharge) The encapsulating material can also protect the active materials from such side-reactions, enabling long-term cycling stability of these electrode materials.

Secondly, such electrochemical reactions are conversion processes, with the structure of the metal or metal fluoride being broken down during the electrochemical process and reformed as the metal fluoride or metal, respectively, during the process. This conversion process results in a significant volume change between charged and discharged states of the active material, as indicated by the examples given in Table 1 below:

TABLE 1
Volume change for metal to metal fluoride conversion
			Volume Change
			During Conversion
	Metal	Metal Fluoride	M + nF− → MFn
	Fe	FeF3	311%
	Pb	PbF2	73%
	Bi	BiF3	134%
	Co	CoF3	351%
	Cu	CuF2	238%
	Sn	SnF2	113%
	La	LaF3	46%
	Ca	CaF2	−5%
	Mg	MgF2	42%
	Li	LiF	−24%

Such significant volume changes limit usefulness of conformal protective coatings encapsulating an FIB electrode material particle, since one particular state of charge will not necessarily be conformal with the particle in a different state of charge, due to the volume changes. What is needed are compositions and processes that protect the electrode active material from side reactions with the electrolyte, allow ion conduction through an encapsulant, and have sufficient void space within the encapsulant and/or encapsulant expansion/contraction properties to accommodate the volume changes of the active material during charge and discharge without permitting direct contact between the active material and the electrolyte. In some embodiments, sufficient void space may be no void space. Such compositions and their preparation are outlined below.

In some embodiments as shown in FIG. 1A, the core-shell nanoparticles include a core that comprises a metal or metal alloy (“Me”), and a shell that comprises a metal halide or a metal oxyhalide. The metal of the core may be the same as the metal of the metal halide shell. In some embodiments, the metal of the core and the metal of the metal halide or metal oxyhalide shell are different metals. The core-shell nanoparticles of the present disclosure may be incorporated into a variety of methods and applications including, but not limited to, electrodes for use in electrochemical cells, including fluoride shuttle batteries as shown in FIG. 2.

The metals or metal alloys used to form the core include, but are not limited to, iron nanoparticles, cobalt nanoparticles, nickel nanoparticles, copper nanoparticles, lead nanoparticles, and alkaline earth metal nanoparticles. In a preferred embodiment, the metal nanoparticles are selected from the group consisting of cobalt nanoparticles and copper nanoparticles. The metals used to form the core may be synthesized by mixing a metal precursor solution with a reducing agent to form metal nanoparticles.

In some embodiments, the metal nanoparticles used to form the core may be synthesized in the presence of a stabilizer that prevents or otherwise inhibits oxidation of the metal nanoparticles during synthesis, and is readily removable from the metal nanoparticles prior to formation of the metal halide or metal oxyhalide shell thereon. For example, bulky polymers such as polyvinylpyrrolidone (molecular weight of 55,000 g/mol) used during metal nanoparticle synthesis inhibit oxidation of metal nanoparticles. However, such stabilizers are not readily removable from the metal nanoparticles following synthesis.

Without being limited to any particular theory, residual stabilizer can form an additional layer between the core formed by the metal nanoparticles and the metal halide or oxyhalide shell that detracts from the performance of the core-shell nanoparticle in the desired system. For example, it is desirable to maintain the conductivity of core-shell nanoparticles used as electrode material in an F-Shuttle battery. However, core-shell materials including an additional layer of residual stabilizer between the core and the shell will likely result in an increased space between electrode materials; the additional layer of residual stabilizer and/or the resulting increased space may decrease the conductivity of the core-shell material. Without wishing to be bound to any particular theory, the additional layer of stabilizer may impede contact between the core and the shell to conduct fluoride ion, while the absence of the stabilizer may increase the likelihood of conducting fluoride ion from the core to the shell.

Therefore, a stabilizer may be used in the synthesis of the metal nanoparticles used to form the core that is readily removable therefrom to minimize the amount of stabilizer on the surface of the core prior to formation of the metal halide or metal oxyhalide shell directly thereon. In a non-limiting example, the one or more stabilizers that may be used in the synthesis of the metal nanoparticles includes a molecular weight (either individually or a weight average) of less than 1000 g/mol, optionally less than 500 g/mol, optionally less than 375 g/mol, and optionally less than 350 g/mol. Illustrative examples include hexadecyltrimethylammonium bromide (CTAB) with a molecular weight of 364 g/mol, citric acid with a molecular weight of 192 g/mol, and mixtures thereof.

In some embodiments, the shell of the core-shell nanoparticles may be formed by mixing isolated metal nanoparticles used to form the core with, for example, a metal salt solution and a halide salt solution that react to form the metal halide shell on the core. The shell is deposited directly on the metal core and may entirely surround the core as shown in FIG. 1A. In some embodiments, the metal salt used to form the shell is selected from the group consisting of alkali metal salts, alkaline earth metal salts, and transition metal salts. In certain embodiments, the metal salt used to form the shell is a transition metal salt. In certain embodiments, the metal salt used to form the shell is selected from the group consisting of lanthanum salts, cerium salts, and magnesium salts. In certain embodiments, the metal salt used to form the shell is selected from the group consisting of lanthanum salts and cerium salts. In certain embodiments, the metal salt is a lanthanum salt. In a preferred embodiment, the lanthanum salt is lanthanum nitrate. In some embodiments, the halide salt is sodium fluoride. In a non-limiting example, the shell comprises a metal fluoride or metal oxyfluoride containing material (i.e. CeF₃, CeOF, LaOF, LaF₃).

In other embodiments, the core (or electrode active material) may be separated from the shell (or encapsulant) by a void space. Compositions and processes according to such embodiments may protect the electrode active material from side reactions with the electrolyte, allow ion conduction through an encapsulant, and have sufficient void space within the encapsulant and/or encapsulant expansion/contraction properties to accommodate the volume changes of the active material during charge and discharge, without permitting direct contact between the active material and the electrolyte.

The terms core and electrode active material are used interchangeably herein. Similarly, the terms shell and encapsulant are used interchangeably herein.

In other embodiments, the present disclosure is directed to an electrode comprising the core-shell nanoparticles disclosed herein. All aspects and embodiments described with respect to the core-shell nanoparticles and methods of making thereof apply with equal force to the electrode. In a non-limiting example, the electrode is part of an F-shuttle battery system.

An “inert atmosphere” refers to a gaseous mixture that contains little or no oxygen and comprises inert or non-reactive gases or gases that have a high threshold before they react. An inert atmosphere may be, but is not limited to, molecular nitrogen or an inert gas, such as argon, or mixtures thereof.

A “reducing agent” is a substance that causes the reduction of another substance, while it itself is oxidized. Reduction refers to a gain of electron(s) by a chemical species, and oxidation refers to a loss of electron(s) by a chemical species.

A “metal salt” is an ionic complex wherein the cation(s) is(are) a positively charged metal ion(s) and the anion(s) is(are) a negatively charged ion(s). “Cation” refers to a positively charged ion, and “anion” refers to a negatively charged ion. In a “metal salt” according to the present disclosure, the anion may be any negatively charged chemical species. Metals in metal salts according to the present disclosure may include but are not limited to alkali metal salts, alkaline earth metal salts, transition metal salts, aluminum salts, or post-transition metal salts, and hydrates thereof.

“Alkali metal salts” are metal salts in which the metal ions are alkali metal ions, or metals in

Group I of the periodic table of the elements, such as lithium, sodium, potassium, rubidium, cesium, or francium.

“Alkaline earth metal salts” are metal salts in which the metal ions are alkaline earth metal ions, or metals in Group II of the periodic table of the elements, such as beryllium, magnesium, calcium, strontium, barium, or radium.

“Transition metal salts” are metal salts in which the metal ions are transition metal ions, or metals in the d-block of the periodic table of the elements, including the lanthanide and actinide series. Transition metal salts include, but are not limited to, salts of scandium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, yttrium, zirconium, niobium, molybdenum, technetium, ruthenium, rhodium, palladium, silver, cadmium, lanthanum, cerium, praseodymium, neodymium, promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, hafnium, tantalum, tungsten, rhenium, osmium, iridium, platinum, gold, mercury, actinium, thorium, protactinium, uranium, neptunium, plutonium, americium, curium, berkelium, californium, einsteinium, fermium, mendelevium, nobelium, and lawrencium.

“Post-transition metal salts” are metal salts in which the metal ions are post-transition metal ions, such as gallium, indium, tin, thallium, lead, bismuth, or polonium.

A “halide salt” is an ionic complex in which the anion(s) is(are) halide ion(s), including but not limited to fluoride ion(s), chloride ion(s), bromide ion(s), and iodide ion(s). A “fluoride salt” is an ionic complex in which the anion(s) is(are) fluoride ion(s). According to the present disclosure, the cation of the halide salt or the fluoride salt may be any positively charged chemical species.

A “metal fluoride” is an ionic complex in which the cation is a metal ion and the anion(s) is(are) fluoride ion(s). According to some aspects of the present disclosure, the metal salt and the fluoride salt react to create a metal fluoride shell around the metal nanoparticle core. Similarly, a “metal halide” is an ionic complex in which the cation is a metal ion and the anion(s) is(are) halide ion(s).

A “fluoride-containing” salt is an ionic complex in which the anion(s) contain fluoride ion but are not limited to being solely fluoride. Instead, “fluoride-containing” salts include ionic complexes where the anion(s) contain fluoride itself in complex with other ions or atoms. “Fluoride-containing” salts suitable for use in aspects of the present disclosure include those known to persons of ordinary skill in the art, including, but not limited to, fluoride salts, non-metal fluoroanions such as tetrafluoroborate salts and hexafluorophosphate salts, and oxyfluoride salts. In some aspects of the present disclosure, the fluoride-containing salts may include quaternary ammonium fluorides and fluorinated organic compounds. According to some aspects of the present disclosure, the metal salt and the fluoride-containing salt react to create a fluoride-containing shell around the metal nanoparticle core.

The term “electrode” refers to an electrical conductor where ions and electrons are exchanged with an electrolyte and an outer circuit. “Positive electrode” and “cathode” are used synonymously in the present description and refer to the electrode having the higher electrode potential in an electrochemical cell (i.e. higher than the negative electrode). “Negative electrode” and “anode” are used synonymously in the present description and refer to the electrode having the lower electrode potential in an electrochemical cell (i.e. lower than the positive electrode). Cathodic reduction refers to a gain of electron(s) of a chemical species, and anodic oxidation refers to the loss of electron(s) of a chemical species. Positive and negative electrodes of the present invention may be provided in a range of useful configurations and form factors as known in the art of electrochemistry and battery science, including thin electrode designs, such as thin film electrode configurations. Electrodes are manufactured as known in the art, including as disclosed in, for example, U.S. Pat. No. 4,052,539, and Oxtoby et al., Principles of Modern Chemistry (1999), pp. 401-443.

The term “electrochemical cell” refers to devices and/or device components that convert chemical energy into electrical energy or vice versa. Electrochemical cells have two or more electrodes (e.g., positive and negative electrodes) and an electrolyte, wherein electrode reactions occurring at the electrode surfaces result in charge transfer processes. Electrochemical cells include, but are not limited to, primary batteries, secondary batteries, and electrolysis systems. General cell and/or battery construction is known in the art (see, e.g., Oxtoby et al., Principles of Modern Chemistry (1999), pp. 401-443).

“Electrolyte” refers to an ionic conductor which can be in the solid state, the liquid state (most common), or more rarely a gas (e.g., plasma).

I. CORE-SHELL NANOPARTICLE COMPRISING A METAL CORE AND A METAL HALIDE OR METAL OXYHALIDE SHELL

In an embodiment, a core-shell nanoparticle is provided that comprises a metal core that is surrounded by a metal halide or a metal oxyhalide shell.

In an illustrative example, the core-shell nanoparticle may be included in an electrode of a rechargeable battery, such as an F-shuttle battery. For example, it is difficult to use metal nanoparticles in the electrode of an F-shuttle battery as the metal is exposed to conditions that lead to undesired oxidation or dissolution of the metal. Accordingly, a halide shell is provided that is tailored to protect the metal core nanoparticle from the environment of the electrode while maintaining the desired performance of the metal nanoparticle. In a non-limiting example, the core may comprise copper metal and the shell may comprise LaF₃.

A method of making the core-shell nanoparticle may comprise providing a first mixture comprising a metal nanoparticle and a reducing agent, and mixing the first mixture with a solution comprising a metal salt and a halide salt to form a metal halide or oxyhalide shell on the metal nanoparticles.

I(a). Synthesis and Isolation of the Metal Core

In general, metal nanoparticles for use as the metal core may be synthesized by reacting a metal salt solution with a reducing agent in the presence of one or more stabilizers. In an illustrative example, the metal salt solution comprises a copper (II) nitrate hemipentahydrate (Cu(NO₃)₂·2.5H₂O) as the metal salt. The metal salt is mixed with CTAB and water, and the pH of the mixture may be adjusted to a pH of about 10-11, with for example, ammonium or sodium hydroxide.

Prior to addition of the reducing agent to the metal salt solution, the reducing agent may be mixed with one or more stabilizers and water, and mixed for a period of time, such as twenty minutes, prior to combining with the metal salt solution. The reducing agent is selected from the group consisting of hydrazine, sodium borohydride, sodium cyanoborohydride, sodium dithionate, sodium dithionite, iron (II) sulfate, tin (II) chloride, potassium iodide, oxalic acid, formic acid, ascorbic acid, thiosulfate salts, dithionate salts, phosphorous acid, phosphite salts, and hypophosphite salts. In a preferred embodiment, the reducing agent is hydrazine.

The metal salt solution and the reducing agent are combined to form the metal nanoparticles. Synthesis of the metal nanoparticles is performed in an atmosphere free of oxygen. Illustrative examples of atmospheres free of oxygen include, but are not limited to, nitrogen, argon, helium, hydrogen, and mixtures thereof. Following synthesis, the metal nanoparticles are isolated from the synthesis solution. It is to be understood that the method of isolating the metal nanoparticles is not limited, and may include one or more techniques such as filtering, decanting, and centrifuging. The metal nanoparticles may be washed one or more times with a solvent, such as ethanol, to remove any residual stabilizer or other organic material from the surface thereof.

I(b) Shell Formation

In general, the isolated metal nanoparticles may be redispersed in an aqueous solution containing additional reducing agent under an atmosphere that is free of oxygen. The mixture containing the isolated metal nanoparticles and reducing agent is then mixed under an atmosphere free of oxygen with a metal salt solution and a halide salt solution used to form the metal halide shell on the metal nanoparticle core. The metal salt solution and the fluoride salt solution used to form the shell may be added sequentially to the nanoparticle mixture, or the metal salt solution and the fluoride salt solution used to form the shell may be added simultaneously to the nanoparticle mixture.

II “YOLK-SHELL” NANOPARTICLES

(i) Protective, Fluoride Ion-Conducting Coatings

Useful protective encapsulating coatings include fluoride-ion conducting phases that are chemically and electrochemically stable in the presence of a liquid FIB electrolyte. Such phases permit the exchange of F— between the electrolyte and the active material. Suitable phases are known in the art and are described, for example, in “The CRC Handbook of Solid State Electrochemistry”, Chapter 6 (CRC, 1997, P. J. Gellings and H. J. M. Bouwmeester, Eds.), Sorokin and Sobolev, Crystallography Reports 2007, 52, 5, 842-863, Sobolev et. al., Crystallography Reports 2005,50, 3, 478-485, and Trnovcova et. al., Russian Journal of Electrochemistry, 2009, 45, 6, 630-639. These include, for example, crystalline phases such as LaF₃, CaF₂, SnF₂, PbF₂, PbSnF₄, analogous doped and/or solid solution phases (e.g. La_0.9Ba_0.1F_2.9, Ca_0.8Y_0.2F_2.2, Ca_0.5Ba_0.5F₂, and Pb_0.75Bi_0.23F_2.25), glassy phases such as 35InF₃.30SnF₂.35PbF₂, and mixed fluoride/other anion phases such as LaOF. For the purposes of this disclosure, any material or phase that permits the exchange of F- between the electrolyte and the active material, with bulk ionic conductivity above 10-10 S/cm at 298K is within the scope of the invention. These phases are chosen with constituents selected to be electrochemically stable at the potentials required for reaction of the species contained within the coatings by considering the standard redox potentials of the shell constituents and the inner species available in standard texts. See the example of FIG. 1G for a more detailed discussion of the selection of coating constituents in this regard.

Alternative protective coatings include polymers that are conducting for fluoride ions, for example boronate-functionalized polymers, alkylammonium-functionalized polymers, or those featuring suitable functional groups such as those described in Gorski et. al., Anal. Chim. Acta 2009, 633, 181-187 and Gorski, et al., Anal. Chim. Acta 2010, 665,39-46

The thickness of the protective coating is chosen so that exchange of F- between the electrolyte and the active material occurs on a timescale such that charge/discharge of the electrochemical cell can be achieved at suitable rates of operation around 298K (e.g C-rate, corresponding to full charge or discharge of the energy stored in the electrochemical cell in one hour), and will depend on the ionic conductivity of the coating material or phase. For example, a coating of LaF₃ is most usefully between 1-200 nm thick. More generally, the coating thickness can be from about 1 nm to about 1 μm.

The coating can be made by any suitable method of synthesis. These may include solution chemistry techniques such as the formation of the coating by precipitation of a solid from a solution containing the fluoride or its constituent precursors, sol-gel or other soft chemistry or “chimie douce” methods, hydrothermal synthesis, vacuum methods such as chemical vapor deposition, physical vapor deposition, sputtering, laser ablation and molecular beam epitaxy, electrochemical deposition, or fluorination of a material after deposition by reaction with a fluorine source. For example, one preferred method for the preparation of a LaF₃ coating is a sol-gel synthesis similar to those described in Rüdiger and Kemnitz, Dalton Trans., 2008, 1117-1127 and Fujihara et al., J. Ceram. Soc. Japan, 1998, 106, 124-126, using soluble lanthanum and fluorine sources in a suitable solvent (for example, La(CH₃COO)₃ and CF₃COOH in water). The coating as prepared may, optionally, be subjected to elevated temperature either in air or inert gas such as Ar for an annealing step, as desired. For example, a LaF₃ coating prepared by the sol-gel method may be heated to 500° C. in air to anneal the coating and assist with removal of impurities such as solvent. In this manner, fluoride-conducting coating phases may be synthesized as desired by adjusting the precursor materials, their stoichiometric ratios, and the post-initial reaction annealing step.

In another example, the LaF₃ coating can be obtained from precipitation, by slowly adding NH₄F into La(NO₃)₃ aqueous solution with nanoparticles of the core material suspended therein. Since LaF₃ is extremely insoluble in water, its crystallization will start on the surface of the suspended nanoparticles.

Alternatively, a sol-gel approach can be used to make a La₂O₃ coating, followed by post-fluorination using F₂ or HF to convert a substantial portion of this oxide to LaOF and/or LaF₃.

Fluoride-conducting encapsulants and/or coating phases and materials may be prepared on a three-dimensional structure (e.g. a metal or metal fluoride nanoparticle, or aggregate of nanoparticles), a two-dimensional structure (e.g. a metal or metal fluoride thin film), or a one-dimensional structure (e.g. a fiber or tube of metal or metal fluoride) as required. Similarly, fluoride-conducting phases may be prepared on the external and/or internal surfaces of complex micro- or mesoporous structures such as a zeolite or highly ordered templated material. This can include, but is not limited to mesoporous silicas such as MCM-41 or SBA-15, or metal-organic frameworks or similar coordination polymers.

(ii) Active Materials Encapsulated Within a Fluoride-Ion Conductive Coating

Useful structures and compositions include those in which a metal or metal fluoride is encapsulated within a fluoride-ion conductive coating (as described in (i) above) such that there exists sufficient void space within the encapsulation for the volume change between metal and metal fluoride phases (or, between a lower-valent metal fluoride species1VIFm and a higher-valent metal fluoride species MFn where n>m for the same metal M) to be accommodated upon conversion without rupture of the coating phase or material. Such structures and compositions are sized to fit within an fluoride-conducting encapsulant, in certain cases with at least enough void space available for up to 100% of the encapsulated metal atoms to be converted to the appropriate metal fluoride phase (e.g. for the process FeΔFeF₃ at least 211% void space is required compared to the starting volume of Fe, from Table 1). In other cases, the degree of conversion may be controlled electrochemically (e.g. by controlling the voltage limits and/or charge/discharge capacity) so that the encapsulant does not rupture during cycling in the cases whereby there is not enough void space for 100% conversion to be achieved. In addition, structures and compositions are also contemplated where the fluoride-conducting encapsulant is conformal or has a void space insufficient to fully accommodate conversion from the metal to metal fluoride, but has suitable flexibility to stretch or contract without rupture or cracking of the encapsulant. Such compositions may be two-dimensional (e.g. film-void-coating), or three-dimensional (e.g. nanoparticle-void-coating, or a more complex arrangement such as metal-impregnated zeolite-void-coating) as desired.

In still other embodiments, multiple, concentrically arranged encapsulants are contemplated. The respective concentrically arranged encapsulants can be separated by voids, and may be constructed of the same or different materials. In still other embodiments of concentrically arranged encapsulants, the active material and the outermost encapsulant (that contacts the electrolyte) may be separated by a polymer or other flexible material that is able to permit the passage of fluoride ions and is dimensionally able accommodate the volume changes upon cycling with rupturing the outermost encapsulant.

As will be understood, an active material completely surrounded and positioned within an encapsulant, but with at least some remaining void space and/or compressible non-active material (such as a polymer) can be referred to as a “yolk-shell” nanocomposite structure. Such fully encapsulated structures can be based on various compositional arrangements of active material and fluoride-conducting encapsulant. However, other arrangements that include an active material only partially surrounded by a fluoride-conducting protective coating are also contemplated. Such structures may include two or three dimensional non-fluoride conducting support structures (e.g. films, open sided cells, tubes, or the like) containing an active material having one or more sides coated with a fluoride conducting material to allow ion transport. Such support structures can include void space or dimensionally flexible polymer or other material to accommodate the volume changes upon cycling without rupturing the support structure or the encapsulant.

General preparative strategies for “yolk-shell” nanocomposite structures are described in Lou et al., Adv. Mater., 2008, 20, 3987-4019. The metal “yolk” material discussed is commonly Au, which is considered not to be a useful active material for FIB electrochemical cells. Likewise, the “shell” material described is often SiO2, which is considered not to be a useful fluoride ion conducting material. Therefore, suitable preparative strategies for “yolk-shell” nanocomposites useful in FIB electrochemical cells are outlined below. These are intended to be exemplary and are not limiting of the current invention. In certain examples, Cu metal or CuF₂ will be used as examples of the active material “yolk” and LaF₃ will be used as an example of an encapsulant or “shell” material; as before, these are not limiting of the invention as any material that can accommodate or release fluoride ions upon electrochemical reaction can be envisaged to constitute the “yolk” and any phase or material that permits the exchange of F- between the electrolyte and the active material can be envisaged to constitute the encapsulant or shell. In certain embodiments the active material is less than 1 micron in diameter, and most usefully, the active material “yolk” is between 1 and 500 nm in diameter and the encapsulant is from 2 to 100 nm thick.

FIG. 1B outlines a general route using a sacrificial inorganic “middle” layer such as SiO_2.

For example, Cu nanoparticles can be prepared by reduction of a solution of Cu' ions using hydrazine or similar reducing agent in the presence of stabilizing and/or coordinating species such as sodium citrate and/or surfactant (e.g. cetyltrimethylammonium bromide). Exposure of Cu nanoparticles to a surface-modifying ligand such as aminopropyltrimethoxysilane, APTS, (or other suitable bifunctional species such that one part of the molecule coordinates to the Cu surface, and the other part is presents a reactive silicon moiety to the external environment) followed by addition of hydrolyzable silica source such as tetraethylorthosilicate (TEOS) or sodium silicate solution (water glass) under appropriate conditions (e.g. Stober synthesis or sol-gel reaction) results in conformal coating of the Cu nanoparticles with SiO_2. The thickness of the SiO₂ layer (and, hence, the resulting void space) can be controlled by modification of the amount of SiO₂ precursor used and the reaction conditions. The SiO₂-coated Cu nanoparticles are then coated with an outer layer of LaF₃ by sol-gel reaction (optionally in the presence of surfactant such as Lutensol AO), whereby the thickness of this coating can be modified by the amount of LaF₃ precursors used and the reaction conditions. This step can be done after separation and/or purification of the intermediate Cu@SiO₂ material, or can be performed in the same reaction mixture after formation of the SiO₂ layer. The resulting Cu@SiO₂@LaF₃ composite may, optionally, undergo an annealing step, and/or the SiO₂ layer is then removed by exposure of the composite to a SiO₂ etchant material such as NaOH or HF under appropriate conditions to afford the Cu@LaF₃ “yolk-shell” composition. This material may subsequently undergo a final annealing step, optionally in the presence of a reducing agent such as H₂ to purify the Cu surface.

FIG. 1C describes a similar route using a sacrificial polymer “middle” layer. For example, Cu nanoparticles are coordinated by a polymer shell, by formation of Cu nanoparticles in the presence of a polymer or copolymer that features amino-, hydroxyl-, carboxylate or other ionizable functional groups (such as poly(acrylic acid), poly(ethyleneimine), poly(vinyl alcohol), poly(styrene sulfonate), a protein, a polysaccharide, or gelatin), or by growth of a polymer from the surface of suitably-modified Cu nanoparticles (e.g. poly(styrene sulfonate) grown by atom transfer radical polymerization from a 11-aminoundecyl 2-bromoisobutyrate functionalized surface). The thickness of the polymer layer (and, hence. the resulting void space) can be controlled by the polymer concentration and/or molecular weight. A shell of LaF₃ is grown around the outside of this Cu@polymer nanocomposite by sol-gel reaction to afford a Cu@polymer@LaF₃ nanocomposite. The polymer layer is then removed by decomposition at elevated temperature (in air or under inert gas such as Ar) or dissolution in suitable solvent (e.g. toluene, dichloromethane or acetone) to give the desired Cu@LaF₃ “yolk-shell” composition. This material may subsequently undergo a final annealing step, optionally in the presence of a reducing agent such as H₂ to purify the Cu surface. Alternatively, a polymer core-shell architecture such as the hollow latex-type particles described in McDonald and Devon, Adv. Colloid. Interf. Sci., 2002, 99, 181-213 may be employed as a template in which Cu nanoparticles are entrapped (either by exposure of Cu nanoparticles to pre-formed hollow latex particles or by coordination of Cu ions in solution to the ionizable pre-polymer or copolymer, followed by reduction of the Cu ions to give Cu nanoparticles and then generation of the hollow structure through e.g. solvent removal), followed by growth of LaF₃ shell, removal of polymer and annealing, as necessary, to generate a Cu@LaF₃ “yolk-shell” composition.

FIG. 1D delineates an alternative route in the absence of a sacrificial “middle” layer. For example, Cu nanoparticles are treated with a suitable surface-modifying ligand (e.g. 11-aminoundecanoic acid, AUDA) before an outer layer of LaF₃ is grown by sol-gel reaction to give a Cu@LaF₃ “core-shell” composite, which may then, optionally, subsequently undergo an annealing step. Partial etching of the Cu “core” using an appropriate etchant (for example, KCN, HCl/H₂O₂ or FeCl₃; suitable etchants for a wide variety of metals and compounds are given in “The CRC Handbook of Metal Etchants” (CRC, 1990, P. Walker and W. H. Tarn eds.), and may be chosen so as to not affect the “shell” material) enabled through control over the reaction conditions (e.g. etchant concentration, temperature, reaction time) generates void space in the Cu@LaF₃ particle, affording a “yolk-shell” Cu@LaF₃ composition. This material may subsequently undergo a final annealing step, optionally in the presence of a reducing agent such as H2 to purify the Cu surface.

FIG. 1E depicts a variation on the “sacrificial” syntheses described above, whereby nanoparticles of the active material are grown on the surface of a “sacrificial” material (here, it is the innermost material that is removed). For example, one or more Cu nanoparticles are grown on the surface of amino-functionalized poly(styrene) or SiO₂ particles. The resulting composite material is treated with a suitable Cu surface-modifying ligand (e.g. AUDA), after which an outer layer of LaF₃ is grown by sol-gel reaction. The innermost material is removed by thermal decomposition, etching or dissolution, resulting in a “yolk-shell” Cu@LaF₃ composition featuring one or more Cu nanoparticles. This material may subsequently undergo a final annealing step, optionally in the presence of a reducing agent such as H₂ to purify the Cu surface(s) and, optionally, to aggregate the Cu nanoparticles.

FIG. 1F outlines an alternative strategy, in which active material is grown in the internal structure or pores of a pre-formed “sacrificial” material. For example, Cu nanoparticles may be grown inside hollow SiO₂ nanospheres (see e.g. Hah et al., Chem. Commun., 2004, 1012-1013 for a possible synthetic approach). These Cu@SiO₂ “core-shell” nanocomposites are then coated with an outer layer of LaF₃ by sol-gel reaction (optionally in the presence of surfactant such as Lutensol AO), whereby the thickness of this coating can be modified by the amount of LaF₃ precursors used and the reaction conditions. The resulting Cu@SiO_2@LaF₃ composite may, optionally, undergo an annealing step, and/or the SiO₂ layer is then removed by exposure of the composite to a SiO₂ etchant material such as NaOH or HF under appropriate conditions to afford the Cu@LaF₃ “yolk-shell” composition. This material may subsequently undergo a final annealing step, optionally in the presence of a reducing agent such as H₂ to purify the Cu surface. In related syntheses, micro- or mesoporous materials such as zeolites may be used as the “template” for Cu nanoparticle formation, followed by subsequent Cu@LaF₃ “yolk-shell” generation in analogous fashion.

FIG. 1G also depicts an analogous alternative strategy whereby a highly-electropositive metal or its metal fluoride, such as CaF₂, is grown within the interior space of a hollow material such as a poly(styrene)-poly(acrylic acid) latex copolymer in a suitable solvent. These polymer-encapsulated CaF₂ nanocrystals are then coated with an outer layer of fluoride-ion conducting material of suitable electrochemical stability so as not to be itself reduced at the conversion potential of CaF₂ to Ca (˜0.2 V vs. Li+/Li). Examples of suitable protective materials include solid solutions such as Ca_xBa_yF₂ (x+y=1) where the Ca' and Ba²⁺ions in the protective shell are not substantially reduced during the conversion reaction of CaF₂ particles within the shell; in contrast a shell featuring a less electropositive metallic element (e.g. LaF₃) would itself be reduced in preference to the inner CaF₂ particles. The resulting CaF_2@polymer@Ca_xBa_yF₂ composite may, optionally, undergo an annealing step, and/or the polymer layer is then removed by exposure of the composite to high temperature or a suitable solvent etchant material that removes the polymer to the CaF₂@Ca_xBa_yF₂ “yolk-shell” composition.

Using the described encapsulated active material and/or yolk-shell nanocomposite electrodes, along with electrolytes, binders, additives, separators, battery casing or packaging, current collectors, electrical contacts, electronic charge and discharge controllers, and other elements of battery construction known to those skilled in the art, one can create useful lithium-free electrochemical cells operable at temperatures ranging from −40 degrees to 200 degrees Celsius. Such electrochemical cells can have substantially irreversible electrochemical reactions during discharge, making them suitable for forming galvanic cells or primary batteries. Alternatively, certain structures and compositions having an electrochemical reaction is at least partially reversible through application of electrical charge, secondary (rechargeable) batteries can be formed.

In certain embodiments, electrolytes suitable for FIB battery systems can include a fluoride salt and a solvent in which the fluoride salt is at least partially present in a dissolved state. The fluoride salt can be a metal fluoride or a non-metal fluoride. The solvent can be an organic liquid or an ionic liquid, or a mixture of the two. In other embodiments, electrolytes suitable for FIB battery systems can include a composite electrolyte containing fluoride salt, a polymer and optionally an organic liquid, an ionic liquid, or a mixture of the two. Electrolytes can include, but are not limited to combinations of fluoride salts and solvents disclosed in U.S. Pat. No. 9,166,249, titled “Fluoride Ion Battery Compositions”, the disclosure of which is herein incorporated by reference.

For example, liquid electrolyte salts suitable for FIB systems may contain complex cations in combination with the fluoride anion. The cation may feature organic groups, such as alkylammmonium, alkylphosphonium or alkylsulfonium species, or may consist of metal-organic or metal-coordination complex motifs, such as metallocenium species. Useful solvents for such liquid electrolyte salts may include non-aqueous solvents (denoted here as “organic”) that are capable of dissolving the aforementioned fluoride salts to molar concentrations of 0.01 M and above, preferred concentrations being between 0.1 and 3 M. Examples of such solvents include acetone, acetonitrile, benzonitrile, 4-fluorobenzonitrile, pentafluorobenzonitrile, triethylamine (TEA), diisopropylethylamine, 1,2-dimethoxyethane, ethylene carbonate, propylene carbonate (PC), y-butyrolactone, dimethyl carbonate, diethyl carbonate (DEC), methyl ethyl carbonate, propyl methyl carbonate, tetrahydrofuran, 2-methyltetrahydrofuran, nitromethane, benzene, toluene, chloroform, dichloromethane, 1,2-dichloroethane, dimethylsulfoxide, sulfolane, N,N-dimethylformamide (DMF), N,N-dimethylacetamide (DMA), carbon disulfide, ethyl acetate, methyl butyrate, n-propyl acetate, methyl propionate, methyl formate, 4-methyl-1,3,-dioxolane, pyridine, methyl isobutyl ketone, methyl ethyl ketone, hexamethylphosphoramide, hexamethylphosphorus triamide, 1 methyl-2-pyrrolidinone, 2-methoxyethyl acetate, trimethyl borate, triethylborate and substituted derivatives thereof, as well as sulfones such as ethylmethylsulfone, trimethylene sulfone, 1-methyltrimethylene sulfone, ethyl-sec-butyl sulfone, ethyl isopropyl sulfone (EIPS), 3,3,3-trifluoropropylmethyl sulfone, 2,2,2-trifluoroethyl sulfone, bis(2,2,2-trifluoroethyl)ether (BTFE), glymes (e.g., diglyme, tetraglyme), 1,2-dimethoxyethane (DME) and mixtures thereof. In certain embodiments, room temperature ionic liquid materials, or ionic liquids that remain liquid at temperatures below 200 degrees Celsius (such as those described in “Electrochemical Aspects of Ionic Liquids”, E. Ohno ed., Wiley Interscience, New York, 2005), are preferred. These can include ionic liquids that remain liquid at temperatures below 100 degrees Celsius such as 1-methyl,1-propylpiperidinium bi s(trifluoromethanesulfonyl)imide (MPPTF SI), butyltrimethylammonium bi s(trifluoromethanesulfonyl)imide (BTMATF SI) and 1-butyl,1-methylpyrrolidinium bis(trifluoromethanesulfonyl)imide (BMPTFSI) and their fluoroalkylphosphate (FAP) anion derivatives (e.g. MPPFAP) where FAP is a hydrophobic anion such as tris(pentafluroethyl)trifluorophosphate, all of which alone or in combination are useful solvents.

In certain other embodiments, the electrolytes suitable for FIB battery systems can include the compositions disclosed above with the addition of a fluoride-ion complexing species such as an anion receptor, a cation complexing species such as a crown ether, or a combination of both. Suitable anion receptors include species capable of binding fluoride anion such as boron, aluminum, ammonium, H-bond donor or similar groups, including aza ethers and alkyl and aryl boron and boronate complexes such as those described in McBreen et al, J. Power Sources, 2000, 89, 163 and West et al., J. Electrochem. Soc., 154, A929 (2007), and boroxin species such as those described in Nair et al., J. Phys. Chem. A, 113, 5918 (2009), all of which are incorporated by reference herein. In particular tris(hexafluoroisopropyl)borate, tris(pentafluorophenyl)borane and all possible regioisomers of difluorophenyl boroxin (DFB), trifluorophenyl boroxin, bis(trifluoromethyl)phenyl boroxin, trifluoromethyl)phenyl boroxin and fluoro(trifluoromethyl)phenyl boroxin can be used.

As will be appreciated, fluoride ion batteries are suitable for a wide range of primary or rechargeable applications, including but not limited to vehicle traction batteries (electric vehicles (EV), hybrid vehicles (HEV), and plug-in hybrid (PHEV)) or vehicle starter or ignition batteries. FIB systems can be useful stationary batteries for emergency power, local energy storage, starter or ignition, remote relay stations, communication base stations, uninterruptible power supplies (UPS), spinning reserve, peak shaving, or load leveling, or other electric grid electric storage or optimization applications. Small format or miniature battery applications including watch batteries, implanted medical device batteries, or sensing and monitoring system batteries (including gas or electric metering) are contemplated, as are other portable applications such as flashlights, toys, power tools, portable radio and television, mobile phones, camcorders, lap-top, tablet or hand-held computers, portable instruments, cordless devices, wireless peripherals, or emergency beacons. Military or extreme environment applications, including use in satellites, munitions, robots, unmanned aerial vehicles, or for military emergency power or communications are also possible.

III (c) COMPARATIVE EXAMPLE 1 AND EXPERIMENTAL EXAMPLE 1

In a Comparative Example 1, copper nanoparticles were made without a shell and analyzed. First, 2 mmol of Cu(NO₃)2·2.5H₂O and 1.87 mmol CTAB were dissolved in 75 ml water at room temperature, and 0.5 ml NH₄OH (28-30 wt % NH₃ in water, 14.8M) were added to adjust the pH to about 10-11. A solution was prepared containing hydrazine (3 ml of 50-60% reagent grade), CTAB (1.87 mmol), and citric acid (0.38 mmol) in water (75 ml) under argon and mixed for about 20 minutes before adding the copper nitrate solution. The reaction mixture was stirred for 1.5 hrs, to maximize copper nanoparticle growth. The resulting copper nanoparticles (˜50 nm) were isolated and washed. Specifically, the reaction synthesis mixture was centrifuged, decanted, mixed with ethanol and sonicated. FIG. 3 shows an X-ray diffraction (XRD) spectrum of the copper nanoparticles as-made. Three peaks are visible, all corresponding to Cu (°2θ): 43.0, 50.5, and 74.0. However, upon exposure to air, Cu is oxidized to Cu₂O, which begins forming at least as early as 4 days and is the main product after 9 days. This is illustrated in FIG. 4, which shows appearance of new peaks at 29.5, 42.3, 61.3, and 73.5°2θ, corresponding to Cu₂O.

In Experimental Example 1, core-shell nanoparticles were made in accordance with the present disclosure that comprised a core comprising a copper nanoparticle coated with a shell comprising lanthanum fluoride (Cu/LaF₃). The ˜50 nm copper nanoparticles were made using the same method as Comparative Example 1, but were redispersed in water with 3 ml of hydrazine (3 ml of 50-60% reagent grade) under an argon atmosphere following isolation and washing of the copper nanoparticles. To the mixture of water, copper nanoparticles, and hydrazine was added a solution of La(NO₃)₃·H₂O (1 mmol in 15 ml H₂O) and a solution of NaF (1 mmol in 15 ml H₂O). The reaction mixture was stirred for 10 minutes and then centrifuged.

The precipitate was isolated by centrifuge and analyzed by XRD. The XRD spectrum of the core-shell nanoparticles as synthesized is shown in FIG. 5. The XRD spectrum shows 5 peaks (°2θ): 25.0 (LaF3), 28.0 (LaF3), 43.5 (Cu), 50.4 (Cu), 74.0 (Cu). FIG. 6 shows stacked XRD spectra of the core-shell nanoparticles upon exposure to air for 9, 16, and 23 days. In contrast to Comparative Example 1, no spectral changes were observed. FIGS. 7A and 7B show TEM images of the core-shell nanoparticles as synthesized. As shown, the copper nanoparticle cores are covered with the LaF₃ shell. The shell has a thickness of about 0.30 nanometers. FIGS. 8A-8C show high-resolution TEM images of the core-shell nanoparticles as synthesized. The central black areas correspond to the copper core, and the peripheral black and white areas correspond to the LaF₃ shell. The figures show homogeneous coverage of the copper core directly coated with the LaF₃ shell.

Accordingly, the core-shell nanoparticle synthesized in Experimental Example 1 provides a shell capable of protecting the underlying metal core. Such a core-shell nanoparticle is useful for applications where the operating conditions would dissolve, oxidize, or otherwise contaminate the metal core. Illustrative examples include use of the core-shell nanoparticles as battery electrode materials.

In a non-limiting example as shown in FIG. 9, the core-shell nanoparticle of Experimental

Example 1 may be included as an active material in a negative electrode (anode) of an F-shuttle battery. The LaF₃ shell protects the copper core allowing it to operate as an active material without being dissolved. As shown in FIG. 10A and 10B, the core-shell nanoparticles of Experimental Example 1 were tested as the active material in an anode. The anode included the core-shell nanoparticles, a conductive agent (super P carbon), and PVdF binder in a ratio of 8:1:1.

COMPARATIVE EXAMPLE 2

An attempt was made to make a core-shell nanoparticle including a core comprising a copper nanoparticle directly coated with a shell comprising lanthanum fluoride (Cu/LaF₃). Comparative Example 2 was performed identically to Experimental Example 1, except that 1 mmol LaCl₃.7H₂O was used instead of La(NO₃)₃.6H₂O.

The XRD spectrum of the nanoparticles as synthesized in Comparative Example 2 is shown in FIG. 11. The XRD spectrum shows 5 peaks (°2θ): 24.5 (LaF₃), 27.6 (LaF₃), 43.6 (Cu), 50.5 (Cu), 74.1 (Cu). Therefore, the Cu remains during the course of the reaction of LaCl₃ and NaF.

However, oxidation of the Cu following exposure of the core-shell nanoparticles of Comparative Example 2 indicated that the shell was not properly formed. FIG. 12 shows stacked XRD spectra of the nanoparticles synthesized in Comparative Example 2 upon exposure to air for 8, 15, and 22 days. Additional peaks are observed starting at 8 days (°2θ): 35.4, 36.4, 38.8, 42.5, 44.8, 48.7, 52.3, 61.5, 73.5. At least the peaks at 36.4, 42.5, 61.5, and 73.5 °2θ are consistent with Cu₂O formation. The peaks at 43.6, 50.5, and 74.1 °2θ, which are consistent with Cu, have also diminished in intensity. As shown in FIG. 13, the TEM image shows inhomogeneous, partial coverage of Cu nanoparticles with LaF₃, as well as LaF₃ that is not associated with Cu nanoparticles. Accordingly, shells made with LaCl₃.7H₂O do not result in a desirable core-shell composition as it would leave the Cu core exposed to the environment of an electrochemical cell that might dissolve the Cu core. In addition, the LaF₃ that is not associated with Cu nanoparticles would decrease the overall efficiency of any system incorporating the mixture.

Layered Thin Film Electrode Study

The core and shell materials may also be studied in a thin film electrode configuration. Briefly, copper was sputtered to a thickness of about 80 nm onto a glassy carbon substrate of 1 mm thickness. After formation of a Cu film, LaF₃ was sputtered onto the Cu layer toa thickness of less than 5 nm, to form a double-layered thin film; for comparison purposes, a single layered Cu thin film without the LaF₃ coating was also prepared. The thin films were studied in a three electrode cell configuration, with a Ag-wire soaked in 1-methyl-1-propylpyrrolidinium bis(trifluoromethylsulfonyl)imide (MPPyTFSI) and 0.01 M AgOTf as the reference electrode and a Pt-wire as a counter electrode, and using 0.1M tetramethylammonium fluoride (TMAF) in MPPyTFSI as the electrolyte. Cyclic voltammetry was measured in the range from −2.4V to −0.7V vs. Ag/Ag+. Evaluation was conducted in a moisture- and oxygen-free glove box.

The cyclic voltammograms obtained are shown in FIG. 14. For the double layered thin film, the anodic peak measured was symmetrical with the cathodic peak, and no copper ions were detected in the electrolyte by ICP-MS. These results indicate reversible transport of fluoride ions from the LaF₃ layer into the Cu later. In comparison, the cyclic voltammogram obtained for the single layered Cu thin film is asymmetric. The anodic current exceeds the cathodic current, indicating dissolution of the Cu during anodic reaction. ICP-MS data confirms this, showing 5 ppm Cu in the electrolyte.

The Cu-LaF₃ double layered thin film electrode was also studied by XPS, initially and after fluorination at the voltages indicated in FIG. 15A. The initial time point (1 in FIG. 15A) was studied as deposited. The potential was then swept from OCV (about −1.5V vs Ag/Ag+) to −0.8V and maintained for 1 hour. After fluorination reaction, a sample of the electrode was taken for XPS depth profiling analysis.

In the initial XPS spectrum (FIG. 15B) the surface contains more La and F than Cu. After fluorination, fluoride ions can be detected at higher levels at deeper depths than in the initial XPS spectrum; in the initial spectrum, fluoride levels dropped off more sharply with increasing depth. Collectively, the XPS data show that fluoride ions can penetrate into the copper layer. Thus, after reduction, fluoride ions can diffuse into the Cu cores.

While the aspects described herein have been described in conjunction with the example aspects outlined above, various alternatives, modifications, variations, improvements, and/or substantial equivalents, whether known or that are or may be presently unforeseen, may become apparent to those having at least ordinary skill in the art. Accordingly, the example aspects, as set forth above, are intended to be illustrative, not limiting. Various changes may be made without departing from the spirit and scope of the disclosure. Therefore, the disclosure is intended to embrace all known or later-developed alternatives, modifications, variations, improvements, and/or substantial equivalents.

Thus, the claims are not intended to be limited to the aspects shown herein, but are to be accorded the full scope consistent with the language of the claims, wherein reference to an element in the singular is not intended to mean “one and only one” unless specifically so stated, but rather “one or more.” All structural and functional equivalents to the elements of the various aspects described throughout this disclosure that are known or later come to be known to those of ordinary skill in the art are expressly incorporated herein by reference and are intended to be encompassed by the claims. Moreover, nothing disclosed herein is intended to be dedicated to the public regardless of whether such disclosure is explicitly recited in the claims. No claim element is to be construed as a means plus function unless the element is expressly recited using the phrase “means for.”

Further, the word “example” is used herein to mean “serving as an example, instance, or illustration.” Any aspect described herein as “example” is not necessarily to be construed as preferred or advantageous over other aspects. Unless specifically stated otherwise, the term “some” refers to one or more. Combinations such as “at least one of A, B, or C,” “at least one of A, B, and C,” and “A, B, C, or any combination thereof” include any combination of A, B, and/or C, and may include multiples of A, multiples of B, or multiples of C. Specifically, combinations such as “at least one of A, B, or C,” “at least one of A, B, and C,” and “A, B, C, or any combination thereof” may be A only, B only, C only, A and B, A and C, B and C, or A and B and C, where any such combinations may contain one or more member or members of A, B, or C. Nothing disclosed herein is intended to be dedicated to the public regardless of whether such disclosure is explicitly recited in the claims.

The examples are put forth so as to provide those of ordinary skill in the art with a complete disclosure and description of how to make and use the present invention, and are not intended to limit the scope of what the inventors regard as their invention nor are they intended to represent that the experiments below are all or the only experiments performed. Efforts have been made to ensure accuracy with respect to numbers used (e.g. amounts, dimensions, etc.) but some experimental errors and deviations should be accounted for.

Moreover, all references throughout this application, for example patent documents including issued or granted patents or equivalents; patent application publications; and non-patent literature documents or other source material; are hereby incorporated by reference herein in their entireties, as though individually incorporated by reference.

Claims

1. A method of making coated metal nanoparticles, the method comprising: a) providing a water/metal nanoparticle mixture;b) exposing the water/metal nanoparticle mixture to an inert atmosphere;c) forming a fluoride-containing shell around a metal nanoparticle core.

2. The method of claim 1, wherein the fluoride-containing shell is directly attached to the metal nanoparticle core.

3. The method of claim 1, further comprising: b′) creating a sacrificial coating around a metal nanoparticle core before forming the fluoride-containing shell, to provide a sacrificial layer between the metal nanoparticle core and the fluoride-containing shell.

4. The method of claim 3, further comprising: d) at least partially removing the sacrificial layer, to provide a void between the metal nanoparticle core and the fluoride-containing shell; ande) annealing the fluoride-containing shell.

5. The method of claim 1, further comprising: d′) at least partially etching the outer surface of the metal nanoparticle core, to provide a void between the metal nanoparticle core and the fluoride-containing shell; ande) annealing the fluoride-containing shell.

6. The method of claim 1, wherein the metal nanoparticle core comprises a plurality of metal nanoparticles attached to the outer surface of an amine-coated polymer or SiO2 nanosphere.

7. The method of claim 6, wherein the method further comprises: d″) removing the nanosphere; ande) annealing the fluoride-containing shell.

8. The method of claim 1, further comprising: b″) adding a reducing agent (i) to the water/metal nanoparticle mixture, before forming the fluoride-containing shell around the metal nanoparticle core.

9. The method of claim 3, wherein the sacrificial coating is a conformal sacrificial polymer.

10. The method of claim 3, wherein the sacrificial coating is a dimensionally flexible polymer.

11. The method of claim 10, wherein the dimensionally flexible polymer is fluoride-conducting.

12. The method of claim 8, wherein the reducing agent (i) comprises hydrazine, sodium borohydride, sodium cyanoborohydride, sodium dithionate, sodium dithionite, iron (II) sulfate, tin (II) chloride, potassium iodide, oxalic acid, formic acid, ascorbic acid, thiosulfate salts, dithionate salts, phosphorous acid, phosphite salts, hypophosphite salts, and mixtures thereof.

13. The method of claim 12, wherein the reducing agent (i) comprises at least one of hydrazine, sodium borohydride, sodium cyanoborohydride, sodium dithionate, and sodium dithionite.

14. The method of claim 8, wherein the reducing agent (i) is hydrazine.

15. The method of claim 1, wherein forming the fluoride-containing shell comprises adding a metal salt (i) and a fluoride-containing salt to the water/metal nanoparticle mixture to create a fluoride-containing shell around the metal nanoparticle core.

16. The method of claim 15, further comprising adding a reducing agent (i) to the water/metal nanoparticle mixture prior to adding the metal salt (i) and the fluoride-containing salt to the water/metal nanoparticle mixture.

17. The method of claim 16, wherein the metal salt (i) is selected from the group consisting of alkali metal salts, alkaline earth metal salts, and transition metal salts.

18. The method of claim 16, wherein the metal salt (i) is a transition metal salt.

19. The method of claim 16, wherein the metal salt (i) is selected from the group consisting of lanthanum salts, cerium salts, and magnesium salts.

20. The method of claim 16, wherein the metal salt (i) is selected from the group consisting of lanthanum salts and cerium salts.

21. The method of claim 16, wherein the metal salt (i) is a lanthanum salt.

22. The method of claim 21, wherein the lanthanum salt is lanthanum nitrate.

23. The method of claim 21, wherein the fluoride-containing salt is sodium fluoride.

24. The method of claim 23, wherein the lanthanum salt is lanthanum nitrate.

25. The method of claim 24, wherein the lanthanum nitrate and the sodium fluoride are added simultaneously to the water/metal nanoparticle/reducing agent mixture.

26. The method of claim 21, wherein the lanthanum salt and the fluoride-containing salt are added simultaneously to the water/metal nanoparticle/reducing agent mixture.

27. The method of claim 1, wherein the metal nanoparticles are selected from the group consisting of iron nanoparticles, cobalt nanoparticles, nickel nanoparticles, copper nanoparticles, and lead nanoparticles.

28. The method of claim 27, wherein the metal nanoparticles are selected from the group consisting of cobalt nanoparticles and copper nanoparticles.

29. The method of claim 16, further comprising mixing one or more isolated metal nanoparticles in water at room temperature to produce the water/metal nanoparticle mixture.

30. The method of claim 29, further comprising mixing a metal salt (ii) with a reducing agent (ii) in the presence of one or more stabilizers, to form the one or more isolated metal nanoparticles, wherein the molecular weight of each of the one or more stabilizers is less than 500 g/mol.

31. The method of claim 30, wherein the molecular weight of each of the one or more stabilizers is less than 400 g/mol.

32. The method of claim 31, wherein the molecular weight of each of the one or more stabilizers is less than 350 g/mol.

33. The method of claim 30, wherein the one or more stabilizers comprises at least one of citric acid and CTAB.

34. The method of claim 30, wherein the one or more isolated metal nanoparticles are formed by mixing a first mixture comprising water, the metal salt (ii), and the one or more stabilizers with a second mixture comprising water, the reducing agent (ii), and the one or more stabilizers.

35. The method of claim 34, wherein the second mixture is mixed for at least 15 minutes before the second mixture is mixed with the first mixture in the presence of argon.

36. The method of claim 30, wherein the metal nanoparticles are isolated from the reaction mixture of the metal salt (ii), the reducing agent (ii), and the one or more stabilizers, the isolated nanoparticles are washed one or more times with a solvent before mixing the metal nanoparticles with the reducing agent (i), the metal salt (i), and the fluoride salt, and optionally the isolated and washed nanoparticles are mixed with water and the reducing agent (i) in an inert atmosphere before mixing with the metal salt (i) and the fluoride salt.

37. The method of claim 30, wherein the reducing agent (ii) comprises at least one of hydrazine, sodium borohydride, sodium cyanoborohydride, sodium dithionate, sodium dithionite, iron (II) sulfate, tin (II) chloride, potassium iodide, oxalic acid, formic acid, ascorbic acid, thiosulfate salts, dithionate salts, phosphorous acid, phosphite salts, and hypophosphite salts.

38. The method of claim 37, wherein the reducing agent (ii) comprises at least one of hydrazine, sodium borohydride, sodium cyanoborohydride, sodium dithionate, and sodium dithionite.

39. The method of claim 38, wherein the reducing agent (ii) is hydrazine.

40. The method of claim 30, wherein the metal salt (ii) is a metal nitrate.

41. The method of claim 40, wherein the metal salt (ii) is copper nitrate and the metal nanoparticles are copper nanoparticles.

42. The method of claim 34, wherein the pH of the first mixture is adjusted to a pH of 10-11 before mixing with the second mixture.

43. The method of claim 42, wherein pH of the first mixture is adjusted to a pH of 10-11 before mixing with the second mixture by adding at least one of ammonium hydroxide and sodium hydroxide.

44. The method of claim 16, wherein the metal salt (i) and the fluoride-containing salt are added simultaneously to the water/metal nanoparticle/reducing agent mixture.

45. The method of claim 16, wherein the metal salt (i) is a lanthanum salt, and the metal salt (i) and the fluoride salt are added simultaneously to the water/metal nanoparticle/reducing agent mixture.

46. The method of claim 1, wherein the metal nanoparticles are selected from the group consisting of iron nanoparticles, cobalt nanoparticles, nickel nanoparticles, copper nanoparticles, and lead nanoparticles.

47. The method of claim 1, wherein the metal nanoparticles are selected from the group consisting of cobalt nanoparticles and copper nanoparticles.

48. The method of claim 1, wherein the coated metal nanoparticles are Cu-LaF3 core-shell nanoparticles.

49. An electrode for a fluoride shuttle battery comprising the coated metal nanoparticles formed by the method of claim 1.

50. A battery comprising the electrode of claim 49.