Patent Publication Number: US-2023163346-A1

Title: Cathodes and electrolytes for rechargeable magnesium batteries and methods of manufacture

Description:
CROSS-REFERENCE TO RELATED APPLICATIONS 
     This application is a continuation of U.S. Continuation-in-Part patent application Ser. No. 17/085,099, entitled “CATHODES AND ELECTROLYTES FOR RECHARGEABLE MAGNESIUM BATTERIES AND METHODS OF MANUFACTURE,” filed Oct. 30, 2020, which claims priority from Divisional U.S. patent application Ser. No. 15,897,721, entitled “CATHODES AND ELECTROLYTES FOR RECHARGEABLE MAGNESIUM BATTERIES AND METHODS OF MANUFACTURE,” filed Feb. 15, 2018, and issued on Nov. 3, 2020 as U.S. Pat. No. 10,826,114, which claims priority from U.S. patent application Ser. No. 14/325,891, entitled “CATHODES AND ELECTROLYTES FOR RECHARGEABLE MAGNESIUM BATTERIES AND METHODS OF MANUFACTURE” filed Jul. 8, 2014, and issued on Apr. 17, 2018 as U.S. Pat. No. 9,947,962, which claims priority under 35 U.S.C. § 119(e) to U.S. Provisional Patent Application Ser. No. 61/843,647, filed Jul. 8, 2013, entitled “CATHODES AND ELECTROLYTES FOR RECHARGEABLE MAGNESIUM BATTERIES AND METHODS OF MANUFACTURE”, which are herein incorporated by reference. 
    
    
     GOVERNMENT FUNDING 
     This invention was made with government support under grant #DE-FE0004000 awarded by the Department of Energy-NETL. The government has certain rights in the invention. 
    
    
     FIELD OF THE INVENTION 
     The invention relates to Chevrel-phase materials and methods for their preparation, and to secondary electrochemical cells utilizing a magnesium-containing anode and a Chevrel-phase-containing cathode. 
     BACKGROUND 
     High energy density, rechargeable electrochemical cells are known in the art. A rechargeable cell is theoretically capable of charging and discharging indefinitely. In producing a rechargeable battery system, a material for the cathode is selected. In certain instances, the cathode material is in the form of a liquid which allows reactions to readily take place. However, when in the form of a liquid, provisions are made to keep the cathode active material away from the anode, otherwise self-discharge can occur. As an alternative, the cathode material can be in the form of a solid which is essentially insoluble in the electrolyte. The solid cathode material is selected such that it absorbs and desorbs the anode ion because solubility of the anode ion occurs reversibly during operation of the cell. Such a solid cathode can be capable of intercalation of ions which are solubilized by the electrolyte. The electrolyte is selected to permit electroplating of solubilized ions at the anode. The plating of ions at the anode occurs during recharge of the cell and the intercalation of the cathode occurs during discharge of the cell. 
     Chevrel-phase compounds (CPs), also referred to as Chevrel materials, include an invariant portion which may consist essentially of molybdenum and a chalcogen. The chalcogen can be selected from elements in Group 16 of the Periodic Table, including sulfur, selenium, tellurium or mixtures of these, with or without minor amounts of oxygen. Ordinarily, this fixed portion has a stoichiometric formula of Mo 6 Z y  where Z represents the chalcogen and y is usually between about 7.5 and 8.5, most typically about 8. The unique crystal structure of the materials permits intercalation of metals, so that the overall stoichiometry of the Chevrel-phase material is represented as M x Mo 6 Z y  where M represents the intercalated metal and ‘x’ may vary from 0 (no intercalated metal) to an upper limit which may be about 4 or less depending upon the particular metal. 
     Ternary CPs are a unique class of cluster compounds which exhibit remarkable magnetic, thermoelectric, catalytic, and superconductive properties. The crystal structure of CPs consists of Mo 6 -octahedron clusters surrounded by eight chalcogen (e.g., S and/or Se) atoms at the corners of a distorted cube. For example, Mo 6 S 8  units are linked with each other and form a three-dimensional framework with open cavities/channels that can be filled with wide-variety of guest atoms and form ternary CPs M x Mo 6 S 8  (0&lt;x&lt;4). However, Mo 6 S 8  binary CPs cannot be synthesized directly and indirectly stabilized via leaching metal from their ternary counterparts. For example, Mo 6 Se 8  binary CPs include an iso-structure wherein Mo 6 Se 8  clusters are rotated approximately 26° about the body diagonal ( 3  axis) of the rhombohedral symmetry (R 3 ) which allows for bonding of Se atoms of one cluster to a Mo atom of a neighboring unit. The resultant three-dimensional Mo 6 Se 8  framework has open cavities/sites that can be filled completely in the M x Mo 6 Se 8  CPs into triclinic (P 1 ) forms due to intrinsic lattice instabilities. Among the three different families of CPs (Mo 6 Z 8 , Z═S, Se, Te), sulfide CPs have high ionic mobility at room temperature which allows them to transport monovalent (Li + , Na + ) and bivalent (Mg 2+ ) cations, and to act as a cathode for rechargeable batteries. 
     Energy is released upon intercalation of the metal into the CPs and as the intercalation process is partially or wholly reversible with certain metals, the CPs can therefore be used as cathodes in electrochemical cells. 
     A cell with a lithium anode and a Chevrel-phase cathode of the formula Li x Mo 6 S 8 , for example, can be subjected to a charge cycle in which lithium is removed from the Chevrel-phase by the applied electrical energy. In a discharge cycle, the lithium is re-intercalated into the Chevrel-phase releasing energy as electrical energy. The reaction mixture containing lithium, molybdenum and sulfur for direct formation of the lithium-intercalated CPs can be prepared by heating a precursor mixture. The precursor mixture including a heat-liable lithium compound together with molybdenum and sulfur, typically as a mixture of MoS 2  and free Mo. Upon heating, the heat-labile compound yields volatile decomposition products which may be swept from the mixture, e.g., by a stream of inert gas, leaving behind the lithium, molybdenum and sulfur to form the Chevrel-phase material. 
     Intercalation reactions in typical battery development have focused on the use of alkali metals, specifically lithium as anodes. In comparison, there has been less research with respect to the use of alkaline earth metals, such as magnesium, for use as anodes and the use of cathodes capable of intercalation of alkaline earth metal ions. 
     It is known in the art to use lithium ion batteries for a wide variety of energy storage applications due to their very high energy density and flexible design. In considering alternative materials to lithium in producing electrochemical batteries, it is acknowledged that magnesium-based energy storage systems may be considered suitable alternatives because magnesium is environmentally safe, cost effective and abundant in the earth&#39;s crest. Further, magnesium is bivalent and theoretically capable of rendering higher volumetric capacity than lithium. 
     It has been found that conventional salts such as Mg(ClO 4 ) 2 , Mg(CF 3 SO 3 ) 2 , Mg[(CF 3 SO 2 ) 2 N] 2  and the like, dissolved in various non-aqueous solvents develop surface passivation on a magnesium anode and effectively block Mg 2+  transport. Relatively fast and easy intercalation of Mg 2+  ions at room temperature makes CPs a preferred material of the cathode for magnesium batteries. However, synthesis of the thermodynamically unstable Mo 6 S 8  phase is challenging. Typically, a CuCP (Cu x Mo 6 S 8 ) is synthesized by solid state reactions of elemental blends of copper, molybdenum, and MoS 2  powders in an evacuated quartz ampoules at a temperature of approximately 1150° C. for one week or by a molten salt approach including heat treatment at approximately 850° C. for about 60 hours under an argon atmosphere. Both of these approaches require chemical leaching in solution for several days at room temperature for complete removal of the copper. 
     The conventional methods utilized are not convenient approaches that can be readily and effectively translated into large scale manufacturing processes for generating the Chevrel phase. For example, an elemental blend sealed in evacuated quartz ampoule and heated at high temperature (˜1273 K) for a long duration (˜7 days) to obtain Cu x Mo 6 S 8  results in high manufacturing costs not withstanding generating reproducible large scale quantities. Further, a significant disadvantage is the high vapor pressure of sulfur inside the ampoule during heating which causes a safety hazard. Furthermore, the final product obtained from the quartz ampoule has non-stoichiometry due to sulfur volatilization and condensation on the ampoule walls further from the product and excess sulfur that may be hence required to compensate for sulfur vapor loss during heating. Attempts to use metal sulfide (CuS, MoS 2 ) instead of elemental sulfur to avoid the high vapor pressure, has resulted in long and arduos synthesis time which is unreasonably long and thus not amenable large-scale production. Moreover, it was found that there can be difficulty in forming a reaction product at high temperature, e.g., the Chevrel phase may not be obtained and instead a sulfur deficient phase can form which adversely affects the desired and expected electrochemical performance. 
     In an attempt to reduce total synthesis time duration involved during the solid-state reaction method, cold-pressing and hot pressing have been employed as alternative means for the synthesis of a Cu x Mo 6 S 8  phase. Neither the milling time nor the sintering temperature has been optimized for the synthesis of Cu x Mo 6 S 8 . However, it was found that pressure-assisted sintering at elevated temperature ˜1123-1473 K was capable of reducing the synthesis duration to ˜5-8 hours as compared to 7 days required for solid-state synthesis in an evacuated quartz ampoule. 
     The desired CPs also have been synthesized from soluble sulfide precursor, e.g., polythiomolybdate and metal salt, which form a chelated complex in ether or methanol solvent and directly forms the desired Cu 2 Mo 6 S 8  phase when heated at ˜1073-1273 K under hydrogen atmosphere. An alternative soluble precursor method was proposed for the synthesis of nickel and lithium ternary CPs. 
     Obtaining Mo 6 S 8  CPs from known soluble sulfide precursor methods requires the use of hydrogen gas during sulfurization. Final reduction of sulfur compounds to desired Chevrel phase at elevated temperature needs strict regulation and skills, and poses a safety concern for the synthesis of CPs. 
     Thus, there is a need for improvements in electrochemical cells incorporating Chevrel-phase cathodes and in the synthesis methods for the CPs, and furthermore, in the use of alkaline earth metals, such as magnesium, as anodes. Moreover, there is a need in the art to develop time-saving economical approaches and methods for the direct synthesis of CPs. In this respect, high energy mechanical milling (HEMM) is employed as a scalable, economical time-saving approach for the direct synthesis of ternary metal CPs (M x Mo 6 Z 8  and M x Mo 6 Z 1   8-y Z 2   y , wherein, for example, Z is S or Se, Z 1  is S and Z 2  is Se) using MZ, Mo and MoZ 2  or MZ 1 , MZ 2 , Mo, MoZ 2   1  and MoZ 2   2  as the precursor. The invention provides easy, rapid and facile precursor approaches for the synthesis of CPs for use as a cathode and magnesium-containing material for use as an anode in an electrochemical cell. 
     SUMMARY OF THE INVENTION 
     In one aspect, the invention provides an electrochemical cell including an alkali metal-containing anode, a cathode and an electrolyte. The cathode includes a Chevrel-phase material of a formula Mo 6 Z 1   8-y Z 2   y  derived from a precursor material of a formula M x Mo 6 Z 1   8-y Z 2   y  wherein M is a metallic element, x is a number from greater than 0 to 4, y is a number from greater than 0 to less than 8, and each of Z 1  and Z 2  is a chalcogen with or without the presence of oxygen, wherein Z 1  is a different chalcogen than Z 2 . 
     In certain embodiments, the alkali-metal-containing anode comprises magnesium. 
     In certain embodiments, the metallic element M can be selected from Li, Na, Mg, Ca, Sc, Cr, Mn, Fe Co, Ni, Cu, Zn, Sr, Y, Pd, Ag, Cd, In, Sn, Ba, La, Pb, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu and mixtures thereof. 
     Each of the chalcogens Z 1  and Z 2  can be selected from chemical elements in Group 16 of the Periodic Table, including sulfur, selenium, tellurium and mixtures thereof._Further, each of Z 1  and Z 2  can be sulfur, selenium, tellurium or a mixtures thereof, with or without the presence of oxygen. Wherein, Z 1  is a different chalcogen than Z 2 . 
     In certain embodiments, M is copper, x is 2, Z 1  is sulfur, and Z 2  is selenium. 
     The precursor material can be formed from a mixture of MZ 1 , MZ 2 , MoZ 2   1 , MoZ 2   2  and molybdenum. 
     The Chevrel-phase material can be of the formula Mo 6 S 8-y Se y  which is derived from a precursor material of Cu 2 Mo 6 S 8-y Se y  and the said precursor material Cu 2 Mo 6 S 8-y Se y  which can be derived from a mixture of ammonium tetrathiomolybdate and anhydrous CuCl 2  in the presence of anhydrous N,N-dimethylformamide. 
     The electrolyte can be in the form of an electrolyte solution including electrolyte metal salt and the desired solvent. In certain embodiments, the electrolyte solution includes amidomagnesium-based magnesium salt transmetallated with an aluminum salt electrolyte dissolved in the solvent. In other embodiments, the electrolyte solution includes phenyl magnesium chloride-aluminum chloride, amidomagnesium-based magnesium salt transmetallated with an aluminum salt electrolyte, and solvent. The solvent can be tetrahydrofuran. 
     In yet other embodiments, the electrolyte solution includes 3-bis(trimethylsilyl)aminophenylmagnesium chloride with aluminum chloride in tetrahydrofuran. 
     The electrochemical cell can be a rechargeable battery. 
     In another aspect, the invention provides a method of synthesizing a Chevrel-phase cathode material. The method includes preparing a precursor material of a formula M x Mo 6 Z 1   8-y Z 2   y , wherein M is a metallic element, x is a number from greater than 0 to 4, y is a number from greater than 0 to less than 8, each of Z 1  and Z 2  is a chacogen with or without the presence of oxygen, wherein Z 1  is a different chalcogen than Z 2 , and removing the metallic element from the precursor material to form a Chevrel-phase cathode material of a formula Mo 6 Z 1   8-y Z 2   y . 
     Each of Z 1  and Z 2  can be selected from the group consisting of sulfur, selenium, tellurium, wherein Z 1  is a different chalcogen than Z 2 . 
     In certain embodiments, preparing the precursor material includes combining stoichiometric amounts of MZ 1 , MZ 2 , MoZ 2   1 , MoZ 2   2  and molybdenum. Furthermore, preparing the precursor material can include combining stoichiometric amounts of ammonium tetrathiomolybdate, anhydrous copper chloride and N,N dimethylformamide to form the desired mixture. Furthermore, preparing the precursor material can include heating the mixture to at least substantially complete reaction, filtering, precipitating, drying the precipitate to yield a precursor material of a formula M 2 Mo 6 Z 1   8-y Z 2   y , completely or partially removing M ions, and drying to obtain the Chevrel-phase cathode material of Mo 6 Z 1   8-y Z 2   y . 
     In other embodiments, preparing the precursor material includes combining stroichiometric amounts of copper (II) sulfide, copper (II) selenide, molybdenum, molybdenum disulfide and molybdenum selenide. Further, preparing the precursor material can include high energy mechanical milling the mixture to form a powder, heating the mechanically milled powder to at least substantially complete the reaction, yielding a precursor material of a formula M 2 Mo 6 Z 1   8-y Z 2   y , completely or partially removing the M ions, and drying to obtain the Chevrel-phase cathode material of a formula Mo 6 Z 1   8-y Z 2   y . In another aspect, the invention provides a method of preparing an electrode. 
     In another aspect, the invention provides an electrode. The electrode includes a slurry and a current collector, wherein the slurry is at least partially deposited onto the current collector to form a coating thereon. The slurry includes a Chevrel-phase cathode material of a formula Mo 6 Z 1   8-y Z 2   y . 
     The current collector can be a material substrate selected from the group consisting of copper, graphite, nickel, platinum, quartz, gold, stainless steel, tantalum, titanium, silver and mixtures thereof. In certain embodiments, the current collector is graphite foil. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG.  1    is a plot that shows powder XRD pattern of Cu 2 Mo 6 S 8  (Cu 2 CP) (top) obtained by high energy mechanical milling of CuS, MoS 2 , and Mo corresponding to the stoichiometric compositions followed by heat treatment at 1000° C./5 h under UHP Ar, and acid leached Cu 1 Mo 6 S 8  (Cu 1 CP) (bottom) obtained after 2 days to partially leach copper using 6 M HCl solution, in accordance with certain embodiments of the invention; 
         FIG.  2   a    is a plot that shows cycling data,  FIG.  2   b    is a plot that shows galvanostatic discharge-charge profile, and  FIG.  2   c    is a plot that shows rate capability of the synthesized Cu 1 Mo 6 S 8  electrode following leaching of Cu 2 CP when cycled against magnesium in Mg-ion battery, in accordance with certain embodiments of the invention; 
         FIG.  3   a    is a plot that shows a galvanostatic discharge-charge profile of Cu 1 CP electrode at 1 st , 2 nd  and 3 rd  cycle carried out at ˜5 mAg −1  current rate within the potential window of 0.5-15 V,  FIG.  3   b    is a plot that shows differential capacity, dQ/dV versus voltage (V) curves of 2 nd  and 3 rd  cycle,  FIG.  3   c    is a plot that shows ex-situ XRD analysis at 0.5V and 1.5V cut-off voltage during charge/discharge cycles, and  FIG.  3   d    is a plot that shows cycling data of Cu 1 CP performed at a slow current rate of ˜5 mAg −1  within 0.5-1.5V potential window in a Mg-ion cell, in accordance with certain embodiments of the invention. 
         FIG.  4    is a plot that shows XRD patterns collected on the powders obtained following mechanically milling for 1 h, 2 h, and 3 h using stoichiometric amounts of the individual elements, sulfide and selenide precursors corresponding to Cu 2 Mo 6 S 7 Se 1  stoichiometry and also on powders obtained after heat-treating at 1000° C. for 5 h showing the formation of Cu 2 Mo 6 S 7 Se 1  and acid leached Mo 6 S 7 Se 1 , respectively, in accordance with certain embodiments of the invention; 
         FIG.  5   a    is a plot that shows a cyclic voltammogram (CV) curve obtained with a sweep rate of ˜50 μVs −1  showing Mg-ion insertion/extraction into/from the synthesized Mo 6 S 7 Se 1  electrode,  FIG.  5   b    is a plot that shows galvanostatic cycling data at a current rate of ˜20 mAg −1 ,  FIG.  5   c    is a plot that shows capacity versus voltage profiles, and  FIG.  5   d    is a plot that shows differential capacity versus voltage (dQ/dV versus V) curves for the 2 nd , 50 th , and 200 th  cycles, in accordance with certain embodiments of the invention; 
         FIGS.  6   a ,  6   b  and  6   c    are plots that show XRD patterns collected on the powders after mechanically milling for 1 h, 2 h, and 3 h corresponding to the stoichiometric ratio of Cu 2 Mo 6 S 8-x Se x  (x=3, 4, 5) and after heat treating at 1000° C. for 5 h showing the formation of (a) Cu 2 Mo 6 S 5 Se 3  and acid leached Mo 6 S 5 Se 3 , (b) Cu 2 Mo 6 S 4 Se 4  and acid leached Mo 6 S 4 Se 4 , and (c) Cu 2 Mo 6 S 3 Se 5  and acid leached Mo 6 S 3 Se 5 , respectively, in accordance with certain embodiments of the invention; 
         FIG.  7   a    is a plot that shows galvanostatic cycling data and  FIG.  7   b    is a plot that shows capacity versus voltage profiles obtained at a current rate of ˜20 mAg −1  cycled between 0.5-1.5V for Mo 6 S 5 Se 3  electrodes using the 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte, in accordance with certain embodiments of the invention; 
         FIG.  8   a    is a plot that shows galvanostatic cycling data and  FIG.  8   b    is a plot that shows capacity versus voltage profiles performed at a current rate of ˜20 mAg −1  between 0.5-1.5 V for Mo 6 S 4 Se 4  electrodes using the 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte, in accordance with certain embodiments of the invention; 
         FIG.  9   a    is a plot that shows galvanostatic cycling data and  FIG.  9   b    is a plot that shows capacity versus voltage profiles performed at a current rate of ˜20 mAg −1  between 0.5-1.75 V for Mo 6 S 3 Se 5  electrodes using the 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte, in accordance with certain embodiments of the invention; and 
         FIG.  10    is a plot that shows rate capabilities of Mo 6 S 5 Se 3  and Mo 6 S 4 Se 4  electrodes in a Mg-ion battery, in accordance with certain embodiments of the invention. 
     
    
    
     DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS 
     The invention relates to Chevrel-phase materials, such as ternary molybdenum chalcogenide compounds. The Chevrel-phase materials, also referred to as Chevrel-phase compounds, in accordance with the invention have the formula Mo 6 Z 8 , wherein Mo represents molybdenum and Z represents a chalcogen, or Mo 6 Z 1   8-y Z 2   y , wherein Mo represents molybdenum and each of Z 1  and Z 2  represents a first chalcogen and a different second chalcogen, respectively. The invention further relates to electrochemical cells incorporating a cathode which includes a Chevrel-phase material, an anode which includes an alkali metal, and an electrolyte. 
     The Chevrel-phase materials of the formula Mo 6 Z 8  or Mo 6 Z 1   8-y Z 2   y  are prepared using various techniques and methods. In accordance with certain embodiments of the invention, the Chevrel-phase materials are derived from said precursor materials. The precursor materials have the formula M x Mo 6 Z 8 , wherein M is a metallic element, ‘x’ is a number from greater than 0 to 4, and Z is a chalcogen, e.g., chalcogenide, or the formula M x Mo 6 Z 1   8-y Z 2   y , wherein M is a metallic element, ‘x’ is a number from greater than 0 to 4, ‘y’ is a number from greater than 0 to less than 8, and each of Z 1 , and Z 2  is a chacogen, e.g., chalcogenide, wherein Z 1  is a different chalcogen than Z 2 . 
     The said precursor materials of the formulas M x Mo 6 Z 8  or M x Mo 6 Z 1   8-y Z 2   y  are formed using various methods. In accordance with certain embodiments of the invention, the precursor materials are formed by combining metal sulfides (MZ and MoZ 2 , or MZ 1 , MZ 2 , MoZ 2   1  and MoZ 2   2 ) with molybdenum (Mo). Further, in certain embodiments, the metal sulfides (MZ and MoZ 2 , or MZ 1 , MZ 2 , MoZ 2   1  and MoZ 2   2 ) and molybdenum (Mo) metal are subjected to high energy mechanical milling (HEMM) and during the ensuing milling process, the individual materials mentioned react resulting in forming the precursor materials. 
     In certain embodiments, the alkali metal is magnesium. Thus, the electrochemical cells in accordance with certain embodiments of the invention include a magnesium or magnesium-containing anode. 
     It is contemplated and understood that M includes a wide variety of metallic elements that are known to one having ordinary skill in the art. In certain embodiments, the metallic element is selected from Li, Na, Mg, Ca, Sc, Cr, Mn, Fe Co, Ni, Cu, Zn, Sr, Y, Pd, Ag, Cd, In, Sn, Ba, La, Pb, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu and mixtures thereof. 
     The chalcogens Z, Z 1  and Z 2  are selected from those known to one having ordinary skill in the art. In certain embodiments, the chalcogens Z, Z 1  and Z 2  are selected from the chemical elements in Group 16 of the Periodic Table, including sulfur, selenium, tellurium and mixtures thereof. Further, in certain embodiments, each of Z, Z 1  and Z 2  is sulfur, selenium, tellurium or a mixture thereof, with or without the presence of oxygen. Typically, the oxygen when present is in a small or trace amount. As aforementioned, Z 1  is a first chalcogen and Z 2  is a different second chalcogen. 
     In accordance with certain embodiments of the precursor approach for use in preparing Chevrel-phase materials, stoichiometric amounts of MZ, MoZ 2  and Mo, or stoichiometric amounts of MZ 1 , MZ 2 , MoZ2 1 , MoZ 2   2  and Mo are combined to form a mixture. The mixture is heated to complete the desired reaction or at least to substantially complete the desired reaction. The heating can be accomplished by various conventional mechanisms known in the art. For example, heating can be conducted over a hot plate at a temperature of about 90° C. under nitrogen bubbling. Following heating, the mixture is filtered using conventional techniques known in the art. Tetrahydrofuran (or any other known suitable solvent material) is added to the filtrate to initiate incipient precipitation. The resulting precipitate is washed in accordance with known techniques, e.g., with tetrahydrofuran and alcohol, e.g., methanol, and then dried using known techniques, e.g., at a temperature of about 60° C. 
     In certain embodiments, the dried product is ground and heated in an argon (or the like) atmosphere at about 1000° C. to yield metallic Chevrel-phase precursor material, e.g., M 2 Mo 6 Z 8  or M 2 Mo 6 Z 1   8-y Z 2   y . 
     The metals, e.g., metallic ions, are leached out using conventional mechanisms. For example, the metallic ions can be removed under an ambient atmosphere using a solution of HCl/O 2  bubbling. The solution is then centrifuged, washed and dried using known methods and techniques to yield the final Chevrel-phase product, e.g., Mo 6 Z 2  or Mo 6 Z 1   8-y Z 2   y . 
     In certain embodiments, the starting materials for use in forming the precursor material can be subjected to high energy mechanical milling (HEMM). Accordingly, appropriate amounts of MZ, MoZ 2  and Mo, or appropriate amounts of MZ 1 , MZ 2 , MoZ 2   1 , MoZ 2   2  and Mo are charged into a HEMM apparatus. The HEMM process is carried out for a defined period of time which can vary. The time period can be as short in duration as thirty minutes or as long as one or two or three hours or even more as needed not extending beyond few hours to initiate and complete the reaction. The HEMM process is subsequently followed by annealing at an elevated temperature under ultra high purity (UHP) argon atmosphere. The temperature can vary and may be maintained from about 1123 to about 1273K. 
     An advantage of employing the HEMM process is that no vacuum or silica ampoule is required for the synthesis due to complete absence of elemental sulfur/selenium in the starting composition. Further, there is no loss or gain in mass between the Chevrel-phase product and the precursor reactants. The ternary Chevrel phase can be formed directly from the ball-milled or mechanically milled powder upon annealing, a major advantage of the invention. In certain embodiments, the annealing is carried out a temperature that is about 1073 K or greater in a corundum crucible in a tubular furnace. 
     In certain embodiments, M is copper, ‘x’ is 2 and Z is sulfur. The precursor material is Cu 2 Mo 6 S 8  which is formed by the combination and reaction of CuS, MoS 2  and Mo. The Chevrel-phase material has the formula of Mo 6 S 8  and is derived from the precursor material Cu 2 Mo 6 S 8  followed by removing the copper or copper ions therefrom by subsequent acid leaching. Suitable materials for use in forming the precursor material can include a mixture of stoichiometric amounts of ammonium tetrathiomolybdate and anhydrous copper chloride (CuCl 2 ) in the presence of anhydrous N,N-dimethylformamide. For example, formation of the Chevrel-phase material can be conducted according to the formula: 2CuS+3Mo+3MoS 2 ═Cu 2 Mo 6 S 8 . For ease of description, much of the disclosure is directed to the chalcogen being sulfur (i.e., Z represents S) and the metallic element is copper (i.e., M represents Cu). However, it is understood that in accordance with the invention, the chalcogen is not limited to sulfur and the metallic element is also not limited to copper. 
     In certain other embodiments, M is copper, ‘x’ is 2, Z 1  is sulfur, Z 2  is selenium and ‘y’ is a number from greater than 0 to less than 8. The precursor material is Cu 2 Mo 6 S 8-y Se y  which is formed by the reaction of a combination of CuS, CuSe, MoS 2 , MoSe 2  and Mo. The Chevrel-phase material has the formula of Mo 6 S 8-y Se y  and is derived from the precursor material Cu 2 Mo 6 S 8-y Se y  followed by removing the copper or copper ions therefrom by subsequent acid leaching. Suitable materials for use in forming the precursor material can include a mixture of stoichiometric amounts of ammonium tetrathiomolybdate and anhydrous copper chloride (CuCl 2 ) in the presence of anhydrous N,N-dimethylformamide. For example, formation of the Chevrel-phase material can be conducted according to the formulas: Cu 2 Mo 6 S 8  (Cu 2 CP); Cu 1 Mo 6 S 8  (Cu 1 CP); Cu 2 Mo 6 S 7 Se 1  (Cu 2 CPSe 1 ); Mo 6 S 7 Se 1 ; Cu 2 Mo 6 S 8-x Se x  (x=3, 4, 5), Cu 2 Mo 6 S 5 Se 3  (Cu 2 CPSe 3 ); Mo 6 S 5 Se 3 , Cu 2 Mo 6 S 4 Se 4  (Cu 2 CPSe 4 ); Mo 6 S 4 Se 4 , Cu 2 Mo 6 S 3 Se 5  (Cu 2 CPSe 5 ); Mo 6 S 3 Se 5 . For ease of description, much of the disclosure is directed to the chalcogens being sulfur and selenium (i.e., Z 1  represents S, and Z 2  represents Se) and the metallic element is copper (i.e., M represents Cu). However, it is understood that in accordance with the invention, the chalcogens are not limited to only sulfur and selenium, and the metallic element is not limited to only copper. The Mo 6 S 8-y Se y  units are linked with each other and form a three-dimensional framework with open cavities/channels that can be filled with wide-variety of guest atoms and form ternary CPs M x Mo 6 S 8-y Se y  (0&lt;x&lt;4 and 0&lt;y&lt;8). 
     In general, the precursor approach includes preparing a precursor material which includes a metallic element and the metallic element (or ions thereof) is subsequently completely or partially removed (e.g., leached out) to produce the said Chevrel-phase product for use as cathode material. 
     The Chevrel-phase material synthesized in accordance with the above-described precursor approach can be employed to prepare and fabricate an electrode, i.e., cathode, using conventional techniques and apparatus. For example, an electrode slurry containing the Chevrel-phase material of the invention can be prepared and deposited on a current collector, and then subsequently dried. The current collector can include a wide variety of suitable materials known by one having ordinary skill in the art. Non-limiting examples include but are not limited to copper, graphite, nickel, platinum, quartz, gold, stainless steel, tantalum, titanium, silver, and mixtures thereof. In certain embodiments, the current collector is also graphite foil (grafoil). Deposition of the slurry can include forming a coating, e.g., thin film, on the current collector. Drying can be accomplished using conventional mechanisms such as drying in a vacuum oven. 
     The Chevrel-phase cathode material can be combined with an alkali-metal anode, e.g., a magnesium or magnesium alloy-containing anode, and an electrolyte to form an electrochemical cell, such as a magnesium ion rechargeable battery. 
     The electrolyte can be in the form of a solution. The electrolyte solution can include electrolyte salt containing magnesium and solvent. 
     In general, suitable electrolytes with high anodic/oxidative stability above 3V wherein magnesium can be deposited reversibly are not widely known and available in the art. It has been found that magnesium may not be reversibly deposited from solutions of simple magnesium salts, e.g., Mg(ClO 4 ) 2 , in conventional organic solvents, e.g., acetonitrile, propylene carbonate or N,N-dimethylformamide. This is primarily due to the formation of a dense passivating surface/blocking layer on the reactive magnesium electrode surface by the reduction products. It is believed and well-known that bare magnesium metal reacts with anions such as ClO 4   −1 , BF 4   −  to form insoluble magnesium salts/halides that block the magnesium electrodes. Moreover, the surface films effectively block the electrodes, as the mobility of the Mg 2+  ions through the impervious passivating films is low. After a period of time, the capacity fades leading to failure of the electrochemical cell. 
     It is generally known that magnesium can be deposited using Grignard reagents in ethereal solvents. Magnesium can be electro-deposited reversibly primarily based on the solutions of tetrahydrofuran (THF) using Grignard reagents (R—MgX, R=alkyl; X═Br, and amidomagnesium halides. However, due to the strongly reducing character of Grignard reagents, and limited oxidative stability (EtMgBr and BuMgCl have an oxidative stability 1.5V vs. Mg), it appears to be incompatible or realistically not possible for cathodes to be developed for use in batteries. Also, it is known to that tetrahydrofuran (THF) or primary amines (N-methylaniline) can be as electrolytes solvents in which both magnesium dissolution and deposition will occur. However, the Coulombic efficiency is typically low. In accordance with the invention, amidomagnesium halide-based Grignard reagent of the formula [3-[bis(trimethylsilyl]aminolphenylmagnesium chloride [(CH 3 ) 3 Si] 2 NC 6 H 4 MgCl] solution in 1.0 M THF is a suitable salt for synthesis of magnesium battery electrolyte. Due to the presence of an aromatic ring coupled with an amino methylsilyl group with MgCl +  ion, and electron lone pair donated to the aryl phenyl group, the R—Mg bond is thus strong and likely precludes or prevents the oxidation of the anionic species. 
     In certain embodiments of the invention, the electrolyte solution includes amidomagnesium-based magnesium salt transmetallated with an aluminum salt electrolyte dissolved in the solvent. In other embodiments, the electrolyte solution includes phenyl magnesium chloride-aluminum chloride, amidomagnesium-based magnesium salt transmetallated with an aluminum salt electrolyte, and solvent. The solvent can be tetrahydrofuran. In yet other embodiments, the electrolyte solution includes 3-bis(trimethylsilyl)aminophenylmagnesium chloride with aluminum chloride in tetrahydrofuran. 
     The cathodes, electrodes and electrochemical cells prepared in accordance with the present invention demonstrate the desired benefits and advantages over those that are known in the art. For example, the electrochemical performance, e.g., rate capability and stable specific capacity with galvanostatic cycling, of the products prepared according to the invention are found to be superior to the known products. The Chevrel-phase material prepared in accordance with the present invention also exhibits very high rate capability and cycling performance when assembled in a rechargeable magnesium electrochemical battery cell. 
     EXAMPLES 
     Example I 
     Materials Preparation 
     Cu 2 Mo 6 S 8  (CuCP) was synthesized as follows. In a 3-neck round bottom flask, stoichiometric amounts of ammonium tetrathiomolybdate (4 g, 15.37 mmol; Alfa-Aesar 99.95%) and anhydrous copper(II) chloride (0.6890 g, 5.12 mmol, Alfa-Aesar 99.985%) were added to N,N dimethylformamide, DMF (130 ml) solution. The resultant mixture was heated over a hot plate (˜90° C.) for 6 hours under constant N 2  bubbling. After complete reaction, the mixture turned deep red in color and was filtered. Tetrahydrofuran (1:5 by volume) was added immediately to the filtrate to incipient precipitation. A fine black precipitate was formed. This precipitate was kept overnight. Then, the precipitate was washed with tetrahydrofuran and methanol followed by drying at ˜60° C. for 24 hours. The final dried solid product was ground and heated in a UHP Ar+6.5% H 2  atmosphere at ˜1000° C. for 5 hours which directly yielded copper Chevrel phase Cu 2 Mo 6 S 8 . The copper ions were leached out under an ambient atmosphere using a solution of 6 M HCl/O 2  bubbling for 8 hours according to the method outlined by Lancry, et al. (“Leaching Chemistry and the Performance of the Mo 6 S 8  Cathodes in Rechargeable Mg Batteries, Chemistry of Materials”, 16 (2004) 2832-2838). Following complete copper leaching, the solution was centrifuged, washed with the same solvent and dried in an oven at ˜60° C. In order to perform qualitative phase analysis, Z-ray diffraction (XRD) was carried out using the Philips PW1830 system employing the CuK α  (λ=0.15406 nm) radiation. Microstructural analysis of the initial Cu 2 Mo 6 S 8  and Mo 6 S 8  obtained after copper removal was then performed using a scanning electron microscopy (JSM-6610, JEOL) operating at 10 kV. 
     Electrochemical Characterization 
     An electrode slurry was prepared by mixing 80 wt. % of the Mo 6 S 8  powder (−325 mesh), 10 wt. % Super P, 10 wt. % polyvinylidene fluoride (PVDF) dissolved into a solution of N-methylpyrrolidinone (NMP) to make a homogeneous solution. The slurry was coated onto a graphite foil and dried at ˜110° C. in a vacuum oven. Electrochemical characterization was conducted at room temperature using fabricated electrodes assembled in 2016 coin cells that were in turn assembled inside an argon-filled MBraun Inc. glove box (&lt;0.1 ppm each of O 2  and H 2 O) employing magnesium foil as a counter electrode and cellgard separator soaked in an electrolyte solution of 0.4 molar 2 (PhMgCl)—AlCl 3  in tetrahydrofuran. Cyclic voltammogram (CV) was performed using an electrochemical workstation (VersaSTAT 3, Princeton Applied Research) between 0.5-1.75 V at a constant sweep rate of ˜0.01 mVs −1 . Galvanostatic charge-discharge cycles were carried out employing various current rates of ˜20-120 mA/g within 0.5-1.5 V, with a short rest period between the charge/discharge cycles using a multichannel battery testing system (Arbin BT2000 instrument). 
     Results 
     The XRD patterns of the heat-treated powder obtained by the precursor route shows characteristic XRD peaks. The major diffraction peaks were indexed to the rhombohedral phase of Cu 2 Mo 6 S 8  (space group: R-3; number: 148; JCPDS-ICDD: 00-047-1519). Similarly, the XRD pattern of the powder obtained after acid removal of copper ions matches with the rhombohedral Mo 6 S 8  (space group: R-3; number: 148; JCPDS number: 00-027-0319). The exact match of the XRD patterns of pristine Cu 2 Mo 6 S 8  and acid leached Mo 6 S 8  phase compared with the standard XRD pattern suggests that the precursor route is a simple and convenient approach to the direct synthesis of Chevrel phase compounds. An impurity phase of MoS 2  (space group: P63/mmc, number: 194, JCPDS number: 01-073 1508) was observed in both Cu 2 Mo 6 S 8  and Mo 6 S 8  identified by the presence of peaks at 2θ=14.4°, 32.8°, and 39.6°. The SEM micrographs of the Cu 2 Mo 6 S 8  and Mo 6 S 8  powder materials showed that distinct micrometer-size cuboidal shape crystallites (˜0.5-2 μm) were formed. The crystallites were relatively smaller for the Mo 6 S 8  as compared to the Cu 2 Mo 6 S 8  phase. 
     Cyclic voltammogram at a scan rate ˜0.01 mVs −1  has been recorded between 0.5-1.75 V of the electrode (comprising 80% Mo 6 S 8 , 10% PVDF, 10% Super-P) in a 0.4 M THF/2(PhMgCl)—AlCl 3  electrolyte solution. The CV curve indicates a highly reversible behavior for magnesium-ion insertion/extraction in the Mo 6 S 8  phase similar to the expected electrochemical phenomena based on observations in the art. The anodic and cathodic peaks observed at ˜1.05 V and 1.17 V respectively, suggest Mg 2+  insertion/extraction into the Mg x Mo 6 S 8  (0&lt;x&lt;2) phase. It is established that Mg 2+  insertion into the Mo 6 S 8 , Chevrel phase occurs in two stages, but due to partial charge entrapment after the initial magnesiation only 60-80% magnesium-ion can be extracted during the first charge, resulting in 20-25% capacity loss compared to the theoretical value (128 mAhg −1 ). The loss in capacity may be salvaged if the electrochemical cell can be operated at an elevated temperature (˜60-80° C.). The galvanostatic charge-discharge profiles (1 st , 2 nd , 25 th  and 50 th  cycle) of the Mo 6 S 8  electrode performed at a constant current rate of ˜20 mAg −1  (˜C/6). During first discharge, electrochemical Mg 2+  insertion occurred into Mo 6 S 8  host, and offered a specific discharge capacity of ˜116 mAhg −1  (91% of theoretical value). During the 1 st  discharge curve, Mg 2+  insertion plateaus occurred at ˜0.9 V, whereas Mg 2+  extraction occurred at ˜1.2 V. The 2 nd , 25 th , and 50 th  cycles indicated only single reaction plateau at ˜1.1 V (Mg 2+  insertion) and at ˜1.2 V (Mg 2+  extraction), respectively. The cycling data suggested that the initial Mg 2+  insertion into Mo 6 S 8  was difficult and intrinsically very slow requiring a slight overvoltage of ˜200 mV compared to the subsequent cycles. The 1 st cycle discharge (˜116 mAhg −1 ) and charge capacity (˜104 mAhg −1 ) suggested ˜91% magnesiation and ˜81% demagnesiation occurred from the Mo 6 S 8  host (resulting in a 1 st  cycle irreversible loss ˜10.3%). Complete removal of Mg 2+  ion was not possible at room temperature due to the partial charge trapping in the Mo 6 S 8  host. The variation of specific capacity vs. cycle number along with coulombic efficiency of the Mo 6 S 8  electrode, cycled at a constant current of ˜20 mAg −1 (˜C/6 rate) in the potential window of 0.5-1.5 V shows that the 1 st  cycle discharge and charge capacity of the Mo 6 S 8  electrode is ˜116 mAhg −1  and 104 mAhg −1 , respectively, with a 1 st  cycle irreversible loss (FIR) of ˜10.3%. However, from the 2 nd  to the 50 th  cycle, it is shown that there was a steady charge and discharge capacity of ˜80 mAhg −1  and ˜76 mAhg −1  respectively, which resulted in an improved coulombic efficiency of ˜95%. This excellent capacity retention may be ascribed to the formation of high surface area cuboidal shaped ˜0.5-2 μm, Mo 6 S 8  particles, which allowed suitable wetting of the active material with the electrolyte promoting good charge transfer. The differential capacity plot (dQ/dV vs. V) of the 1 st , 2 nd , 25 th , and 50 th  cycle shows that during the 1 st  discharge and charge cycles, magnesiation/demagnesiation occurred at ˜0.92 V and at ˜1.17 V, respectively. A sharp peak is shown at ˜ 1.10 V (magnesiation) and at ˜1.17 V (demagnesiation) for the 2 nd , 25 th  and 50 th  cycles which was due to the known phenomena of partial entrapment of Mg 2+  ion after the 1 st  magnesiation (Mg 2 Mo 6 S 8 ) reaction which resulted in only one Mg 2+  ion cycling into/from the Mg x Mo 6 S 8  (0&lt;x≤1) host from the 2 nd  cycle and thereon. The differential capacity plot matched well with the charge-discharge profile of the electrode cycled at 20 mAg −1  which suggested excellent cyclability and reversibility of Mg 2+ insertion/extraction phenomena of the as-synthesized Mo 6 S 8  electrode in an Mg cell. 
     The excellent electrochemical rate performance was validated. The Mg/Mo 6 S 8  cell was cycled at various current rates. The results showed the rate capability of the Mo 6 S 8  electrode performed at current rates of 20 mAg −1  (˜C/6), 64 mAg −1  (˜C/2), 128 mAg −1  (˜C), and 192 mAg −1  (˜1.5 C). The capacity retention of the synthesized cuboidal Mo 6 S 8  via the novel precursor approach was excellent compared to literature reports of similar Chevrel phase compounds synthesized by published approaches. The discharge capacities at the above current rate was ˜76 mAhg −1 , 72 mAhg −1 , ˜68 mAhg −1 , and ˜66 mAhg −1  respectively. The coulombic efficiency at ˜C/6, ˜C/2, ˜1 C, and ˜1.5 C rate was 95%, 97.8%, 98.9%, and 99.3%, respectively. Although it is expected that coulombic efficiency decreases with increasing C-rate, the unique features of cuboidal Mo 6 S 8  (excellent electronic conductivity) rendered it suitable for fast insertion/extraction of Mg 2+  ions at ambient temperature with an improved coulombic efficiency in a Mg prototype cell. 
     Conclusions 
     In summary, unique cuboidal shape ˜0.5-2 μm size Cu 2 Mo 6 S 8 /Mo 6 S 8  Chevrel phase was synthesized by a rapid and facile precursor route. XRD confirmed the phase formation and the electrochemical measurements indicated superior performance, such as rate capability and stable specific capacity. The Mo 6 S 8  Chevrel phase exhibited extremely high rate capability and cycle performance when assembled in an Mg cell. The cell delivered a capacity of ˜66 mAhg −1  at ˜1.5 C rate making it suitable as a cathode for a magnesium-ion battery. 
     Example II 
     Stoichiometric amounts of MoS 2 , Mo, and CuS were batched in a SS vial (powder:ball ratio=1:10). The powders were mechanically milled for intervals of 1 hour, 2 hours and 3 hours, and subjected to XRD patterns. After 3 hours of milling, the powder was heat-treated at 1000° C./5 hours under UHP argon atmosphere. The X-ray diffraction patterns showed the synthesis of Cu 2 Mo 6 S 8  Chevrel-phase by the high energy mechanical milling route. The XRD patterns of the heat-treated powder also showed the formation of pure crystalline Cu 2 Mo 6 S 8 . The Cu 2 Mo 6 S 8  was washed with HCL/O 2  bubbling for 7 hours to yield completely crystalline Mo 6 S 8 . 
     Example III 
     Stoichiometric amounts of MoSe 2 , Mo, and CuSe were batched in a SS vial (powder: ball ratio=1:10). The powders were mechanically milled for intervals of 1 hour, 2 hours and 3 hours, and subjected to XRD patterns. After 3 hours of milling, the powder was heat-treated at 1000° C./5 hours under UHP argon atmosphere. The XRD analysis and patterns collected showed the synthesis of Cu 2 Mo 6 Se 8  Chevrel-phase by the high energy mechanical milling route. Further, the XRD patterns of the heat-treated powder showed the formation of pure crystalline Cu 2 Mo 6 Se 8 . The Cu 2 Mo 6 Se 8  was washed with HCL/O 2  bubbling for 7 hours to yield completely crystalline Mo 6 Se 8 . 
     Example IV 
     Novel amidomagnesium-based electrolytes at varying molar ratios were compared with Aurbach&#39;s 1 st  and 2 nd  generation electrolytes by conducting cyclic voltammetry. The electrochemical parameters obtained from the cyclic voltammograms conducted at a 25 mvs −1  scan rate using amidomagnesium-based novel electrolytes at different molar ratios are compared with Aurbach&#39;s 1 st  generation electrolyte (i.e., 0.25 molar Mg(AlCl 2 EtBu) 2 /THF) and 2 nd  generation electrolyte (i.e., 0.4 molarPhMgCl)—AlCl 3 /THF) are shown in Table 1. 
     
       
         
           
               
             
               
                 TABLE 1 
               
             
            
               
                   
               
               
                 Electrochemical parameters obtained from the cyclic  
               
               
                 voltammograms conducted at 25 mVs −1  scan rate using novel  
               
               
                 amidomagnesium based electrolytes at different molar ratio 
               
               
                 and compared with Aurbach&#39;s 1 st  and 2 nd  generation electrolyte. 
               
            
           
           
               
               
               
               
            
               
                   
                 Onset 
                 Anodic 
                   
               
               
                   
                 deposition 
                 stripping peak 
                 Mg cycling 
               
               
                 base/acid ratio 
                 potential (V) 
                 potential (V) 
                 efficiency (%) 
               
               
                   
               
            
           
           
               
               
               
               
            
               
                 1:1 
                 −0.283 
                 0.983 
                 93.2 
               
               
                 2:1 
                 −0.242 
                 0.842 
                 63.7 
               
               
                 3:1 
                 −0.351 
                 0.401 
                 56.5 
               
               
                 1:2 
                 −0.193 
                 1.032 
                 95 
               
               
                 (1 st  generation) 
                   
                   
                   
               
               
                 2:1 
                 −0.37 
                 0.643 
                 85.5 
               
               
                 (2 nd  generation) 
                   
                   
                   
               
               
                   
               
            
           
         
       
     
     The 1:1 (Lewis base:Lewis acid ratio) electrolyte conducted at a scan rate of 25 mVs −1  demonstrated enhanced performance for all of the novel electrolytes in accordance with the invention. Further, Table 1 suggests that the coulombic efficiency for reversible magnesium deposition/dissolution was near or about 93% for the 1:1 electrolyte. The coulombic efficiency for the 2:1 and 3:1 electrolytes was about 64% and about 56%, respectively. 
     The linear sweep voltammograms obtained at a scan rate of 1 mVs −1  from open circuit potential to approximately 4 V showing the anodic stability onto Pt working electrode of the novel amidomagnesium-based electrolytes at varying molar ratios as compared with Aurbach&#39;s 1 st  and 2 nd  generation electrolyte. The linear sweep voltammograms of the above-mentioned electrolytes from open circuit potential to about 4 V at 1mVs −1  showed that the electrochemical stability of the amidomagnesium-based novel electrolytes of 1:1, 2:1 and 3:1 was about 2.27, about 2.33 and about 2.19 V, respectively, onto noble metal (e.g., platinum electrode). The electrochemical stability of the novel electrolyte was similar to Aurbach&#39;s 1 st  generation electrolyte but significantly lower than Aurbach&#39;s 2 nd  generation electrolyte. 
     Example V 
     A Mo 6 S 8  cathode was tested in a 2016 coin cell using 0.4 M 3((3-bis(trimethylsilyl)amino)phenylmagnesium chloride)-AlCl 3 THF (3:1 novel electrolyte). The electrochemical performance in particular when conducted at a current rate of 20 mAg −1  and cyclic voltammetry employing a scan rate of 100 microvolts per second (1000/s −1 ) showed a 1 st  cycle irreversible loss of about 40% and stable discharge capacity about 37 mAhg −1  at C/6 rate with coulombic efficiency about 90%. 
     Example VI 
     A Mo 6 S 8  cathode was tested in a 2016 coin cell using 0.4 M 2((3-bis(trimethylsilyl)amino)phenylmagnesium chloride)-AlCl 3 THF (2:1 novel electrolyte). The electrochemical performance in particular when conducted at a constant current of 20 mAg −1  and a scan rate of 100 microvolts per second (1000/s −1 ) showed a 1 st  cycle irreversible loss of about 48% and stable discharge capacity about 54 mAhg −1  at C/6 rate with coulombic efficiency about 88%. 
     Example VII 
     A Mo 6 S 8  cathode was tested in a 2016 coin cell using 0.4 M ((3-bis(trimethylsilyl)amino)phenylmagnesium chloride)-AlCl 3 THF (1:1 novel electrolyte). The electrochemical performance in particular when cycled at a constant current of 20 mAg −1  and a scan rate of 100 microvolts per second (1000/s −1 ) showed a 1 st  cycle irreversible loss of about 26% and stable discharge capacity about 60 mAhg −1  at C/6 rate with coulombic efficiency about 99%. 
     Example VIII 
     Cu 2 Mo 6 S 8  (Cu 2 CP) Chevrel phase was developed by High Energy Mechanical Milling (HEMM) route. Stoichiometric amounts of MoS 2 , Mo, and CuS were batched in a SS vial (powder:ball ratio=1:10). The powders were mechanically milled for 1 hour, 2 hour, and 3 hour intervals and subjected to XRD analysis to collect the XRD patterns. After 3 hours of high-energy mechanical milling (HEMM), the powder was heat-treated at 1000° C./5 h under UHP Ar atmosphere. XRD pattern of the heat-treated powder collected showed the formation of pure crystalline Cu 2 Mo 6 S 8 . Further, Cu 2 Mo 6 S 8  was washed with HCl/O 2  bubbling for 7 hours yields to obtain completely crystalline Mo 6 S 8  (CP). 
     It was established that Mg 2+  insertion into Mo 6 S 8  Chevrel phase occurred in two stages, and theoretically could offer a capacity ˜128 mAhg −1 . However, due to partial charge entrapment after initial magnesiation, only 50-60% magnesium-ion could be extracted during first charge, resulting in 40-50% irreversible loss in the 1 st  cycle from the theoretical value (˜128 mAhg −1 ). In order to minimize the 1 st  cycle irreversible loss, Cu was partially leached from the original Cu 2 CP structure. 1.8 g of Cu 2 CP was added in 20 ml 6M HCl solution in a small glass vial with a magnetic stir bar. Cu 2 CP/HCl solution was continuously stirred for 2 days at room temperature. After 2 days of continuous stirring, the solution was ultrasonically cleaned using distilled water (3 times) and dried at a temperature of 60° C. for 24 hours. XRD pattern of the partial leached Cu 2 CP collected showed the formation of completely crystalline partially de-cuprated, CuMo 6 S 8  (Cu 1 CP). 
     Results 
     The XRD patterns were collected on Cu 2 Mo 6 S 8  (Cu 2 CP) powder obtained by high energy mechanical milling of CuS, MoS2 and Mo stoichiometric compositions followed by heat treatment at 1000° C./5 h under UHP Ar, and acid leached CuMo 6 S 8  (CuCP) obtained after 2 days partial leaching of copper using 6M HCl solution. The Bragg diffraction lines were indexed to a hexagonal-rhombohedral symmetry unit cell of Cu 2 Mo 6 S 8  (space group: R-3; number: 148; JCPDS-ICDD: 00-047-1519). Lattice parameter(s) calculated using least-square method of the experimental data (a=0.96478 nm, c=1.02026 nm, and unit cell volume=822.42×10 −3  nm 3 ) was in good agreement with the standard Cu 2 Mo 6 S 8  unit cell parameters (a=0.9584 nm, c=1.025 nm, unit cell volume=815.36×10 −3  nm 3 ). Similarly, the XRD pattern obtained after removal of one copper from the heat-treated powder using hydrochloric acid treatment matched with the JCPDS patterns. The Braggs lines were indexed with the hexagonal-rhombohedral symmetry unit cell of CuMo 6 S 8  phase (space group: R-3; number: 148; JCPDS-ICDD: 00-034-1379), and the calculated lattice parameter(s) (a=0.94412 nm, c=1.04761 nm, and unit cell volume=808.70×10 −3  nm 3 ) matched quite well with standard unit cell parameters of CuMo 6 S 8  obtained from above ICDD database (a=0.94120 nm, c=1.04070 nm, unit cell volume=798.40×10 −3  nm 3 ). The calculated lattice parameters values were consistent with the standard lattice parameter(s) values of pristine Cu 2 Mo 6 S 8  and acid leached CuMo 6 S 8  powder obtained from JCPDS-ICDD database suggested that 6M HCl treatment for 2 days leached 50% copper from the original Cu 2 CP structure and yielded CuMo 6 S 8  (CuCP). 
     The variation of specific capacity versus cycle number along with coulombic efficiency of the CuMo 6 S 8  electrode, cycled at a constant current of ˜20 mAg −1  (˜C/6 rate) in the potential window of 0.5-1.5 V using 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte showed that the 1 st  cycle discharge and charge capacity of the CuMo 6 S 8  electrode was ˜105 mAhg −1  and ˜78 mAhg −1 , respectively, with a 1 st  cycle irreversible loss (FIR) of 25.7% (or coulombic efficiency of ˜74.3%). It is to be noted that, the 1 st  cycle irreversible loss (FIR) of Mo 6 S 8  is ˜50% obtained by completely leaching out copper from the HEMM derived Cu 2 CP structures. Further, from 10 th  cycles onward there was a steady charge-discharge capacity of ˜55 mAhg −1 , with a coulombic efficiency of ˜99.9%. The preliminary results of CuCP suggested that partial Mg 2+  charge entrapment which is common during 1 st  cycle magnesiation (discharge) in Mo 6 S 8  cathode may be overcome with CuMo 6 S 8  structure where one Mg 2+  can cycle without any hindrance. 
     The HEMM derived Mo 6 Se 8  cathode assembled in a 2016 coin cell using Mg metal anode, 0.4 molar 2 (PhMgCl)—AlCl 3 /tetrahydrofuran electrolyte exhibited a ˜17% capacity fade after 100 cycles. The exact reason of fading is still under investigation. However, in order to improve the electrical conductivity of the Mo 6 Se 8  cathode, it was mixed with conductive graphite and coated with Mg 2+  conducting MgSO 4  and used as composite cathode. 
     Example IX 
     The Cu 2 Mo 6 Se 8  (Cu 2 CP) Chevrel phase developed by 3 hours of High Energy Mechanical Milling (HEMM) of stoichiometric amounts of MoSe 2 , Mo, and CuSe was followed by heat-treatment at 1000° C./5 h under UHP Ar atm, were further mixed with commercial available synthetic graphite (SigmaAldrich, 1-2 m) in situ during milling process at 70:30 ratio (weight percent) and used as composite cathode for magnesium battery. Further, Cu 2 Mo 6 Se 8 /graphite was washed with HCl/O 2  for 7 hours to develop Mo 6 Se 8 /graphite composite cathode. 
     Example X 
     Mo 6 Se 8  Chevrel-phase obtained after the complete removal of copper from HEMM derived Cu 2 Mo 6 Se 8  was mixed thoroughly with previously prepared water solution of commercially available MgSO 4  (Aldrich, 99.9%) at 70:30 ratio (weight percent). Further the mixed slurry was dried at 60° C. for 24 hours and used as MgSO 4  coated Mo 6 Se 8  cathode for magnesium battery. 
     Example XI 
     Electrochemical impedance spectroscopy (EIS) was carried out on a Mo 6 S 8  electrode before and after cycling to evaluate Mg 2+ -ion charge storage mechanisms. EIS was performed using a Versastat 3 (Princeton Applied Research Inc.) potentiostat over a frequency range of 0.01 Hz-100 KHz. An A.C. amplitude of 5 mV was used and the spectra were obtained before cycling and subsequent to 1 st  and 2 nd  discharge cycle. Electrode potential was stabilized after discharge cycle and EIS was performed (i.e., immediately such that no significant relaxation processes and equilibrium phase changes occurred) to observe any noticeable changes in the charge storage mechanism upon cycling. The effect of cycling on charge transfer parameters was also analyzed by performing EIS. Z-View (Scribner Associates, Inc.; version 3.3) software was used for Randall&#39;s equivalent circuit modeling of the experimentally collected impedance spectra. 
     Results 
     Electrochemical impedance study (EIS) was performed on a newly prepared Mo 6 S 8  electrode (wet chemical route) as well as cycled Mo 6 S 8  electrode at the magnesiated (discharged) and de-magnesiated (charged) states assembled in a 2016 coin cell using magnesium foil as the counter and reference electrodes, Mo 6 S 8  composite electrode as the working electrode and 0.4 molar 2 (PhMgCl)—AlCl 3  in tetrahydrofuran as the electrolyte. A Nyquist plot was generated for the electrode prepared using the Chevrel phase (Mo 6 S 8 ) at different stages. A clear transition in behavior was observed upon cycling. The impedance behavior was modeled using a Randall&#39;s circuit which considered a number of electrochemical phenomena including:
         a) High frequency series resistance (R s );   b) High frequency semi-circle (HFS) due to sluggish charge and electron transfer kinetics (CPE e  and R e );   c) Gerischer impedance as a result of the coupling of a chemical and an electrochemical process (GE);   d) Low frequency semi-circle (LFS) due to Mg-ion trapping in the Chevrel phase (Mo 6 S 8 ) host (CPE i  and R i ); and   e) Diffusion characteristic and associated ion-trapping (W o , R trap , CPE trap ).       

     A model including all of these elements can be used for circuit modeling. The model employed considered both charge transfer and mass transfer phenomena contributing to the electrode impedance. The circuit also included constant phase elements (CPEs) due to the porous nature of the electrodes. In addition, it was found that the Gerischer impedance element (GE) was very small and insignificant for the electrode. 
     With respect to the effect of insertion/extraction on the impedance profile of the electrode materials, it was observed that the material exhibited a significant increase in overall impedance following the initial Mg 2+ -ion insertion after the 1 st  discharge cycle. Table 2 depicts the values of resistances obtained as a result of Randall&#39;s circuit modeling. The solution resistance (R s ) was almost invariable. The charge transfer resistance (R e ) which is a characteristic of electron and ion transfer differed, pre- and post-Mg 2+ -ion insertion stage. There was a drop in Re post 1 st  discharge and an increase from subsequent to 2 nd  discharge. Interfacial resistance increased post 1 st  discharge and decreased subsequent to 2 nd  discharge. Charge trapping (R trap ) which remained very small before cycling and post 1 st  discharge, increased by almost 8 orders, post 2 nd  discharge. The transition in these three parameters provided information with respect to the Mg +  charge storage mechanisms occurring in the Chevrel phase. The significant increase in overall impedance subsequent to first discharge indicated that the Mg 2+ -ion insertion was accompanied by a rate limiting phenomenon. This, in turn, was seen by the two order rise in interfacial resistance (R i ) subsequent to 1 st  discharge. The electrode resistance, however, maintained the same order indicating that post-insertion in the 1 st  discharge cycle, the electrode became kinetically limiting for electrochemical charge transfer processes as a result of the formation of either a secondary interface or a phase change. After the 2 nd  discharge, however, the R i  was small but R trap  and Re increased indicating that part of the layer was either inactive or became a barrier to solid state diffusion of Mg 2+ . Without intending to be bound by any particular theory, this mass transfer limitation and loss in magnesium trapped irreversibly as a result of the phase change occurring in the 1 st  discharge cycle, was believed to be the reason for the low capacity occurring from the 2 nd  cycle onward. 
     
       
         
           
               
             
               
                 TABLE 2 
               
             
            
               
                   
               
               
                 Charge transfer parameter(s) of the Chevrel phase electrode at different stages obtained from Randall circuit model. 
               
            
           
           
               
               
               
               
               
               
               
               
               
               
               
               
               
               
               
               
            
               
                   
                   
                 CPE e - 
                 CPE e - 
                   
                 CPE i - 
                 CPE i - 
                   
                 GE- 
                 GE- 
                 W o - 
                 W o - 
                 W o - 
                   
                 CPE trap - 
                 CPE trap - 
               
               
                   
                 R s   
                 T 
                 P 
                 R e   
                 T 
                 P 
                 R i   
                 T 
                 P 
                 R 
                 T 
                 P 
                 R trap   
                 T 
                 P 
               
               
                   
                   
               
            
           
           
               
               
               
               
               
               
               
               
               
               
               
               
               
               
               
               
            
               
                 Before 
                 10.27 
                 8.03E−06 
                 0.974 
                 286.4 
                 8.49E−06 
                 1.009 
                 53.28 
                 0.693 
                 0.134 
                 5.041 
                 4.22E−06 
                 0.393 
                 2.32E−04 
                 1.318E−04 
                 0.125 
               
               
                 cycling 
               
               
                 After 
                 12.36 
                 4.88E−06 
                 0.941 
                 182.6 
                 7.23E−05 
                 0.821 
                 9748 
                 5.195 
                 0.089 
                 0.205 
                 1.61E−07 
                 0.416 
                 3.01E−05 
                 1.287E−04 
                 0.294 
               
               
                 1 st   
               
               
                 dis- 
               
               
                 charge 
               
               
                 After 
                 12.94 
                 4.29E−05 
                 0.76 
                 921.2 
                 1.14E−05 
                 0.881 
                 65.09 
                 3.849 
                 0.728 
                 0.135 
                 1.08E−07 
                 0.375 
                 8855 
                 5.813E−04 
                 0.479 
               
               
                 2 nd   
               
               
                 dis- 
               
               
                 charge 
               
               
                   
               
            
           
         
       
     
     Example XII 
     The electrochemical behavior and stability of amidomagnesium-based three non-aqueous electrolyte 0.4 molar [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]—AlCl 3 /THF were investigated using both a three-electrode electrochemical cell and coin cells. The cyclic voltammetry, linear sweep voltammetry, and coin cell charge/discharge measurements indicated that the electrolyte is capable of reversibly cycling magnesium with a Coulombic efficiency ˜90% and electrochemical stability ˜2.3V. Reversible cycling of magnesium from the amidomagnesium-based electrolytes were proved by scanning electron microscopy (SEM), and energy-dispersive X-ray spectroscopy (EDX) analyses. SEM and EDX show that uniform spherical magnesium particles (1-5 m) free from any dendrites formation deposited on platinum substrate. Moreover, Mo 6 S 8  cathode derived by molten salt and high energy mechanical milling route able to deliver a first cycle discharge capacity ˜120-128 mAhg −1  demonstrate the feasibility of the system as potential 2V magnesium battery electrolyte. 
     1 molar [(CH 3 ) 3 Si] 2 NC 6 H 4 MgCl] salt in THF solution was transmetallated with 1 molar AlCl 3 /THF in-house solution at three different Lewis base-acid molar ratio of 1:1, 2:1 and 3:1 and studied the electrochemical behavior using cyclic voltammetry, chronopotentiometry, linear sweep voltammetry, and galvanostatic charge-discharge cycles. Electrochemical data shows that amiodomagnesium-based electrolyte is electrochemically stable up to 2.3V and capable of delivering 100% theoretical capacity (˜128 mAhg −1 ) from Mo 6 S 8  Chevrel phase cathode at room temperature. 
     Experimental Section 
     Synthesis of 0.4 Molar L −1 [(CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]—AlCl 3 /THF Electrolyte 
     The starting chemical of [(CH 3 ) 3 Si] 2 NC 6 H 4 MgCl] (1 molar in tetrahydrofuran) was purchased from Sigma Aldrich and used without further purification. Highly pure inhibitor-free anhydrous tetrahydrofuran (THF) was obtained from EMD Millipore and further dried (using Na chips and benzophenone) under ultra high purity Argon atmosphere using stringent drying steps outlined in the literature. Anhydrous AlCl 3  (99.999%) powder in glass ampoules was obtained from Sigma Aldrich and used as-received. First, 1 molar AlCl 3 /THF was prepared where ˜2 g AlCl 3  was gradually added in an anhydrous THF (˜-15 ml) through a powder addition funnel inside a Schlenk flask under constant stirring. The above reaction is exothermic and a light yellowish solution was obtained after the reaction was over. The electrolyte of chemical formula 0.4 molar L −1  [(CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]—AlCl 3 /THF at different molar ratio was synthesized according to the following method. Stoichiometric amounts of [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl] (1 molar in THF) and AlCl 3  (1 molar in THF) (1:1, 2:1, and 3:1 Lewis base/Lewis acid ratio in volume) were added in a 25 ml clear glass vial. The mixture was continuously stirred for ˜2 h inside the glass vial closed with a screw threaded cap. After 2 h reaction, the screw cap was carefully opened and the electrolyte solution was diluted using anhydrous tetrahydrofuran (THF), resulting in the formation of 0.4 molar L −1  [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]—AlCl 3 /THF electrolyte. The electrolyte preparation was carried out inside an MBraun Inc. glove box where the oxygen and moisture levels are always maintained &lt;0.1 ppm. 0.25 molar L −1 Mg(AlCl 2 EtBu) 2 /THF (butyl-ethyl complex or BEC) as well as 0.4 molar L −1  2(PhMgCl)—AlCl 3 /THF (all-phenyl complex or APC) were also synthesized as reference electrolytes according to the standard protocol outlined in literature. 
     Characterization 
     Electrochemical analyses, including linear sweep voltammetry (LSV) and cyclic voltammetry (CV) were carried out on a CHI660D electrochemical station. The electrochemical cell used in the LSV and CV study was a three electrode cell which consisted of a working electrode (Pt), counter electrode (Mg), and reference electrode (Mg). The scan speed of the test was set to 10, 25, and 50 mV/s within −1V to +2.2V potential ranges. Deposition/dissolution efficiency of Mg on to Pt electrode was carried out in 2016 coin cells at a constant current density of 0.25 mAcm −2  for 1 hour deposition and −0.25 mAcm −2  for 1 hour dissolution for chronopotentiometic measurements. The three electrode cells were assembled with the Pt working electrode, woven fiberglass (GFD separator), Mg counter and reference electrode, and 0.4 M L −1  [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]—AlCl 3 /THF electrolyte. 
     Scanning electron microscopy (SEM) and energy-dispersive X-ray spectroscopy (EDX) were performed using a Philips XL-30 operating at an accelerating voltage of 20 kV. It is noted that the electrodes were washed by copious amount of THF three times and dried in vacuum before SEM and EDX analysis. The conductivity of the synthesized electrolyte was measured by a portable conductivity meter (HI991301, HANNA). 
     Results and Discussions 
     Amidomagnesium halide-based Grignard reagent of the formula [3-[bis(trimethylsilyl)amino]phenylmagnesium chloride [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl] solution in 1.0 THF was identified as a potential salt for the synthesis of ma mangsium battery electrolyte. The chronopotentiogram of the 1 st  cycle plating and stripping on platinum substrate using 1 mol L −1  [(CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]/THF solutions demonstrated the expected reversibility of Mg&#39;. Metallic magnesium was reversibly plated onto platinum and stripped versus Mg 2+ /Mg couple in a three electrode cell at a constant current rate of ˜0.1 mA/cm 2  for 1 h. It was observed that the overpotential for magnesium plating (−0.123V versus Mg 2+ /Mg) and stripping (0.103V versus Mg/Mg 2+ ) was low and Coulombic efficiency ˜75% was observed suggest that the [(CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]/THF Grignard reagent based solvent is capable of cycling Mg-ion in a reversible manner. Cyclic voltammetry study of this amiodomagnesium-based solvent using platinum as working electrode and magnesium being counter and reference electrode in a three electrode cell further prove our hypothesis. The cell was first run from open circuit potential to −1V (for Mg deposition) followed by −1V to 2.2V (for Mg stripping) using different voltage scan rate. The cyclic voltammogram at different scan rates (10, 25 and 50 mV/s) between −1 to 2.2 V showed the obvious reversible magnesium deposition/dissolution which occurred within the potential window of ˜2.2V. The onset potential for 1 st  cycle Mg deposition was −0.192V, −0.243V and −0.293V for 10 mVs −1 , 25 mVs −1  and 50 mVs −1  scan rate respectively (see Table 1). The increase in onset potential with increasing voltage scan rate is due to solution resistance and increasing kinetic barriers with high charge transfer rate that exist in any standard electrochemical cell. A typical charge balance during cathodic plating and anodic stripping of the 1 mol L −1  [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]/THF solutions showed ˜65% cyclic efficiency. Table 1 shows the onset deposition potential and the magnesium cyclic efficiency of the 1 mol L −1  [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]/THF solutions at different scan rate. It appears that the 1 mol L −1  [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]/THF Grignard reagent has some potential benefits like the electrochemical stability window ˜1.5V but the Coulombic efficiency is very low (˜65%). However, preliminary electrochemical data suggest that [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]/THF is a Grignard reagent based Lewis base is a promising system which can be transmetallated with a strong Lewis acid (AlCl 3 , BF 3  etc.) in order to improve its electrochemical performance as Aurbach et al. mentioned in literature. This prompted our interest to synthesize amidomagnesium-based electrolyte by transmetallation of the amidomagnesium chloride [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl] with a strong Lewis acid (AlCl 3 ) at different base/acid ratio and further dissolving the reaction product in tetrahydrofuran at different molar level and study their electrochemical performance. 
     Three different electrolytes were synthesized at three different base/acid ratio (we will call it 1:1, 2:1, and 3:1 electrolyte) as listed in Table 3. 
     
       
         
           
               
             
               
                 TABLE 3 
               
             
            
               
                   
               
               
                 Electrochemical parameters of amidomagnesium based  
               
               
                 electrolyte compared with BEC and APC electrolyte including  
               
               
                 the anodic stability of the electrolytes on Pt working electrode. 
               
            
           
           
               
               
               
               
               
            
               
                   
                 Onset 
                 Anodic  
                 Mg cycling 
                 Anodic stability 
               
               
                 base/acid 
                 deposition 
                 stripping peak  
                 efficiency  
                 limit in Pt 
               
               
                 ratio 
                 potential (V) 
                 potential (V) 
                 (%) 
                 (1 &gt; 100 μAcm −2 ) 
               
               
                   
               
            
           
           
               
               
               
               
               
            
               
                 1:1 
                 −0.283 
                 0.983 
                 93.2 
                 2.27 
               
               
                 2:1 
                 −0.242 
                 0.842 
                 63.7 
                 2.33 
               
               
                 3:1 
                 −0.351 
                 0.401 
                 56.5 
                 2.19 
               
               
                 1:2 (BEC 
                 −0.193 
                 1.032 
                 95 
                 2.2 (known) 
               
               
                 electrolyte) 
                   
                   
                   
                   
               
               
                 2:1 (APC 
                 −0.37 
                 0.643 
                 85.5 
                 3.0 (known) 
               
               
                 Electrolyte 
                   
                   
                   
                   
               
               
                   
               
            
           
         
       
     
     In order to validate the quality of the amidomagnesium-based three different electrolytes, it was first evaluated by cyclic voltammetry (CV) study using a three-electrode cell. The first five cycles of CV within the potential window −1 V to 2.2V performed using platinum working electrode, magnesium counter and reference electrode in 0.4M L −1  [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]—AlCl 3 /THF electrolyte family demonstrated that deposition and dissolution of magnesium in the present system is highly reversible with a 1 st  cycle deposition-dissolution efficiency of ˜93% for 1:1 electrolyte (Table 1). On the contrary, 1 st  cycle magnesium deposition-dissolution efficiency was ˜63% and ˜56% for 2:1 and 3:1 electrolytes, respectively. From the 2 nd -5 th  cycles magnesium deposition/dissolution efficiency increased to ˜77% and ˜85% for 2:1 and 3:1 electrolytes, respectively. The cycling efficiency for magnesium deposition-dissolution was calculated from total charge balance during reduction/oxidation for each half-cycle as described in an earlier publication. The overpotential for the deposition was observed to be −0.23V and remain steady from the 1 st  to 5 th  cycles for 1:1 electrolyte. In the case of 2:1 and 3:1 electrolytes, overpotential for the deposition was −0.24V and −0.35V respectively. The decrease in overpotential and the increasing deposition-dissolution efficiency of magnesium from the 2 nd  cycle onwards may be ascribed to the desorption of electrolyte on the working electrode. Importantly, a cyclic voltammetry study showed a minimum 5-fold increase in total current density for magnesium deposition and dissolution which suggest that transmetallation of amidomagnesium-based Grignard reagent with AlCl 3  increases number of active ionic-species in the electrolytes for Mg-ion transport. 
     The magnesium deposition and dissolution reactions on platinum substrate could be repeated hundreds of times for 1:1, 2:1, and 3:1 electrolytes as confirmed for 0.4 molar [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]—AlCl 3 /THF (1:1) electrolyte solution. The first three cycles for magnesium deposition-dissolution obtained from 1:1, 2:1 and 3:1 electrolytes at a given current rate of ˜0.25 mAcm −2  for 15 minutes (0.225 Ccm −2 ), respectively, showed that the overpotential for 1 st  cycle deposition drops drastically to a lower voltage from open circuit potential, however, the voltage steadied after 10-15 seconds. For 1:1, 2:1, and 3:1 electrolyte, the overpotential for the deposition were −0.15V, −0.06V and −0.07V for the first three cycles and dissolution were 0.1V, 0.05V, and 0.04V respectively. Low overpotential for magnesium deposition-dissolution observed from the chronopotentiogram suggested that the magnesium-ion transport was amenable in the above electrolytes. Galvanostatic cycling for the first 100 cycle magnesium deposition-dissolution on the platinum substrate gave a reoxidation cycling efficiency of ˜89% and ˜83%, respectively, for 1:1 and 2:1 electrolytes. The reoxidation cycling efficiency of 3:1 was found to fluctuate between ˜60-80% for the first 50 cycles and then steadily increased to ˜88%. In all the three cases, the reoxidation cycling efficiency was found to increase steadily from the 1 st  to 20 th  cycle may be due to desorption of electrolyte and electroactive species on the working electrode. In order to confirm the deposit structure, magnesium was electrodeposited on a platinum substrate from the three different amidomagnesium-based electrolytes at 0.5 mAcm −2  for 1 hour (1.8 Ccm −2 ). SEM image analysis of the platinum substrate after 1 hour deposition from 2:1 electrolyte reflected the presence of pronounced spherical particles of 1-5 μm on the surface. An EDX full frame analysis of the SEM image confirmed that the spherical particles were magnesium. The uniform spherical magnesium deposition morphology is extremely important for practical use of the electrolytes because it ensures the lack of dendrite formation in battery systems. 
     The electrochemical performance of the three amidomagnesium-based electrolytes at varying molar ratios was compared with BEC and APC electrolytes. The electrochemical parameters obtained from the cyclic voltammograms conducted at a 25 mVs −1  scan rate are shown in Tables 1 and 2 including the cyclic voltammograms of the amidomagnesium-based electrolytes with a direct comparison with BEC (i.e., 0.25 molar Mg(AlCl 2 EtBu) 2 /THF) and APC (i.e., 0.4 molar 2(PhMgCl)—AlCl 3 /THF) electrolyte. The 1:1 (Lewis base:Lewis acid ratio) amidomagnesium-based electrolyte demonstrated enhanced performance among all the amidomagnesium-based electrolytes synthesized. It showed a 1 st  cycle Coulombic efficiency ˜93% and was in excellent agreement with chronopotentiometic measurements. Table 2 lists the electrochemical parameter(s) obtained from the linear sweep voltammograms (LSV) performed at a scan rate of 1 mVs −1  from open circuit potential to approximately 4V showing the anodic oxidative stability of the amidomagnesium-based electrolytes onto platinum working electrode compared with known anodic stability of ˜2.2V and ˜3V for BEC and APC electrolytes, respectively. It was found that the electrochemical stability of the amidomagnesium-based novel electrolytes was ˜2.27V, ˜2.33V and ˜2.19V for 1:1, 2:1 and 3:1 electrolytes, respectively. The electrochemical anodic stability of the amidomagnesium-based electrolyte was similar to Aurbach&#39;s BEC electrolyte but significantly lower than APC electrolyte. 
     In order to validate the feasibility of the amidomagnesium-based electrolyte solutions for a magnesium battery system, Mo 6 S 8  Chevrel phase a known magnesium-ion intercalation cathode was synthesized by molten salt (MS) route found in literature and high energy mechanical milling (HEMM) route first time reported. The 2016-type coin cell was constructed using the 0.4M L −1  [(CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]—AlCl 3 /THF solution as the electrolyte (3:1 molar ratio), a Mg disc as a negative electrode, and Mo 6 S 8  as a positive electrode. The 2016 coin cells were cycled at a current rate of ˜C/6 (˜20 mAg −1 ) with the discharge and charge voltage limits of 0.5V and 1.5V versus Mg reference electrode at room temperature. The results showed that the 1 st  cycle discharge and charge capacity was ˜128 mAhg −1  (100% of theoretical capacity) and ˜70 mAhg −1  with 1 st  cycle Coulombic efficiency ˜54.8% for HEMM derived Mo 6 S 8  cathode. The expected drop in 1 st  cycle capacity was due to partial charge trapping which occurred in the Mo 6 S 8  electrode during 1 st  cycle. Nevertheless, Mo 6 S 8  electrode derived by MS and HEMM method was able to cycle magnesium reversibly and yield a discharge capacity of ˜66 mAhg −1  and ˜60 mAhg −1  calculated based on the weight of the cathode&#39;s active mass with Coulombic efficiency ˜97% and ˜95% respectively, between 2 nd  and 50 th  cycle. Typical cyclic voltammogram conducted between 0.5-1.5V at a scan rate of 0.1 mVs −1  shows cathodic and anodic peak at ˜1.0V and ˜1.3V due to formation of Mg x Mo 6 S 8  (0&lt;x≤1) phase. 
     Conclusions 
     In summary, we have synthesized a ˜2.3V amidomagnesium based magnesium electrolyte system based on the Lewis base˜acid complex via a reaction between organometallic Grignard reagent [CH 3 ) 3 Si] 2 NC 6 H 4 MgCl] and AlCl 3  in tetrahydrofuran solvent. The [(CH 3 ) 3 Si] 2 NC 6 H 4 MgCl]—AlCl 3 /THF electrolyte solution shows excellent reversibility of Mg deposition˜dissolution (˜90% cycling efficiency for reversible magnesium deposition), and electrochemical anodic stability (2.3V vs. Mg reference electrode). In addition, the good compatibility of the amiodomagnesium-based electrolyte solution with the Mo 6 S 8  intercalation cathode derived by the molten salt as well as the high energy mechanical milling routes confirms that the electrolyte could be practically used in 2V rechargeable Mg battery systems. 
     Example XIII 
     High energy mechanical milling (HEMM) of a stoichiometric mixture of molybdenum and copper chalcogenide (CuT and CuT 2 ), followed by a short thermal treatment at elevated temperature was applied to synthesize Chevrel phases (Cu 2 Mo 6 Z 8 ; Z═S, Se), a cathode precursor for magnesium battery. Differential scanning calorimetry, thermo-gravimetric analyses, combined with X-rays diffraction and scanning electron microscopy was used to evaluate the phase transformation(s) during milling and thermal treatment. It was shown that CuS and Mo reacted at elevated temperature and formed an intermediate ternary Chevrel phase which further reacted with residual Mo and MoS 2  to form the desired Cu 2 Mo 6 S 8 . Quantitative XRD analyses showed the formation of ˜96-98% Chevrel phase as low as 30 minutes time during post milling thermal treatment process. Electrochemical performance of de-cuprated Mo 6 S 8  and Mo 6 Se 8  phase were evaluated by cyclic voltammetry (CV), galvanostatic cycling, electrochemical impedance spectroscopy (EIS). CV and galvanostatic cycling data of Mo 6 S 8  and Mo 6 Se 8  electrodes showed expected anodic/cathodic behavior and a stable capacity after the 1 st  cycle with the formation of Mg x Mo 6 Z 8  (Z═S, Se; x=1≤x≤2). EIS at ˜0.1 V intervals of Mo 6 S 8  electrode during 1 st  and 2 nd  cycle showed that partial Mg-ion trapping caused increased charge transfer resistance, R e . Carbon incorporation during milling resulted in improved capacity fade in the case of Mo 6 Se 8  electrode and 99.93% Coulombic efficiency was achieved. Importantly, ease of fabrication, stable capacity, high Coulombic efficiency and excellent rate retention rendered HEMM-derived Chevrel phases as suitable magnesium battery cathodes for stationary electrical energy storage (EES) applications. 
     Electrochemical performance of HEMM-derived Mo 6 S 8  and Mo 6 Se 8  phase devoid of copper was evaluated in 2016 coin cell by cyclic voltammetry, and galvanostatic cycling at various C-rates. The Chevrel phase(s) exhibited competitive electrochemical results and provided a time saving, rapid approach. 
     Materials Synthesis 
     Cu x Mo 6 S 8  was synthesized as follows using an HEMM approach in accordance with certain embodiments of the invention. Stoichiometric amounts of MoS 2  (1 g, 99% Alfa Aesar), Mo (0.6 g, 99.9% Alfa Aesar), and CuS (0.4 g, 99.8% Alfa Aesar) were batched in a stainless steel vial (powder:ball ratio=1:10). The powders were mechanically milled in atmospheric condition for 30 minutes, 1 hour, 2 hours, and 3 hours in a SPEX-8000M shaker mill and subjected to XRD analysis. Cu x Mo 6 Se 8  was also synthesized using a similar approach. Stoichiometric amounts of MoSe 2  (1.141 g, 99.9% Alfa Aesar), Mo (0.432 g, 99.9% Alfa Aesar), and CuSe (0.427 g, 99.5% Alfa Aesar) were batched in a stainless steel vial (powder:ball ratio=1:10). The powders were mechanically milled for 30 minutes, 1 hour, 2 hours, and 3 hours, and subjected to XRD analysis. The milled powder was thermal treated at elevated temperature under ultra-high purity Argon (UHP-Ar) atmosphere. Copper-ions were subsequently leached out from HEMM-derived ternary Chevrel phase(s) using 6 molar hydrochloric acid solution under constant oxygen flow for 8 hours in ambient atmosphere. After copper-ions were leached completely from the parent phase, the acid solution containing the residue was centrifuged, washed with de-ionized water three times and dried in an oven at ˜323K. 
     Materials Characterization 
     The thermal behavior of the milled powder was evaluated by thermo-gravimetric (TG)/differential scanning calorimetry (DSC) using a Netzsch STA 409 PC Luxx thermal analyzer unit in an ultra UHP-Ar atmosphere at a heating rate of 10 K/min, up to 1273K. The milled powder samples were isothermally heat treated at 1273K for 30 minutes under UHP-Ar atmosphere followed by X-rays diffraction (XRD) analyses. In addition, the mechanically milled powder was thermal treated at elevated temperature for different durations (30 minutes, 5 hours) under UHP-Ar atmosphere. Powder X-ray diffraction (XRD) of the milled, commercial and thermally-treated powders was carried out using the Philips PW1830 system employing the CuK α  (λ=0.15406 nm) radiation. Quantitative phase analysis was carried out using PANalytical X&#39;Pert HighScore Plus Rietveld program on the powder XRD patterns. No other attempt was made to determine the composition obtained from the HEMM approach at high temperature. Microstructural analyses of the milled, commercial and heat treated powders (Chevrel phases) were performed using a scanning electron microscopy (JSM-6610, JEOL) operating at 10 kV and high resolution transmission electron microscopy-HRTEM (JEOL JEM 2000FX) operating at 200 kV. Specific surface area of the milled powder was measured using the Brunauer-Emmett-Teller (BET) technique. Each sample was vacuum degassed and then tested using a Micromeritics ASAP 2020 BET equipment. 
     Electrochemical Characterization 
     Electrode slurry was formulated by mixing 80 wt. % of active material (−325 mesh), 10 wt. % Super-P carbon, 10 wt. % polyvinylidene fluoride (PVDF) binder with N-methylpyrrolidinone (NMP) solvent together in a glass vial with constant magnetic stirring for 24 hours. The slurry obtained was coated (50 μm thick) onto graphite foil acting as a current collector and dried at ˜383K overnight in a vacuum oven. Further, the dried electrodes were uniaxially pressed at ˜5 MPa to improve the particle contacts and then circular disks (Θ=11.28 mm) were punched with an active material loading ˜1-3 mg/cm 2 . An electrochemical test was carried out at room temperature with 2016-type coin cells assembled inside an argon-filled MBraun Inc. glove box (&lt;0.1 ppm each of O 2  and H 2 O) employing magnesium foil as the counter and reference electrode, electrode disks as working electrode, and Celgard® separator soaked in an electrolyte solution of 0.4 molar 2 (PhMgCl)—AlCl 3 /tetrahydrofuran. Cyclic voltammogram (CV) was acquired using an electrochemical workstation (VersaSTAT 3, Princeton Applied Research) at a constant sweep rate of ˜0.001 Vs −1 . Galvanostatic charge-discharge cycles were carried out at various rates ˜20-160 mAg −1  within 0.5-1.5V or 0.5-1.7V, employing a short rest period between the charge/discharge cycles using a multichannel battery testing system (Arbin BT2000 instrument). Electrochemical impedance spectroscopy (EIS) was performed to understand the charge storage behavior in Chevrel phases. EIS was performed on the Versastat 3 over a frequency range of 0.01 Hz-100 KHz. An A.C. amplitude of 5 mV was used and the spectra were obtained after charge/discharge cycles. The charge transfer characteristics and accompanying parameters were analyzed by equivalent circuit modeling using Z-View (Scribner Associates, Inc.; version 3.3). 
     Results and Discussion 
     Synthesis of Cu x Mo 6   8  Chevrel phase by HEMM Approach 
     Each as-received commercial powder as well as mechanically milled powders was subjected to XRD analysis. The major XRD peaks from commercial powders can be indexed with standard Mo (ICDD number: 98-006-2711; cubic; space group Im-3m, number 229), CuS (ICDD number: 01-079-2321; hexagonal; space group P63/mmc, number 194), and MoS 2  (ICDD number: 03-065-7025; hexagonal; space group P63/mmc, number 194) phase. From the XRD pattern of mechanically milled powders, it appeared that gradual increase in milling duration from 30 minutes to 3 hours induced a homogeneous mixture between CuS, Mo, MoS 2  phase. The Bragg reflection of high intensity peaks from MoS 2 , Mo and CuS were evident in the XRD patterns of milled powders. The absence of any peaks besides CuS, Mo and MoS 2  suggested that mechanical milling only induced an intimate mixture between the constituent phases rather than forming any new phase(s). However, gradual increase in milling duration would likely induce an X-rays amorphization of the MoS 2  and CuS phase either due to formation of ultrafine particles or diffusive mixing mechanisms initiated between the CuS and MoS 2  phases which would significantly decrease the peak intensity and allow peak broadening. The relative intensity of peaks from (002), (010), (013), (105) and (112) planes of MoS 2  and (102), (013), (006), (110) planes of CuS were significantly reduced and peaks were broadened as the milling duration increased from 30 minutes to 3 hours. The Bragg reflection from (011), (002), (112), and (022) planes reflected from elemental Mo were found to be relatively intense. The difference in peak intensities and broadening during milling operation was mainly due to a difference in the hardness of starting compositions, where ductile and hard Mo metal powder repeatedly got fractured and cold welded whereas brittle and soft MoS 2 , and CuS ceramic phase got fragmented and embedded within the ductile Mo matrix during milling operation. 
     SEM images of the commercial powder used during milling showed unique morphology of the particles before milling. CuS particles were of irregular shape and agglomerated, whereas MoS 2  were large and flaky, and Mo particles were round and globular. Following 30 minutes of mechanical milling, the morphology of the particles changed completely and irregular shape particles were formed. SEM image of the 30 minute-milled powder showed formation of agglomerated irregular shaped particles mechanically bonded together. Quantitative elemental composition of the milled powder obtained by EDX analyses confirmed that measured atomic percent of each element (Cu, Mo, and S) was close to the stoichiometric batch composition. The elemental X-ray mapping of Cu, Mo, and S atoms in the milled powder showed homogeneous distribution of Cu, Mo, and S within the agglomerated particles without segregation on any specific site. Importantly, the absence of any oxides of copper and molybdenum up to 3 hours of milling was evident from the XRD patterns which suggested that milling between CuS, MoS 2 , and Mo in atmospheric conditions does not oxidize or contaminate the milled composition. However, mechanical milling did not form the desired ternary CP (since Chevrel phase formation is a thermally activated metastable process and requires thermal treatment at elevated temperature under inert atmosphere to form the desired phase). The Brunauer-Emmett-Teller (BET) surface area measurement by nitrogen adsorption/desorption technique of the milled powder was ˜12.33 m 2 /g, 14.61 m 2 /g, 7.72 m 2 /g, and 9.65 m 2 /g, for 30 minute-, 1 hour-, 2 hours-, and 3 hours-milled powder sample, respectively. From the surface area measurement it appeared that mechanical milling beyond 1 hour had no effect on reduction of surface area of milled particles. However, to complete the formation of homogeneous mixture between the constituents the mechanical milling was continued up to 3 hours. 
     To assess phase formation during thermal treatment of the mechanically milled powder, selected milled samples were subjected to thermo gravimetric-differential scanning calorimetry (TG-DSC) under UHP-Ar atmosphere up to 1273K at a constant heating rate of 10K/min. The TG-DSC trace showed a continuous exothermic behavior of the milled powder samples. The 30 minutes-milled sample showed a broad exothermic peak between 600-1260K associated with an enthalpy of formation ˜775 J/g (˜743 kJmol −1 ) approximated to the calculated enthalpy of formation (˜873 kJmol −1 ) for Cu 2 Mo 6 S 8  at 1000K. DSC traces of 1 hour- and 3 hour-milled powder samples showed a continuous exothermic behavior beyond 600K with no apparent exotherms up to 1273K. However, thermo gravimetric (TG) curves exhibited ˜4% weight loss between ˜525K to ˜630K for each sample. The 4% weight loss associated with TG analysis was accompanied by heat evolution in the DSC curves which suggested that an exothermic process was initiated. To assess the exothermic reaction processes evolved with DSC scan of milled powder sample, each of the constituents (CuS, Mo and MoS 2  powder) used during milling was subjected to TG-DSC under identical conditions. The thermo gravimetric trace of Mo and MoS 2  commercial powder showed no appreciable weight change. However, CuS showed ˜16% weight loss when heated to ˜745K that was accompanied by an endothermic reaction (enthalpy of formation: −206 J/g or 19.7 kJ/mol) between ˜686K to ˜773K with the peak endotherm at ˜745K. Without intending to be bound by any particular theory, it is believed that the endothermic peak was due to formation of Cu 2 S and sulfur-rich liquid phase from CuS since the thermodynamic measurement of enthalpy of formation for peritectic decomposition of CuS to Cu 2 S and S-rich liquid was 17.87 kJ/mol. The formation of Cu 2 S from CuS resulted in a 16% weight difference according to the following formula:—2CuS (2×95.61)=Cu 2 S (159.16)+S (32.06). The ˜4% weight loss (¼th of ˜16%) observed was related to the phase transformation of CuS to Cu 2 S and sulfur-rich liquid phase and was in agreement with the following formula:—2CuS+3Mo+3MoS 2 ═Cu 2 Mo 6 S 8 . It is believed that the sulfur-rich liquid reacted immediately with elemental Mo and formed the MoS 2  phase which subsequently reacted with Cu 2 S, unreacted Mo and MoS2 and formed the desired ternary copper CP according to the following formula—Cu 2 S+3MoS 2 +xMoS 2 +(3−x)Mo+(1−2x)S═Cu 2 Mo 6 S 8 . 
     To assess the details of phase formation during thermal treatment, equimolar amounts of Mo (˜1 g) and CuS(˜1 g) were mechanically milled for 30 minutes and subjected to TG-DSC. The TG-DSC trace of CuS-Mo powder exhibited three regions, a small endothermic hump at ˜714K (due to peritectic reaction and melting of CuS to Cu 2 S and S) associated with ˜8% weight loss, a plateau between the temperature interval of 714K-800K, and a continuous exothermic region beyond 800K up to 1273K. It appeared that the peritectic reaction at ˜714K occurred slightly earlier than expected likely due to mechanical milling having decreased the particle size and collapsed the hexagonal crystal structure of CuS. The XRD pattern of the mechanically milled powder showed the presence of Mo and CuS phase. XRD analysis was performed on the remnant powder after the TG-DSC test was completed. The XRD showed the formation of Cu 1.83 Mo 3 S 4  phase (ICDD: 98-000-5103), along with elemental Mo and Cu. It is believed that CuS dissociated into Cu 2 S and elemental sulfur and further reacted with Mo to form the Cu 1.83 Mo 3 S 4  Chevrel phase according to the following reactions: 
       CuS═Cu 2 S+Mo (˜714 to ˜745K)
 
       2Cu 2 S+2S+4Mo═Cu 1.83 Mo 3 S 4 +2.17Cu+Mo (between 800K-1273K).
 
     Thermal treatment of CuS+Mo powder was carried out inside a tube furnace at two different temperatures of ˜773K (above the peritectic temperature of CuS) and ˜1273K at a heating rate of 10K/min and allowed the powder to furnace cool under UHP-Ar atmosphere. The XRD pattern of the sample thermally treated to ˜773K showed the presence of Cu 2 S and elemental Mo, whereas, the sample heated to ˜1273K showed the formation of Cu 1.83 Mo 3 S 4 , Cu and Mo peaks. Similar study between equimolar Mo (0.75 g) and MoS 2  (1.25 g) showed the small endotherm 711K associated with ˜8% weight loss due to the peritectic reaction melting of CuS in the TG-DSC trace. However, the CuS+MoS 2  milled powder when heated to ˜773K and ˜1273K respectively, showed no traces of Chevrel phase formation confirmed by XRD analyses, instead Cu 2 S and MoS 2  phase were intact. The above evaluations suggested that the presence of CuS and Mo in the starting composition was essential for the formation of ternary copper CP. One possible reaction scheme for the formation of Cu 2 Mo 6 S 8  ternary CP at elevated temperature may be Cu 1.83 Mo 3 S 4 +2.17Cu+Mo+2Mo+6MoS 2 =2Cu 2 Mo 6 S 8 . 
     To assess whether ternary CP can be formed during thermal treatment, a XRD analysis of the remnant powder was conducted following completion of the TG-DSC on 2CuS+3Mo+3MoS 2  samples milled for 30 minutes and 1 hour. The alumina crucible used during the TG-DSC test was carefully opened upon cooling to room temperature and the sample (˜10 mg) was evenly spread onto a glass slide and a XRD analysis between 10-90° 2θ value was performed. Unexpectedly, the XRD data of a 1 hour milled sample heated to 1273K at a constant heating rate of ˜10K/min showed the formation of Cu 2 Mo 6 S 8  phase along with unreacted MoS 2 , Mo, and MoO 2  phase as impurities. It is believed that Cu 2 Mo 6 S 8  was formed before the temperature was reached to 1273K. However, incomplete formation/transformation of Cu 2 Mo 6 S 8  phase was mainly due to insufficient time to allow completion of the solid state diffusive reaction to occur between the constituents. A similar TG-DSC evaluation was repeated up to 1273K with an additional 30 minute-holding time at 1273K with 1 hour- and 3 hour-milled powders. The XRD analysis performed on 1 hour- and 3 hour-mechanically milled powder following TG-DSC test showed the formation of Cu 2 Mo 6 S 8  phase with minor unreacted MoS 2  and Mo. According to the Cu—Mo—S ternary phase diagram at 1273K, Cu x Mo 6 S 8  phase could co-exist with MoS 2  and metallic Mo and appear as minor impurities during high temperature synthesis of the ternary Chevrel phase, M x Mo 6 S 8  (M═Cu, Sn). The above results were encouraging and indicated that ternary copper CP (Cu 2 Mo 6 S 8 ) could be formed using CuS, Mo, and MoS 2  powder at 30 minute-dwell time at 1273K peak temperature. The magnified portion between 2θ values of 12-16° of the XRD data clearly showed that 30 minute-dwell time at 1273K had a pronounced effect on Cu 2 Mo 6 S 8  formation, as the high intensity peak from (002) plane of MoS 2  was significantly reduced at the expense of peak intensity from (101) plane of Cu 2 Mo 6 S 8  phase. An ˜2 g powder sample of 30 minute- and 1 hour-milled powder was placed on a corundum crucible and thermally treated inside a tubular furnace with a heating rate of 10K/min at two different temperatures of 1123K and 1273K with a 30 minite-dwell time at peak temperature followed by cooling to room temperature at a constant cooling rate of 10K/min (the above experiments were done under UHP-Ar, gas flow rate ˜100 standard cubic centimeter/min). The heat-treated powder analyzed by XRD showed the formation of ternary copper CP -Cu 2 Mo 6 S 8 . The 30 minute-mechanically milled powder sample thermally treated to 1123K with 30 minute-dwell time showed the formation of Cu 2 Mo 6 S 8  with slight presence of unreacted MoS 2  and Mo powder. However, the 30 minute- and 1 hour-milled powder samples when heated to 1273K with 30 minute-dwell time at the peak temperature, the MoS 2  peak was completely vanished and fully crystalline Cu 2 Mo 6 S 8  phase was formed. The magnified portion between 12-16° of the XRD patterns depicted the high intensity peak from (101) plane of Cu 2 Mo 6 S 8  phase matched completely with the standard Cu 2 Mo 6 S 8  database (ICDD number: 00-047-1519). Secondary electron SEM image of the Cu 2 Mo 6 S 8  phase synthesized at 1123K and 1273K with 30 minute-dwell time at peak temperature showed the formation of sub-micron to micrometer size irregular shaped particles. The composition, obtained by EDX quantitative analyses, of the copper Chevrel phase formed at 1123K and 1273K, respectively, was in good agreement with TG-DSC/XRD data and suggested that rapid synthesis of Cu 2 Mo 6 S 8  by HEMM was possible and could be achieved in a time period as low as at 30 minutes. Lattice parameter(s) calculated using the least-square method of the experimental XRD data was in good agreement with the standard Cu 2 Mo 6 S 8  (ICDD number: 00-047-1519; a=0.9584 nm, c=1.025 nm, unit cell volume=815.36×10 −3  nm 3 ) unit cell parameters and presented in Table 1. 
     Phase Formation and Electrochemical Activity of HEMM Derived De-Cuprated Mo 6 S 8    
     To obtain the de-cuprated Mo 6 S 8  phase, Cu 2 Mo 6 S 8  phase formed at 1123K and 1273K was treated with 6 molar hydrochloric acid solution with constant O 2  bubble for 7 hours in a round bottom flask. In order to confirm the formation of Mo 6 S 8  after complete copper leaching, XRD analysis was performed. All the Braggs peaks in the XRD patterns matched with the standard Mo 6 S 8  (ICDD: 98-005-708) pattern which suggested complete copper removal was achieved. EDX full frame analyses also confirmed that hydrochloric acid-treated samples were devoid of copper. High resolution SEM image of the respective Mo 6 S 8  phase showed agglomerated particles of submicron to micrometer size. Electrochemical performance of the 80 wt. % Mo 6 S 8 : 10 wt. % Super-P: 10 wt. % PVDF composite electrode was evaluated in a 2016 coin cell. The galvanostatic cycling conducted at ambient condition between 0.5-1.7V with a current of 20 mAg −1  (˜C/6 rate) showed 1 st  cycle discharge capacity of ˜101 mAhg −1  and ˜100 mAhg −1  for de-cuprated Cu 2 CP formed at ˜1123K and ˜1273K, respectively. A steady and expected discharge capacity of ˜68 mAg −1  and ˜70 mAhg −1  was achieved from 2 nd  to 100 th  cycle due to partial Mg-ion trapping within Mo 6 S 8  structure and associated 30% drop in capacity in the 1st cycle. The cyclic voltammogram of the Mo 6 S 8  electrode showed expected signature of two anodic peaks during magnesiation and a cathodic peak during de-magnesiation, respectively. 
     To achieve the fully crystalline phase pure Cu 2 Mo 6 S 8  ternary CP, dwell time at peak temperature of ˜1273K was increased to 5 hours. The XRD pattern of 3 hour-mechanically milled powder heat treated at 1273K with the holding time of 5 hours at peak temperature confirmed the complete formation of Cu 2 Mo 6 S 8 . De-cuprated Mo 6 S 8  was obtained after complete copper removal using a 6 molar HCl solution with constant oxygen bubbling for 7 hours. The lattice parameter(s) calculated using least-square method of Cu 2 Mo 6 S 8  phase formed after 3 hour-mechanically milled powder thermally treated at ˜1273K with 5 hours dwell time at peak temperature are shown in Table 4 and are in good agreement with standard unit cell parameter(s). 
     
       
         
           
               
             
               
                 TABLE 4 
               
             
            
               
                   
               
               
                 Calculated lattice parameter(s) of Cu x Mo 6 S 8  phase. 
               
            
           
           
               
               
               
            
               
                   
                   
                 Quantitative  
               
               
                   
                 Lattice parameter(s) of 
                 Phase for- 
               
               
                 Condition 
                 Cu 2 Mo 6 S 8   
                 mation (%) 
               
               
                   
               
               
                 1 h mechanically  
                 a H : 0.963138 nm, c H : 1.021042  
                 0.3% Mo +  
               
               
                 milled powder  
                 nm 
                 99.7% 
               
               
                 thermally treated 
                 a R : 0.651957 nm, α R : 95.233° 
                 Cu 2 Mo 6 S 8   
               
               
                 to 1273 K with 30  
                 unit cell volume = 820.2588 ×  
                   
               
               
                 min hold at 1273 K 
                 10 −3  nm 3   
                   
               
               
                 30 min mechanically 
                 a H : 0.962119 nm, c H : 1.021095  
                 0.3% Mo +  
               
               
                 milled powder  
                 nm 
                 99.7% 
               
               
                 thermally treated to  
                 a R : 0.651464 nm, α R : 95.1953° 
                 Cu 2 Mo 6 S 8   
               
               
                 1273 K with 30 min  
                 unit cell volume = 818.567 ×  
                   
               
               
                 hold at 1273 K 
                 10 −3  nm 3   
                   
               
               
                 30 min mechanically 
                 a H : 0.959014 nm, c H : 1.022991  
                 1.4%  
               
               
                 milled powder  
                 nm 
                 MoS 2  +  
               
               
                 thermally treated  
                 a R : 0.650268 nm, α R : 95.0207° 
                 0.3% Mo + 
               
               
                 to 1123 K with 30 
                 unit cell volume = 814.8032 ×  
                 98.3% 
               
               
                 min hold at 1123 K 
                 10 −3  nm 3   
                 Cu 2 Mo 6 S 8   
               
               
                 3 h mechanically  
                 a H : 0.961938 nm, c H : 1.021293  
                 100%  
               
               
                 milled powder  
                 nm 
                 Cu 2 Mo 6 S 8   
               
               
                 thermally treated to  
                 a R : 0.65141 nm, α R : 95.1822° 
                   
               
               
                 1273 K with 5 h  
                 unit cell volume = 818.4188 ×  
                   
               
               
                 hold at 1273 K 
                 10 −3  nm 3   
               
               
                   
               
            
           
         
       
     
     Whereas, lattice parameter(s) of de-cuprated Mo 6 S 8  calculated using the least-square method (a=0.919233 nm, c=1.087942 nm, unit cell volume=796.1371×10 −3  nm 3 ) were found to be in excellent agreement with the standard Mo 6 S 8  (ICDD number: 98-005-1708; a=0.92 nm, c=1.088 nm, unit cell volume=797.51×10 −3  nm 3 ) unit cell parameters showed that complete removal of copper was achieved. The SEM image of Cu 2 Mo 6 S 8  and de-cuprated Mo 6 S 8  showed irregular shape submicron size particles that were formed in the case of Cu 2 Mo 6 S 8  phase, which retained their morphology in the de-cuprated Mo 6 S 8  phase as well. The HRTEM lattice fringe spacing of Cu 2 Mo 6 S 8  and Mo 6 S 8  phase was calculated as ˜0.645 nm and ˜0.479 nm which corresponded to the interplanar d-spacing of (101) and (102) planes for Cu 2 Mo 6 S 8  and ˜0.641 nm for Mo 6 S 8  corresponding to the interplanar d-spacing of (101) plane (hexagonal crystal system: space group R-3). The de-cuprated Mo 6 S 8  phase was then tested as a magnesium battery cathode in a 2016 coin cell setup using 2(PhMgCl)—AlCl 3 /tetrahydrofuran electrolyte and polished Mg foil as the anode. The electrochemical performance of Mo 6 S 8  composite electrode showed outstanding performance where Mg-ions could be inserted/extracted reversibly from the de-cuprated Mo 6 S 8  phase. The cyclic voltammogram acquired at a sweep rate of 0.1 mVs −1  between 0.5-1.75V versus Mg/Mg 2+  showed typical reversible magnesiation/demagnesiation phenomena of Mo 6 S 8  electrode where magnesiation and demagnesiation occurred at ˜1V and ˜1.28V, respectively. The galvanostatic cycling of Mo 6 S 8  electrode showed 1 st  cycle discharge (magnesiation) and charge (demagnesiation) capacity of ˜92 mAhg −1  (˜72% of theoretical capacity 128 mAhg −1 ) and ˜57 mAhg −1  with Coulombic efficiency ˜62% when cycled at a current density of 20 mAg −1 . Between the 2 nd  and 107 th  cycle a stable discharge and charge capacity of ˜62 mAg −1  and 67 mAg −1  was observed with 95.6% Coulombic efficiency. The expected drop in capacity from 2 nd  cycle onwards was due to one Mg-ion being trapped which occurred within the Mo 6 S 8  framework at the 1 st  cycle resulting in a capacity loss from the theoretical value (˜128 mAhg −1 ). Capacity versus voltage profile of 25 th , 50 th , and 100 th  cycle exhibited magnesiation and demagnesiation reaction plateaus at ˜1.07V and ˜1.2V and was in agreement with a CV curve and those reported in the literature. Rate retention of Mo 6 S 8  electrode was also excellent, at C/24, C/12, C/6, C/4, C/3, C/2, 1 C (1 C˜120 mAg −1 ) and 1.5 C current rate a discharge capacity of ˜79 mAhg −1 , ˜74 mAhg −1 , ˜70 mAg −1 , ˜65 mAhg −1 , ˜62 mAhg −1 , ˜59 mAhg −1 , ˜56 mAhg −1 , ˜51 mAhg −1  and ˜49 mAhg −1  was achieved with a Coulombic efficiency ˜96.8%, ˜94.2%, ˜97.1%, ˜99.2%, ˜99.9%, ˜99.9%, ˜99.7%, ˜99.9%, and ˜99.2%, respectively. In addition, long cycle stability of Mo 6 S 8  electrode was tested in a 2016 coin cell setup and showed remarkable performance and durability. The 2016 coin cell was cycled continuously for 48 days and was able to deliver a specific capacity ˜70 mAhg −1  with a Coulombic efficiency ˜99% at 330 th  cycle. These attributes support the HEMM approach for rapid synthesis of Cu 2 Mo 6 S 8  Chevrel phase, and as an alternative synthesis route for ternary CP. 
     Synthesis of CuMo 6 Se 8  Chevrel Phase by HEMM Approach 
     It was demonstrated that Cu 2 Mo 6 S 8  could be synthesized by HEMM approach and its electrochemical performance in a magnesium battery was deemed competitive with electrochemical data for Chevrel phases made by known synthesis methods. This similar HEMM approach was employed for the synthesis of ternary Chevrel phase —Cu 2 Mo 6 Se 8  using CuSe, Mo, and MoSe 2  as starting powders. XRD analyses showed powder XRD patterns collected of 30 minutes, 1 hour, 2 hours, and 3 hours of mechanically milled powder of 2CuSe+3MoSe 2 +3Mo nominal composition. The XRD patterns from the commercial powders were also acquired and compared. The major XRD peaks of commercial powders were indexed with Mo, MoSe 2  (ICDD number: 03-065-7025; hexagonal; space group P63/mmc, number 194), and CuSe (ICDD number: 98-007-1382; hexagonal; space group P63/mmc, number 194) phase along with minor Cu 3 Se 2  (ICDD number: 98-000-6312) as impurities. A gradual increase in milling duration from 30 minutes to 3 hours likely induced a homogeneous and intricate mechanical mixture obtained between CuSe, Mo, MoSe 2  phases. The XRD patterns showed the Bragg reflections of high intensity peaks from MoSe 2 , Mo are present but the CuSe peaks completely vanished after 2 hours of milling. Importantly, the absence of oxides of copper and molybdenum during milling operation indicated that mechanical milling between CuSe, MoSe 2 , and Mo phase was also conducive for the direct synthesis of the Cu 2 Mo 6 Se 8  phase. SEM images of the CuSe, and MoSe 2  commercial powder used during milling showed unique morphologies of the particles before milling. CuSe particles were plate-like, whereas MoSe 2  particles were large and flaky. However, upon 30 minutes of milling the morphology of the particles changed completely and correspondingly irregular shaped particles were formed. SEM image of the 30 minutes milled powder showed the formation of agglomerated irregular shape particles. EDX full frame analysis confirmed that the stoichiometry of the batch composition was maintained. Elemental X-ray mapping analysis confirmed that the distribution of Cu, Mo, and Se atoms in the milled powder were homogeneous throughout the microstructure. However, it is to be noted that direct mechanical milling did not form the desired ternary CP and thermal treatment at elevated temperature under inert atmosphere was required. The BET surface area of the 30 minutes, 1 hour, 2 hours, and 3 hours milled powder was ˜5.82 m 2 /g, ˜3.87 m 2 /g, ˜2.09 m 2 /g, and ˜2.29 m 2 /g, respectively. The BET surface area measurement showed that 30 minutes of milling generated fine particles and further milling had no pronounced effect on the particle size. However, the milling duration was continued up to 3 hours to complete the formation of a homogeneous intricate mixture of the different reaction constituents. 
     The thermal behavior of the 30 minutes, 1 hour, 2 hours and 3 hours mechanically milled powder was evaluated by thermo gravimetric-differential scanning calorimetry (TG-DSC). The samples were heated under UHP-Ar atmosphere up to ˜1273K at a constant heating rate of 10K/min. DSC trace of 30 minutes sample showed a continuous exothermic behavior up to ˜624K followed by a plateau up to ˜745K. The thermo gravimetric (TG) curve exhibited a ˜7% weight loss within the above temperature range. However, there was no further weight loss beyond ˜624K and a continuous exothermic behavior was observed up to ˜1273K. To assess the exothermic/endothermic behavior evolved with TG-DSC scan of milled powder sample, each constituent used during milling was subjected to TG-DSC under identical conditions. The TG-DSC trace of commercial CuSe, Mo, and MoSe 2  powder from room temperature to ˜1273K showed no appreciable weight change of MoSe 2  commercial powder. However, CuSe showed ˜23% weight loss between 646K-860K reflected in the TG curve, that was accompanied by two endothermic reaction peaks at ˜658.8K (enthalpy: 68.45 J/g or 9.75 kJ/mol) and at ˜798K (enthalpy: 10.83 J/g or 1.54 kJ/mol) in the DSC trace. The endothermic peak observed at ˜658.8K was due to incongruent melting of CuSe and formation of Cu 2 Se and Se-rich liquid and the second endothermic peak observed at ˜798K was due to eutectic melting of Cu 2 Se and sulfur-rich phase according to the copper-selenium binary phase diagram. Previous studies showed that enthalpy of formation for peritectic decomposition of CuSe to Cu 2 Se and Se-rich liquid was ˜11.8±0.03 kJ/mol and was in agreement with experimental data. The formation of Cu 2 Se and Se-rich liquid from CuSe at ˜658.8K observed in the DSC curve resulted in a 27.7% weight loss according to the following formula:—2CuSe (2×142.51)=Cu 2 Se (206.05)+Se (78.96). Thus, the ˜7% weight loss (¼th of ˜27.7%) was related to the phase transformation of CuSe to Cu 2 Se phase and was in excellent agreement with the following formula:—2CuSe+3Mo+3MoSe 2 ═Cu 2 Mo 6 Se 8 . It was believed that Se-rich liquid reacted immediately with Mo powder and formed the MoSe 2  phase and further, the remaining constituents (Cu 2 Se, Mo and MoSe 2 ) reacted with each other and formed the desired Cu 2 Mo 6 Se 8  phase. 
       Cu 2 Se+3MoSe 2   +x MoSe 2 +(3 −x )Mo+(1−2 x )Se═Cu 2 Mo 6 Se 8  
 
     The thermal treatment of milled powder at elevated temperature was important to initiate liquid-phase sintering between the constituents. To assess the phase formation during heat treatment, ˜2 g of 1 hour mechanically milled powder sample of nominal composition 2CuSe+3Mo+3MoSe 2  was heated inside a tube furnace with a heating rate of 10K/min at various temperatures followed by cooling to room temperature at a constant cooling rate of 10K/min (these experiments were done under UHP-Ar atmosphere with gas flow rate ˜100 standard cubic centimeter/min). The XRD pattern of the sample heated to ˜733K could be indexed to Mo, MoSe 2 , Cu 2 Se and MoO 2  phases. The presence of (11-1) MoO 2  peaks at 26.0° 2θ value was likely as a result of the oxidation of Mo to MoO 2  during thermal treatment due to the unavoidable presence of trace amount of oxygen inside the furnace. In addition, Cu 2 Se phase [presence of (111) peak at 26.7° 2θ value] was evident instead of CuSe in the XRD pattern due to incongruent melting of CuSe to Cu 2 Se and Se-rich liquid at ˜659K according to the TG-DSC analysis. However, there was no Bragg&#39;s reflection observed from elemental Se in the XRD pattern which suggested that Se-rich liquid immediately reacted with Mo and formed the MoSe 2  phase. This is supported by the TG-DSC analysis of 1 hour milled powder as an exothermic peak is observed at ˜735K due to formation of MoSe 2  phase. MoSe 2  could be formed at temperatures as low as ˜650K and is stable over wide temperature range between ˜273K to ˜1473K according to the Mo-Se binary phase diagram. The XRD patterns of the sample heated to ˜925K and ˜1000K showed similar XRD peaks with the sample heated to ˜733K which corroborated that higher temperature beyond ˜1000K is required for Cu x Mo 6 Se 8  phase to be formed. The powder sample when heated to ˜1089K showed the formation of Cu 2 Mo 6 Se 8  phase with the presence of elemental Mo, MoSe 2 , and MoO 2  as impurities. The absence of high intensity peak from (111) plane of Cu 2 Se phase at 26.7° 2θ value in the XRD pattern except for the ˜733K sample suggested that Cu 2 Se started to disappear above 800K due to eutectic melting of Cu 2 Se phase which likely reacted with Mo and MoSe 2  phase and nucleated the desired ternary selenium CP phase analogous to the case observed with sulfur CP (shown above). As expected, the sample when heated to ˜1151K also showed the formation of Cu 2 Mo 6 Se 8  phase. However, phase-pure Cu x Mo 6 Se 8  was not detected in the XRD patterns when the sample was heated to ˜1089K or ˜1151K due to insufficient dwell time at the respective temperature needed to allow for complete transformation to occur. Intrigued by the above observation, ˜2 g sample of 30 minutes, 1 hour, 2 hours, and 3 hours of mechanically milled powder was placed on a corundum crucible and thermally treated at ˜1151K with 30 minute dwell time at the peak temperature inside a tube furnace under argon atmosphere. The powder XRD analysis of the heat-treated powder confirmed the formation of ternary copper CP—Cu 2 Mo 6 Se 8  with slight presence of unreacted Mo, MoO 2  and MoSe 2  phase. Full frame quantitative EDX analyses of the low magnification (1000×) SEM images also proved the presence of Cu, Mo and Se atoms in the ternary Cu—Mo 6 Se 8  phase formed at 1151K with 30 minute dwell time as well as in the hydrochloric acid treated de-cuprated Mo 6 Se 8  phase. The above data was encouraging and in good agreement with TG-DSC, and suggested that synthesis of fully crystalline Cu 2 Mo 6 Se 8  phase was possible by the HEMM approach in a time duration as low as 30 minutes at ˜1151K. Lattice parameter(s) of Cu 2 Mo 6 Se 8  phase were calculated using the least-square method of the experimental data and are presented in Table 5. The excellent agreement of lattice parameters with the standard unit cell parameter(s) of Cu 2 Mo 6 Se 8  reported in the literature suggested that the HEMM approach could be applied successfully for the synthesis of selenium CP with minimal thermal treatment required at ˜1151K under argon atmosphere. 
                     TABLE 5                  Calculated lattice parameter(s) of Cu x Mo 6 Se 8  phase.                                 Quantitative            Lattice parameter(s) of    Phase       Condition   Cu 2 Mo 6 Se 8     formation (%)               1 h mechanically    a H : 0.999259 nm, c H :    0.2% Mo + 1.8%        milled powder    1.072559 nm   MoO 2  + 1.7%        thermally treated   a R : 0.678719 nm, α R :    MoSe 2  + 96.3%        to 1089 K   94.8065°   Cu 2 Mo 6 Se 8             unit cell volume =                927.4872 × 10 −3  nm 3             1 h mechanically    a H : 0.997191 nm, c H : 1.07323    0.3% Mo + 1.8%        milled powder    nm   MoO 2  + 1.7%        thermally treated   a R : 0.677823 nm, α R :    MoSe 2  + 96.2%        to 1151 K   94.7132°   Cu 2 Mo 6 Se 8             unit cell volume =                924.2306 × 10 −3  nm 3             30 min    a H : 0.972965 nm, c H :    0.2% Mo + 1.9%        mechanically   1.092789 nm   MoO 2  + 1.7%        milled powder    a R : 0.669508 nm, α R :   MoSe 2  + 96.2%        thermally treated    93.2087°   Cu 2 Mo 6 Se 8         to 1151 K with    unit cell volume =            30 min hold at    895.9042 × 10 −3  nm 3             1151 K               3 h mechanically    a H : 1.002506 nm, c H : 1.07251    1.8% MoO 2  +       milled powder    nm   1.7% MoSe 2  +        thermally treated    a R : 0.680305 nm, α R :    96.5%       to 1273 K with 5    94.9202°   Cu 2 Mo 6 Se 8         h hold at 1273 K   unit cell volume =                933.4816 × 10 −3  nm 3                      
Phase Formation and Electrochemical Activity of HEMM Derived De-Cuprated Mo 6 Se 8  
 
     The de-cuprated Mo 6 Se 8  phase was obtained by completely leaching out copper from Cu 2 Mo 6 Se 8  phase formed at 1151K with 30 minutes dwell time at the peak temperature. The XRD patterns analysis confirmed the formation of Mo 6 Se 8  phase along with minor MoO 2  and unreacted MoSe 2  phase. The major Bragg peaks matched with the standard Mo 6 Se 8  pattern (ICDD: 01-085-0455) suggested copper was completely removed. SEM image of the Mo 6 Se 8  phase showed particles of submicron to micrometer size. Electrochemical performance of the 80 wt. % Mo 6 Se 8 : 10 wt. % Super-P: 10 wt. % PVDF composite electrode was evaluated in a 2016 coin cell. The electrochemical test showed the 1st cycle discharge (magnesiation) and charge (de-magnesiation) capacity was ˜58.5 mAhg −1  and ˜64 mAhg −1  with Coulombic efficiency ˜91.5%. In the 2nd cycle the discharge and charge capacity were ˜59.4 mAhg −1  and ˜70.5mAhg −1  and in the 3rd cycle, the discharge and charge capacity were ˜63.8 mAhg −1  and ˜75.5mAhg −1 , respectively. It is apparent from the voltage profile that a single voltage plateau was observed during the 1st cycle discharge (˜0.85V) and charge (˜1.17V) whereas 2-steps magnesiation at ˜1.05V and ˜0.97V and de-magnesiation reactions at ˜1.1V and ˜1.17V were evident in the 2nd and 3rd cycle. The detailed subtle differences in the charge-storage mechanisms into Mo 6 Se 8  phase from the 1st cycle and the subsequent cycles are discussed later herein. However, the competitive electrochemical data of de-cuprated Mo 6 Se 8  phase obtained from Cu 2 Mo 6 Se 8  phase formed at 30 minutes suggested the ease of synthesis of the corresponding selenium CP. 
     The fully crystalline, Cu 2 Mo 6 Se 8  ternary CP was also obtained upon heating the 3 hours mechanically milled sample at ˜1273K with additional 30 minutes dwell time at peak temperature. The XRD pattern of 3 hours mechanically milled powder thermally treated at ˜1273K with 5 hours dwell time at peak temperature showed the formation of Cu 2 Mo 6 Se 8  phase along with MoSe 2  and MoO 2  as impurities (Table 5). De-cuprated Mo 6 Se 8  was obtained by complete leaching of copper using a 6 molar HCl solution under oxygen bubbling for 7 hours. The lattice parameter(s) of Cu 2 Mo 6 Se 8  was calculated using least-square method and are shown in Table 5. The lattice parameter(s) of Cu 2 Mo 6 Se 8  was in good agreement with standard unit cell parameter(s). Whereas, lattice parameter(s) of de-cuprated Mo 6 Se 8  (a=0.955858 nm, c=1.116432 nm, unit cell volume=883.3835×10-3 nm3) was found to be in excellent agreement with the standard Mo 6 Se8 (ICDD number: 01-085-0455; a=0.95488 nm, c=1.12095 nm, unit cell volume=884.40×10-3 nm3) unit cell parameters suggesting that copper was completely removed by HCl treatment from the Cu 2 Mo 6 Se 8  phase. The SEM image of Cu 2 Mo 6 Se 8  and de-cuprated Mo 6 Se 8  showed irregular shaped submicron size particles that were formed in the case of Cu 2 Mo 6 Se 8  phase which retained its morphology completely in the de-cuprated Mo 6 Se 8  phase. The HRTEM lattice fringe spacing was calculated as ˜0.668 nm and ˜0.35 nm corresponded to the interplanar d-spacing of (101) and (202) planes for Cu 2 Mo 6 Se 8  and ˜0.666 nm for Mo 6 Se 8  corresponding to the interplanar d-spacing of (101) plane (hexagonal crystal system: space group R-3). 
     The composite electrode consisted of 80 wt. % Mo 6 Se 8  phase (˜325 mech) with 10 wt. % Super-P carbon additive and 10 wt. % PVDF binder. It was then tested in a 2016 coin cell setup as a cathode and polished Mg foil as anode separated by a Celgard® separator soaked in 2(PhMgCl)—AlCl 3 /tetrahydrofuran electrolyte. It showed good electrochemical performance. The cyclic voltammogram, acquired at a sweep rate of 0.1 mVs −1  between 0.5-1.5V versus Mg/Mg 2+  couple, showed a typical two-step reversible magnesiation/demagnesiation phenomena where magnesiation occurred at ˜1.04V, and ˜0.96V and demagnesiation at ˜1.11V, and ˜1.18V, respectively. The anodic/cathodic peaks matched well with the theoretical calculation of the magnesiation/demagnesiation voltage. It was noted that magnesium intercalation/de-intercalation phenomena from Mo 6 Se 8  phase was completely reversible and no partial Mg-ion trapping occurred as in the Mg x Mo 6 S 8  phase due to the higher polarizability of the selenium anionic framework. The electrochemical performance of Mo 6 Se 8  composite electrode as well as the Mo 6 Se 8 -graphite (7:3 weight ratio) in situ composite electrode were compared when tested at a current rate of 20 mAg −1 . The galvanostatic cycling of Mo 6 Se 8  composite electrode showed a 1 st  cycle discharge (magnesiation) and charge (demagnesiation) capacity of ˜83.5 mAhg-1 (˜95% of theoretical capacity-88 mAhg −1 ) and ˜76.3 mAhg −1  with Coulombic efficiency ˜91.4%. Between the 2 nd  and 100 th  cycle, an average discharge and charge capacity of ˜71.2 mAhg −1  and 74.2 mAhg −1  was observed with ˜96% Coulombic efficiency. The gradual fade in capacity from the 2 nd  to 100 th  cycle accompanied by ˜4% irreversible loss per cycle was due to a change in the crystal structure of magnesiated Mo 6 Se 8  from rhombohedral (R 3 ) to triclinic (P 1 ) phase and corresponding loss in electronic and ionic conductivity. The Mg 1 Mo 6 Se 8  and Mg 2 Mo 6 Se 8  crystallized into the triclinic form at room temperature by cation displacement or due to cation ordering of crystal structure which caused expansion of the unit cell and resulted in loss of electrical contact of the active mass with current collector. The calculated molar volume of Mo 6 Se 8  (R0), Mg 1 Mo 6 Se 8  (T1) and Mg 2 Mo 6 Se 8  (T2) phase were 88.78 cm 3 /mol, 184.38 cm 3 /mol, and ˜195.63 cm 3 /mol, respectively. The R0 to T1 transformation was associated with ˜107% cell volume expansion which may cause loss of electrical contact between the active mass and current collector as well as inherently poor electronic and ionic conductivity of the triclinic Chevrel phase resulting in ˜4% capacity fade. In the Mg 2 Mo 6 Se 8  phase, both the Mg-ions were located in the tetrahedral sites of outer ring of cavity 2 and formed a new type of cationic arrangements. The structural rearrangement occurred where four cation sites (2 tetrahedra and two square-pyramids) in cavity 1 for Mg 1 Mo 6 Se 8  degenerated into six tetrahedral sites. Thus, it appeared that the triclinic phase (T1 and T2) is suitable for Mg-ion diffusion and is free from any charge trapping although the loss in capacity gradually is due to poor ionic/electronic conductivity of the magnesiated Mo 6 Se 8  phase. 
     To counteract the loss in electronic/ionic conductivity and associated capacity fade, a bottom-up approach was employed. First, Mo 6 Se 8  particles embedded within the graphitic matrix were obtained using synthetic graphite during milling operation. 70 wt % of (2CuSe+3Mo+3MoSe2) powder with 30 wt. % synthetic graphite (Aldrich, 1-2 μm) was mechanically milled for 3 hours and subjected to thermal treatment at ˜1273K with 5 hours dwell time at the peak temperature. The XRD patterns of the milled, thermal-treated and copper leached powder showed the presence of elemental Mo, MoSe 2 , and CuSe phase along with the high intensity peak from (003) plane of graphite at 2θ value of 26.31° of the 3 hours milled powder. The 3 hours milled powder when heated to ˜1273K under argon atmosphere showed the formation of fully crystalline Cu 2 Mo 6 Se 8 +graphite phase along with unreacted MoSe 2 . Further, copper was leached out and as a result, the de-cuprated Mo 6 Se 8 +graphite (7:3) phase was obtained. It can be seen from the three XRD patterns that peak from (003) plane of graphite was present. However, the peak intensity decreased and indicated the collapse of microcrystalline graphite structure and formation of an amorphous disordered carbon due to defect induced melting commonly observed during high energy mechanical milling. 
     The electrochemical performance of the in situ Mo 6 Se 8 +graphite (7:3) when evaluated in a 2016 coin cell showed significantly improved performance compared to Mo 6 Se 8  electrode. Although the capacity of in situ Mo 6 Se 8 +graphite (7:3) electrode was lower than Mo 6 Se 8  electrode due to 70% active mass, it showed an extremely stable capacity up to 100 cycle. The 1 st  cycle discharge and charge capacity was ˜69.3 mAhg −1  and ˜54.8 mAhg −1  with ˜79.1% Coulombic efficiency. Between the 2 nd  and 100 th  cycle, an average discharge and charge capacity of ˜50.43 mAhg −1  and 50.4 mAhg −1  was observed with 99.93% Coulombic efficiency. From the above study, it can be inferred that graphite provided the required electronic path for Mg-ion intercalation/de-intercalation to occur reversibly into and from the Mo 6 Se 8  phase and improve the Coulombic efficiency from ˜96% to 99.93%. Capacity versus voltage profile of 1 st , 2 nd , 3 rd , 4 th , 15 th , and 100 th  cycle of Mo 6 Se 8  and Mo 6 Se 8 +in situ graphite (7:3) showed exactly similar two-steps magnesiation at ˜0.96V and ˜1.03V and demagnesiation reaction plateaus at ˜1.11V and ˜1.18V was in agreement with cyclic voltammetry data. However, the 1 st  cycle magnesiation required a slight overvoltage and a single sloping reaction plateau was observed at ˜0.85V and correspondingly, the de-magnesiation reaction occurred at ˜1.15V and ˜1.20V due to the kinetic barrier that existed in the Chevrel phase host. Rate retention of Mo 6 Se 8  electrode was also good, at C/4, 3C/8, C/2, 3C/4, 1 C (1 C˜80 mAg −1 ), 3 C/2, and 2 C current rate giving average discharge capacity of ˜71.3 mAhg −1 , ˜60.5 mAhg −1 , ˜56.2 mAhg −1 , ˜51.7 mAhg −1 , ˜47.7 mAhg −1 , ˜41.9 mAhg-1, and ˜31.2 mAhg-1 was achieved with Coulombic efficiency ˜96.1%, ˜97.5%, ˜98.7%, ˜99.5%, ˜99.3%, ˜99.8%, and ˜99.9%, respectively. From the above study it appears that HEMM approach is also suitable for rapid synthesis of Cu 2 Mo 6 Se 8  Chevrel phase, another potential cathode for rechargeable magnesium battery. 
     Conclusions 
     High energy mechanical milling is a suitable approach for preparing ternary Chevrel phase (Cu 2 Mo 6 Z 8 ; Z═S, Se) using metal and metal sulfide as precursors. Cu 2 Mo 6 S 8  was synthesized from CuS, Mo and MoS 2  composition by using the higher energy mechanical milling (HEMM) approach. Mechanical milling of 2CuS+3Mo+3MoS 2  in the corresponding stoichiometric composition for 30 minutes to 3 hours formed a homogeneous intricate mixture which upon heating at elevated temperature formed the desired ternary phase. Quantitative X-rays diffraction study showed ˜98% Cu 2 Mo 6 S 8  phase could be obtained with 30 minutes of milling followed by thermal treatment at 1123K for 30 minutes under argon. SEM images showed the formation of submicron to micrometer sized agglomerated particles. TG-DSC curves were able to show that elemental Mo reacted with CuS and nucleated the Cu 1.83 Mo 3 S 4  phase first which further reacted with MoS 2 , and unreacted Mo and formed the desired Cu 2 Mo 6 S 8  phase. Electrochemical performance of de-cuprated Mo 6 S 8  phase in a magnesium battery exhibited competitive performance where magnesiation and de-magnesiation was observed at ˜1.0V and ˜1.28V respectively. Galvanostatic cycling data showed the 1st cycle discharge and charge capacity of ˜92 mAhg −1  and ˜57 mAhg −1  with Coulombic efficiency ˜62%. The Mo 6 S 8  electrode was able to deliver a specific capacity ˜70 mAhg −1  up to 330 cycles with 99% Coulombic efficiency in a coin cell setup demonstrated the structural integrity of the HEMM-derived Mo 6 S 8  phase. The corresponding Cu 2 Mo 6 Se 8  phase was also synthesized by thermal treatment of the milled powder at 1151K for 30 minutes with ˜96% yield with unreacted Mo, MoSe 2  and MoO 2  as minor impurities. Electrochemical data of Mo 6 Se 8  electrode showed a two-step magnesiation (at ˜1.04V and ˜0.96V) and de-magnesiation (at ˜1.11V and ˜1.18V) phenomena. Galvanostatic cycling of Mo 6 Se 8  electrode showed a 1 st  cycle discharge and charge capacity of ˜83.5 mAhg −1  and ˜76.3 mAhg −1 , respectively with ˜91.4% Coulombic efficiency. A stable discharge and charge capacity of ˜71.2 mAhg −1  and ˜74.2 mAhg −1  was observed with 4% fade per cycle likely due to ˜107% stress generated at the electrode due to change in the crystal structure of magnesiated Mo 6 Se 8  from rhombohedral (R 3 ) to triclinic (P 1 ) phase which resulted in a loss in the electrical path of active mass with current collector. Conductive carbon matrix embedded Mo 6 Se 8  particles generated via milling approach were capable of salvaging the fade in capacity and a stable specific capacity of ˜50 mAhg −1  was observed up to 100 cycles with ˜0.07% fade per cycle using graphite and PMAN as the carbon source. 
     In summary, sulfur and selenium ternary CPs synthesized by the time saving, scalable HEMM approach, and binary CPs obtained by acid leaching copper thereafter were shown as cycle stable Mg-ion battery cathodes suitable for electrical energy storage applications. 
     Example XIV (Cu 1 Mo 6 S 8 ) 
     Experimental 
     The Cu 2 Mo 6 S 8  (Cu 2 CP) Chevrel phase was synthesized by using the high energy mechanical milling (HEMM) route. The approach involved taking stoichiometric amounts of MoS 2 , Mo, and CuS batched in a SS vial (powder:ball ratio=1:10). The powders were mechanically milled for 1 h, 2 h, and 3 h intervals. After 3 h milling, the powder was heat-treated at 1000° C. with a heating rate 10° C./min and kept at the peak temperature for 5 h under ultra-high purity (UHP) Ar atmosphere. XRD pattern of the heat-treated powder showed the formation of pure crystalline Cu 2 Mo 6 S 8 . Further, Cu 2 Mo 6 S 8  was washed with hydrochloric acid for 2 days to yield a completely crystalline Cu 1 Mo 6 S 8 (Cu 1 CP) phase. It was known that Mg 2+  insertion into the Mo 6 S 8  Chevrel phase occurs in two stages, and therefore offers a capacity ˜120 mAhg −1 . Due to partial charge entrapment after the initial magnesiation reaction only ˜50-60% magnesium-ion could be extracted resulting ˜40-50% irreversible loss in the 1 st  cycle from the theoretical value (˜120 mAhg −1 ). In order to minimize the 1 st  cycle irreversible loss (FIR), Cu ions were partially leached from the original Cu 2 CP structure. Therefore, 1.8 g of Cu 2 CP was added to 20 ml 6 M HCl solution in a small glass vial with a magnetic stir bar. The Cu 2 CP/HCl solution was continuously stirred for 2 days at room temperature. After 2 days of continuous stirring, the solution was ultrasonically cleaned using distilled water (3 times) and dried at 60° C. for 24 h. The XRD pattern of the partial leached Cu 2 CP shows the formation of completely crystalline Cu 1 Mo 6 S 8  (Cu 1 CP). Electrodes were fabricated from the synthesized Cu 1 Mo 6 S 8  (Cu 1 CP) and tested in 2016 coin cells using 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte in the voltage window of 0.5V-1.5V against pure Mg used as the anode following our published work [3]. Results of the electrochemical cycling are provided below. 
     Results 
       FIG.  1    shows the XRD pattern of the heat-treated Cu 2 CP powder obtained by the precursor route. The Bragg diffraction lines were indexed to a hexagonal-rhombohedral symmetry unit cell of Cu 2 Mo 6 S 8  (space group: R-3; number: 148; JCPDS-ICDD: 00-047-1519). Lattice parameter(s) calculated using the least-square method from the collected experimental data (a=0.96478 nm, c=1.02026 nm, and unit cell volume=822.42×10 −3  nm 3 ) were in good agreement with the standard Cu 2 Mo 6 S 8  unit cell parameters (a=0.9584 nm, c=1.025 nm, unit cell volume=815.36×10 −3  nm 3 ). Similarly,  FIG.  1    exhibits the XRD pattern obtained after removal of one copper from the heat-treated powder using the hydrochloric acid treatment. The Braggs lines were indexed with the hexagonal-rhombohedral symmetry unit cell of CuMo 6 S 8  phase (space group: R-3; number: 148; JCPDS-ICDD: 00-034-1379), and the calculated lattice parameter(s) (a=0.94412 nm, c=1.04761 nm, and unit cell volume=808.70×10 −3  nm 3 ) matched quite well with standard unit cell parameters of CuMo 6 S 8  obtained from the above ICDD database (a=0.94120 nm, c=1.04070 nm, unit cell volume=798.40×10 −3  nm 3 ). The calculated lattice parameters values are also consistent with the standard lattice parameter(s) values of pristine Cu 2 Mo 6 S 8  and acid leached CuMo 6 S 8  powder obtained from JCPDS-ICDD database suggesting that the 6M HCl treatment for 2 days was successful in leaching out 50% copper from the original Cu 2 CP structure and thus yielding Cu1Mo 6 S 8  (Cu 1 CP) (Table 6). 
     
       
         
           
               
             
               
                 TABLE 6 
               
             
            
               
                   
               
               
                 Calculated lattice parameter(s) of Cu 2 Mo 6 S 8  and Cu 1 Mo 6 S 8  along  
               
               
                 with cell parameter(s) with standard ICDD. 
               
            
           
           
               
               
               
               
            
               
                   
                   
                   
                 Unit cell volume  
               
               
                 Material 
                 a (Å) 
                 c (Å) 
                 (10 6  × pm 3 ) 
               
               
                   
               
            
           
           
               
               
               
               
            
               
                 HEMM derived Cu 2 Mo 6 S 8   
                 9.6478 
                 10.2026 
                 822.42 
               
               
                 Standard Cu 2 Mo 6 S 8  (ICDD:  
                 9.5840 
                 10.250 
                 815.36 
               
               
                 00-047-1519) 
                   
                   
                   
               
               
                 HCl leached CuMo 6 S 8   
                 9.4412 
                 10.4761 
                 808.70 
               
               
                 Standard CuMo 6 S 8  (ICDD:  
                 9.4120 
                 10.4070 
                 798.40 
               
               
                 00-034-1379) 
               
               
                   
               
            
           
         
       
     
       FIG.  2   a    displays the variation in specific capacity versus cycle number along with Coulombic efficiency of the acid leached Cu 1 Mo 6 S 8  electrode, cycled at a constant current of ˜20 mAg −1 (˜C/6 rate) in the potential window of 0.5-1.5 V using 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte. As observed in  FIG.  2   a   , the 1 st  cycle discharge and charge capacity of the Cu 1 Mo 6 S 8  electrode is ˜105 mAhg −1  and ˜78 mAhg −1 , respectively, with a 1 st  cycle irreversible loss of 25.7% (or Coulombic efficiency of ˜74.3%). However, from the 10 th  cycle onward we can see the electrode maintaining a steady charge-discharge capacity of ˜55 mAhg −1 , with a Coulombic efficiency of ˜99.9%. It is noted that a first cycle irreversible loss of ˜50% is seen for the Mo 6 S 8  CP obtained by completely leaching copper out of HEMM derived Cu 2 CP structures. The preliminary results obtained for Cu 1 CP is therefore encouraging and suggest that partial Mg 2+  charge entrapment which is common during the 1 st  cycle magnesiation (discharge) in Mo 6 S 8  cathode can be partially overcome with Cu 1 Mo 6 S 8  structure where one Mg 2+  can cycle without any hindrance.  FIG.  2   b    shows the galvanostatic charge-discharge profile (1 st , 2 nd , 3 rd , 10 th , 20 th , 50 th  and 90 th  cycle) of the Cu 1 Mo 6 S 8  electrode conducted at a constant current rate ˜20 mAg −1  (˜C/6). During the 1 st  cycle, a sloping voltage curve is observed for Mg 2+  insertion/extraction owing to kinetic limitation requiring slight overvoltage of ˜200-300 mV from the equilibrium magnesiation potential of ˜1.1 V. However, from 10 th , 20 th , 50 th , and 90 th  cycles onwards single reaction plateaus are observed at ˜1.1 V (Mg 2+  insertion) and at ˜1.2 V (Mg 2+  extraction), respectively.  FIG.  2   c    shows the rate capabilities of the Cu 1 Mo 6 S 8  electrode at various current rates of 5 mAg −1  (˜C/24), 10 mAg −1  (˜C/12), 20 mAg −1 (˜C/6), 30 mAg −1  (˜C/4), 40 mAg −1 (˜C/3), and 60 mAg −1  (˜C/2). The Cu 1 Mo 6 S 8  delivers average discharge capacity of ˜57 mAhg −1 , ˜56 mAhg −1 , ˜44 mAhg −1 , ˜40 mAhg −1 , ˜32 mAhg −1 , ˜29 mAhg −1  at ˜C/24, ˜C/12, ˜C/6, ˜C/4, ˜C/3, and ˜C/2 rates with Coulombic efficiency ˜97%, ˜100%, ˜98.6%, ˜98.7%, 99.1%, and ˜98.7%, respectively. 
     In order to understand the reaction mechanism, the Cu 1 CP electrode was cycled at a slow current rate of ˜5 mAg −1  (˜C/24 rate) within the potential window of 0.5-1.5 V using 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte in a Mg cell. The 1 st  cycle discharge (magnesiation) and charge (demagnesiation) capacity was observed ˜81 and ˜80 mAhg −1  with 1 st  cycle irreversible loss ˜1.23% implying partial Mg-ion trapping that is common to the Chevrel phase electrodes (Mo 6 T 8 , T═S, Se) can be avoided (see  FIG.  3   a   ). In the 2 nd  and 3 rd  cycle ˜99% Coulombic efficiency was observed. Noticeably, the differential capacity versus voltage curves (dQ/dV versus V) of the 2 nd  and 3 rd  cycle illustrates four pairs of redox peaks observed at ˜1.22 V, ˜1.15V, ˜1.1V, and ˜0.8V during discharge and ˜1.04V, ˜1.18V, ˜1.23V, and ˜1.32V during charge implying that the magnesiation/de-magnesiation reactions in the synthesized Cu 1 CP occurs in various stages (see  FIG.  3   b   ). In order to understand the phase formation, 2016 coin cells were cycled at a slow current rate of ˜5 mAg −1  between ˜0.5V and ˜1.5V cut-off voltage. The cells were then disassembled inside an UHP Ar filled glove box and washed with anhydrous tetrahydrofuran (THF) followed by vacuum drying. Ex-situ XRD analysis of the cycled electrodes compared with the bare electrode interestingly indicate partial copper leaching and simultaneous Mg-ion intercalation/de-intercalation with the formation of Cu 1-x Mg x CP and Cu 1-y Mg y CP (y&lt;x; x,y&lt;1) at the discharge and charge states, respectively (see  FIG.  3   c   ). In the 2 nd  cycle, complete copper leaching and exchange with one Mg-ion intercalation occurred during the discharge cycle with the formation of Mg 1 CP, whereas complete Mg-ion removal did not occur during the charge cycle leading to the formation of Cu 1-y Mg y CP (y&lt;1). In the subsequent cycles however, single Mg-ion intercalation along with partial copper leaching occurred between the two end members of Cu 1 CP and Mg 1 CP resulting in suppression of Mg-ion trapping akin to CP and thereby resulting in improved Coulombic efficiency. More importantly, it should be noted that the cycling data of Cu 1 CP between 2 nd -50 th  cycle at a slow current rate of ˜5 mAg −1  shows an average discharge-charge capacity of ˜55 mAhg −1  yielding a Coulombic efficiency ˜98% (see  FIG.  3   d   ). The interesting aspect is the ability of the Cu 1 CP to reversibly intercalate one Mg 2+  ion and also reversibly cycle Cu 2+  ion. 
     Example XV (Mo 6 S 8-x Se x  1&lt;x&lt;8) 
     Experimental: Synthesis of Cu 2 Mo 6 S 7 Se 1 /Mo 6 S 7 Se 1  by the High Energy Mechanical Milling (HEMM) Route 
     Stoichiometric amounts of MoS 2  (0.875 g), MoSe 2  (0.1426 g), Mo (0.579 g), CuS (0.35 g) and CuSe (0.0534 g) were batched in a SS vial (powder:ball ratio=1:10). The powders were mechanically milled for 3 h and subjected to XRD analysis. After 3 h milling, the powder was heat-treated at 1000° C. for 5 h under UHP Ar atmosphere. XRD pattern of the heat-treated powder shows the formation of fully crystalline, pure Cu 2 Mo 6 S 7 Se 1 . The resultant Cu 2 Mo 6 S 7 Se 1  was then subsequently washed with HCl/O 2  bubbling for 7 h and the XRD pattern collected on the leached material confirms the formation of Mo 6 S 7 Se 1  (see  FIG.  4   ). Electrodes were again fabricated as in the case of Example XIV. Accordingly, electrodes were fabricated from the synthesized Mo 6 S 7 Se 1  (CP) and tested in 2016 coin cells using 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte in the voltage window of 0.5V˜1.8V against pure Mg used as the anode following our published work. Results of the electrochemical cycling are provided below. 
     Results 
     The cyclic voltammogram (CV) in  FIG.  5   a    acquired at a sweep rate of ˜50 μVs −1  between 0.5-1.8 V versus Mg/Mg 2+  shows the magnesiation reaction (˜0.98V) and demagnesiation reaction (˜1.3 V, and ˜1.56 V) events occurring in the Mo 6 S 7 Se 1  electrode respectively, in the very 1 st  cycle. In the 2 nd  cycle, 2 pairs of magnesiation and demagnesiation peaks were observed at ˜1.08 V, ˜1.0 V, ˜1.3 V, ˜1.56 V, respectively.  FIG.  5   b    shows the variation of specific capacity versus cycle number along with Coulombic efficiency of the Mo 6 S 7 Se 1  electrode, cycled at a constant current of ˜20 mAg −1  (˜C/6 rate) in the potential window of 0.5-1.8 V using 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte. The galvanostatic cycling result shows a 1 st  cycle discharge (magnesiation) and charge (demagnesiation) capacity of ˜68.5 mAhg −1  (˜58% of the theoretical capacity of ˜115.6 mAhg −1 ) and ˜66.3 mAh·g −1 , respectively, with a Coulombic efficiency of ˜96.8%. Between the b  2   nd  and 200 th  cycles, an average discharge and charge capacity of ˜66 and 64 mAhg −1 , respectively, were observed with ˜97% Coulombic efficiency (see  FIG.  5   b   ). The capacity versus voltage profiles of the 2 nd , 100 th , and 200 th  cycles shown in  FIG.  5   c   , exhibiting two pairs of magnesiation (˜1.17 V and ˜1.13 V) and demagnesiation (˜1.17 V and ˜1.45 V) reaction plateaus, respectively, in agreement with the differential capacity versus voltage curves (see  FIG.  5   d   ). The results above show the ability of the sulfo-selenide CP to reversibly cycle Mg 2+  ions in the voltage window of 0.5V˜1.8V with respect to Mg. 
     Experimental: Synthesis of Cu 2 Mo 6 S 8-x Se x /Mo 6 S 8-x Se x  (x=3, 4, 5) by the HEMM Route 
     Cu 2 Mo 6 S 5 Se 3 /Mo 6 S 5 Se 3 : Stoichiometric amounts of MoS 2  (0.625 g), MoSe 2  (0.428 g), Mo (0.537 g), CuS (0.25 g) and CuSe (0.16 g) corresponding to the nominal composition of Cu 2 Mo 6 S 5 Se 3  were batched in a SS vial (powder:ball ratio=1:10). The powders were mechanically milled for 3 h and subjected to XRD analysis. After 3 h milling, the powder was heat-treated at 1000° C. for 5 h under UHP Ar atmosphere. XRD pattern of the heat-treated powder shows the formation of fully crystalline, pure Cu 2 Mo 6 S 5 Se3. The resultant Cu 2 Mo 6 S 5 Se 3  was washed with HCl/O 2  bubbling for 7 h and the XRD pattern collected on the resultant powder confirms the formation of Mo 6 S 5 Se 3  (see  FIG.  6   a   ). 
     Cu 2 Mo 6 S 4 Se 4 /Mo 6 S 4 Se 4 : Stoichiometric amounts of MoS 2  (0.5 g), MoSe 2  (0.57 g), Mo (0.516 g), CuS (0.23 g) and CuSe (0.214 g) corresponding to the nominal composition of Cu 2 Mo 6 S 4 Se 4  were batched in a stainless steel (SS) vial (powder:ball ratio=1:10). The powders were mechanically milled for 3 h and subjected to XRD analysis. After 3 h milling, the powder was heat-treated at 1000° C. for 5 h under UHP Ar atmosphere. XRD pattern collected on the heat-treated powder shows the formation of pure crystalline Cu 2 Mo 6 S 4 Se 4 . The resultant Cu 2 Mo 6 S 4 Se 4  was washed with HCl/O 2  bubbling for 7 h and the XRD collected on the acid treated powder confirms the formation of Mo 6 S 4 Se 4  (see  FIG.  6   b   ). 
     Cu 2 Mo 6 S 3 Se 5/ Mo 6 S 3 Se 8 : Stoichiometric amounts of MoS 2  (0.375 g), MoSe 2  (0.7125 g), Mo (0.495 g), CuS (0.15 g) and CuSe (0.2675 g) corresponding to the nominal composition of Cu 2 Mo 6 S 3 Se 5  were batched in a SS vial (powder:ball ratio=1:10). The powders were mechanically milled for 3 h and subjected to XRD analysis. After 3 h milling, the powder was heat-treated at 1000° C. for 5 h under UHP Ar atmosphere. XRD pattern collected on the heat-treated powder shows the formation of pure crystalline Cu 2 Mo 6 S3Se5. The obtained Cu 2 Mo 6 S 3 Se 5  was washed with HCl/O 2  bubbling for 7 h and the XRD collected on the acid treated powder confirms the formation of Mo 6 S 3 Se 5  (see  FIG.  6   c   ). 
     As outlined in EXAMPLE XIV and EXAMPLE XV above, electrodes were fabricated from the synthesized Mo 6 S 8-x Se x  (x=3, 4, 5) materials. Accordingly, electrodes were fabricated from the synthesized Mo 6 S 8-x Se x  (x=3, 4, 5) materials and tested in 2016 coin cells using 0.4 molar 2 (PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte in the voltage window of 0.5V˜1.5V for Mo 6 S 8-x Se x  (x=3, 4) and 0.5-1.75V for Mo 6 S 8-x Se x  (x=5) against pure Mg used as the anode following our published work. Results of the electrochemical cycling are provided below. 
     Results 
       FIG.  7   a    exhibits the variation of specific capacity versus cycle number along with Coulombic efficiency of the Mo 6 S 5 Se 3  electrode, cycled at a constant current of ˜20 mAg −1  (˜C/6 rate) in the potential window of 0.5-1.5 V using 0.4 molar 2 (PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte. As observed in  FIG.  7   a   , the 1 st  cycle discharge and charge capacity of the Mo 6 S 5 Se 3  electrode is ˜74.2 mAhg −1  and ˜52.5 mAhg −1 , respectively, with a 1 st  cycle irreversible loss of 29.3% (or coulombic efficiency of ˜70.7%). From the 2 nd  to 90 th  cycle however, we observed an average stable discharge and charge capacity of 50.8 mAhg −1  and ˜51.9 mAhg −1  with Columbic efficiency ˜97.9%.  FIG.  7   b    shows the galvanostatic charge-discharge profile (1 st , 2 nd 10 th , 20 th , and 50 th  cycle) of the Mo 6 S 5 Se 3  electrode obtained at a constant current rate ˜20 mAg −1  (˜C/6). During the 1 st  cycle, a single plateau is observed at ˜0.92 V for Mg 2+  insertion owing to the kinetic limitation in Mo 6 S 5 Se 3  electrode. However, for the 2 nd , 10 th , 20 th , and 50 th  cycle onwards sloping charge and discharge reaction plateaus are observed centered on ˜1.1 V/˜1.25 V for both Mg 2+  insertion/extraction reactions, respectively. 
       FIG.  8   a    illustrates the variation in specific capacity versus cycle number along with Coulombic efficiency obtained for the Mo 6 S 4 Se 4  electrode, cycled at a constant current of ˜20mAg −1 (˜C/6 rate) in the potential window of 0.5-1.5 V using 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte. As observed in  FIG.  8   a   , the 1 st  cycle discharge and charge capacity of the Mo 6 S 4 Se 4  electrode is ˜63 mAhg −1  and ˜43 mAhg −1 , respectively, with a 1 st  cycle irreversible loss of ˜31.7% (or Coulombic efficiency of ˜68.3%). From the 2 nd  to 100 th  cycle we observed an average stable discharge and charge capacity of ˜40.5 mAhg −1  and ˜38.7 mAhg −1  with Columbic efficiency ˜95.6%.  FIG.  8   b    shows the galvanostatic charge-discharge profile (1 st , 2 nd , 10 th , and 20 th  cycle) of Mo 6 S 4 Se 4  electrode obtained at a constant current rate ˜20 mAg −1  (˜C/6). During the 1 st  cycle, a single plateau is observed at ˜0.86 V for the Mg 2+  insertion owing to the kinetic limitation in the Mo 6 S 4 Se 4  electrode. However, for the 2 nd , 10 th , and 20 th  cycle onwards characteristic sloping reaction plateaus are observed as in the case of the Mo 6 S 5 Se 3  electrode. 
       FIG.  9   a    illustrates the variation of specific capacity versus cycle number along with Coulombic efficiency of the Mo 6 S 3 Se 5  electrode, cycled at a constant current of ˜20 mAg −1 (˜C/6 rate) in the potential window of 0.5-1.75 V using 0.4 molar 2(PhMgCl—AlCl 3 )/tetrahydrofuran electrolyte. As observed in  FIG.  9   a   , the 1 st  cycle discharge and charge capacity of the Mo 6 S 3 Se 5  electrode is ˜78 mAhg −1  and ˜63 mAhg −1 , respectively, with a 1 st  cycle irreversible loss of ˜19.2% (or Coulombic efficiency of ˜80.8%). From the 2 nd  to 200 th  cycle however, we observed an average discharge and charge capacity of ˜60.6 mAhg −1  and ˜63.5 mAhg −1  with Columbic efficiency ˜95.6%.  FIG.  9   b    shows the galvanostatic charge-discharge profile (1 st , 2 nd , 10 th , 20 th , and 50 th  cycle) of Mo 6 S 3 Se 5  electrode obtained at a constant current rate ˜20 mAg −1  (˜C/6). During the 1 st  cycle, a single reaction plateau is observed at ˜0.74 V for Mg 2+  insertion owing to the kinetic limitation in Mo 6 S 3 Se 5  electrode. However, for the 2 nd , 10 th , 20 th , and 50 th  cycles onwards, characteristic sloping reaction plateaus are observed. 
     Rate Capability 
       FIG.  10    shows the rate capabilities of the synthesized Mo 6 S 5 Se 3  and Mo 6 S 4 Se 4  electrodes at various current rates of 5 mAg −1  (˜C/24), 10 mAg −1  (˜C/12), 30 mAg −1  (˜C/4), 40 mAg −1 (˜C/3), and 60 mAg −1  (˜C/2). The Mo 6 S 5 Se 3  electrode delivers average discharge capacity of ˜50 mAhg −1 , ˜42 mAhg −1 , ˜26 mAhg −1 , ˜23 mAhg −1 , ˜19 mAhg −1  at ˜C/24, ˜C/12, ˜C/4, ˜C/3, and ˜C/2 rates whereas, the Mo 6 S 4 Se 4  electrode delivers an average discharge capacity of ˜42 mAhg −1 , ˜34 mAhg −1 , ˜25 mAhg −1 , ˜20 mAhg −1 , ˜7 mAhg −1  at ˜C/24, ˜C/12, ˜C/4, ˜C/3, and ˜C/2 rates, respectively. 
     In summary, it is important to note that both Cu 2 CP and Cu 1 CP combined with sulfo-selenide substituted forms of Mo 6 S 7 Se 1 ; Mo 6 S 5 Se 3 ; Mo 6 S 4 Se 4 ; Mo 6 S 3 Se 5  were successfully synthesized using the high energy mechanical milling (HEMM) approach. The resultant materials were then successfully converted to the desired Chevrel phase (CP) following heat treatments in ultra-high purity (UHP) Ar environment at temperature of 1000° C. for 5 h and then with appropriate acid leaching treatments in 6M HCl and a mixture of HCl/O 2  gas bubbling to form the partially-cuprated and de-cuprated substituted sulfo-selenide systems. All of the leached partially-cuprated/de-cuprated Chevrel phases are indeed electrochemically active showing stable capacities in the 51 mAhg −1 -66 mAg −1 . Increasing amounts of Se substitution in the CP phase results in the CP system exhibiting the highest specific capacity of ˜66 mAhg −1 . 
     Whereas particular embodiments of the invention have been described herein for purposes of illustration, it will be evident to those skilled in the art that numerous variations of the details may be made without departing from the invention as set forth in the appended claims.