Abstract:
A composite of silicon and tin is prepared as a negative electrode composition with increased lithium insertion capacity and durability for use with a metal current collector in cells of a lithium-ion battery or a lithium-sulfur battery. This negative electrode material is formed such that the silicon is present as a distinct amorphous phase in a matrix phase of crystalline tin. While the tin phase provides electron conductivity, both phases accommodate the insertion and extraction of lithium in the operation of the cell and both phases interact in minimizing mechanical damage to the material as the cell experiences repeated charge and discharge cycles. In general, roughly equal atomic proportions of the tin and silicon are used in forming the phase separated composite electrode material.

Description:
[0001]    This application is a continuation-in-part of Ser. No. 13/234209, filed on Sep. 16, 2011, now U.S. Patent Application Publication No. 2013-0071736. The complete contents of that application are incorporated herein by reference. 
     
    
     TECHNICAL FIELD 
       [0002]    This invention pertains to the preparation of negative electrode materials that are suitable for both lithium-ion and lithium-sulfur batteries. More specifically, this invention pertains to the preparation and use of composite particles that contain nanoscale islands of amorphous silicon phases embedded in crystalline or amorphous tin phases as negative electrode material for cyclic insertion and extraction of lithium in the operation of a lithium-ion battery or a lithium-sulfur battery. The combination of suitable atomic proportions of tin and silicon, and the sizes of the respective phases in such composites enables the insertion of increased amounts of lithium over repeated electrochemical cycles with less damage to the particulate negative electrode material. 
       BACKGROUND OF THE INVENTION 
       [0003]    Lithium-ion batteries are used as electric storage systems for powering electric and hybrid electric vehicles. These batteries comprise a plurality of suitably interconnected electrochemical cells arranged to provide a predetermined electrical current at a specified electrical potential. In each such cell, lithium is transported as lithium ions from a negative electrode through a non-aqueous, lithium-containing, electrolyte solution to a lithium-ion-accepting positive electrode as an electronic current is delivered from the battery to an external load, such as an electric traction motor. A suitable porous separator material, infiltrated with the electrolyte solution and permeable to the transport of lithium ions in the electrolyte, is employed to prevent short-circuiting physical contact between the electrodes. Graphite has been used as a negative electrode material and bonded in a thin electrode layer on a copper current collector. During charging of the cells, lithium is inserted into the graphite (lithiation, forming LiC 6 , about 372 mAh/g) and extracted from the graphitic carbon during discharging (delithiation). A suitable particulate material for receiving and storing inserted lithium during discharge of each cell is used as the positive electrode material. Examples of such positive electrode materials include lithium cobalt oxide (LiCoO 2 ), a spinel lithium transition metal oxide such as spinel lithium manganese oxide (LiMn X O Y ), a lithium polyanion such as a nickel-manganese-cobalt oxide [Li(Ni X Mn Y Co Z )O 2 ], lithium iron phosphate (LiFePO 4 ), or lithium fluorophosphate (Li 2 FePO 4 F), or a mixture of any of these materials. Suitable positive electrode materials are often bonded as a thin layer to an aluminum current collector. The electrochemical potential of such lithium ion cells is typically in the range of about 2 to 4.5 volts. 
         [0004]    The use of lithium-ion batteries to power electric motors in automotive vehicles has led to the need for higher gravimetric and/or volumetric capacity batteries. While graphitic carbon is a durable and useful lithium-intercalating, negative electrode material for lithium-ion cells, it has a relatively low capacity for such lithium insertion. Other potential negative electrode materials such as silicon (theoretical capacity, 3600 mAh/g for Li 15 Si 4 ) and tin (theoretical capacity, 992 mAh/g for Li 22 Sn 5 ) have much higher theoretical capacities than graphite for lithium insertion. However, the volume change of up to 300 volume percent for silicon during lithiation and delithiation processes leads to fracture of the active silicon material and/or loss of electrical contact with the conductive additives or the current collectors. And tin has the same problem of a large volume expansion upon lithiation, leading to rapid capacity degradation. 
         [0005]    Lithium-sulfur batteries, like lithium-ion batteries, are rechargeable. They are also notable for their high energy density. The low atomic weight of lithium and the moderate weight of sulfur enable lithium-sulfur batteries to be relatively light. Like lithium-ion cells, the anode or negative electrode of the lithium-sulfur cell includes lithium. During lithium-sulfur cell discharge lithium is dissolved into an electrolyte from the anode surface, transported in the electrolyte (e.g., a molten or liquid alkali metal polysulfide salt) through a porous separator to a cathode (positive electrode during cell discharge) which comprises a polysulfide (e.g., S 8 ). Upon reaching the cathode, lithium atoms progressively reduce the polysulfide to a lithium sulfur composition (e.g., Li 2 S 3 ). The chemical changes are reversed when the lithium-sulfur cell is recharged. The light weight and high energy density of lithium-sulfur cells make lithium-sulfur batteries good candidates for vehicle propulsion systems and other electrical energy consuming devices. 
         [0006]    The basic mechanism responsible for the loss of capacity of a battery due to fracture of the electrode materials in its cells is the loss of electrical contact with conductive material and the creation of new surfaces, which irreversibly consume the active lithium to form new solid electrolyte interfaces. Both problems shorten the effective cycling capacity of a battery. There remains a need for a more effective way or material form of utilizing silicon or tin in negative electrodes of lithium-ion cells and lithium-sulfur cells. 
       SUMMARY OF THE INVENTION 
       [0007]    In accordance with embodiments of this invention, an improved negative electrode material is formed by combining silicon and tin as intermixed, but immiscible, solid phases. The material is suitable for use in negative electrodes for both lithium-ion batteries and lithium-sulfur batteries. A particulate composite of silicon and tin is formed in which the silicon and tin are phase-separated. Both phases are receptive to the insertion and extraction of lithium atoms. The composite is formed with a two-phase or multi-phase structure that is nanometer to micrometer in characteristic length and is achieved by controlling the synthesis process to produce the mixed phases to be below the critical size for the generation of micro-cracks due to the repeated insertion of lithium into the mixed phases. In a preferred embodiment, confined particulate architectures are formed wherein the silicon phases are separated in a tin phase matrix. Such a microstructure provides several advantages: (1) the tin phase is electrically conductive, which enables electrons to reach the island-like silicon phase particles, (2) the diffusion of lithium in tin is much faster than in silicon, which can reduce the concentration gradient of lithium ions through the larger composite particles of silicon and tin, in effect reducing the diffusion induced stress to mitigate the fracture of the larger composite particles, (3) if a crack is generated in the composite material, the relatively soft tin matrix tends to absorb the elastic strain energy and prevent the micro-cracks from propagating, and (4) the immiscible characteristics of silicon and tin and their phase separation minimizes electrochemical sintering and thus prevents coalescence of the particles that would otherwise lead to rapid mechanical degradation of the electrode material. 
         [0008]    The phase separated particle composites may be produced, for example, by rapid solidification practices (e.g., melt spinning) from a homogeneous liquid mixture of elemental tin and silicon. In another example, phase separated composites may be formed by sputtering of separate sources of tin and silicon and co-depositing phase separated mixtures of tin and silicon in predetermined proportions as an electrode film on a suitable surface, such as a copper current collector. In general, it is preferred to prepare a phase separated composite of about forty to sixty atomic percent of silicon and the balance tin for negative electrode materials for lithium-ion cells and lithium-sulfur cells. 
         [0009]    In accordance with practices of the invention, the mechanical degradation that occurs when pure tin or silicon is used for lithium insertion is thus mitigated by tuning the Si/Sn ratio of the tin-silicon composite. We also demonstrate that at suitable Si/Sn ratios, phase separation occurs with amorphous phase clusters of silicon being embedded in a generally continuous phase of crystalline or amorphous tin. The resulting negative electrode materials exhibit significant improvements in charge storage capability along with excellent cycling stability. 
         [0010]    Thus, in accordance with practices of the invention, phase separated composites of tin and silicon are formed as relatively thin layers on a suitable current collector for use as negative electrode material in the cells of a lithium-ion battery or in the cells of a lithium-sulfur battery. By thus using this phase separated combination of tin and silicon, the lithium-insertion capacity of each cell is increased to improve the volumetric and/or gravimetric capacity of lithium-ion batteries and lithium-sulfur batteries. When the phase separated composites of tin and silicon are to be used as negative electrode material in the cells of a lithium-sulfur battery it may be preferred to introduce the required amount of lithium into the negative electrode material before the negative electrode is assembled into a battery. 
         [0011]    Other objects and advantages of the invention will be apparent from a detailed description of practices of embodiments of the invention which follows in this specification. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0012]      FIG. 1  is an enlarged schematic illustration of a few electrochemical cells of an exemplary lithium-ion battery arrangement. Each cell includes a thin, rectangular negative electrode that may include the phase separated tin and silicon composite material of this invention, a like-shaped positive electrode, and a separator sandwiched between that electrodes. 
           [0013]      FIG. 2  is a further enlarged and exploded cross-sectional view of one of the electrochemical cells shown in  FIG. 1 .  FIG. 2  also illustrates the metallic current collectors that support the respective electrode materials. The elements of the cell are shown separated for illustration, but they are actually in compressed face-to-face contact and the electrode materials are formed on, or bonded to, their respective current collectors. 
           [0014]      FIGS. 3A-3C  are scanning electron microscope images (SEM) illustrating the surface morphologies of phase separated Si n Sn 1-n  compositions formed by sputtering of tin and silicon from separate targets onto a copper strip substrate. In  FIG. 3A  the composition in atomic percent proportions is Si 40 Sn 60 , in  FIG. 3B  the composition is Si 48 Sn 52 , and in  FIG. 3C  the composition is Si 68 Sn 32 . 
           [0015]      FIGS. 4A and 4B  are High Angle Angular Dark Field (HAADF) scanning transmission electron microscope (STEM) images showing the phase separation of silicon and tin in films produced by sputtering. Silicon is the darker phase and tin is the brighter phase.  FIG. 4A  is of higher silicon content (about 60 atomic percent silicon and the balance tin) and  FIG. 4B  is of lower silicon content (about thirty atomic percent silicon). 
           [0016]      FIGS. 5A and 5B  are galvanostatic charge curves (Potential, Volts, Li/Li +  vs. Charge Capacity mAh/cm 2 ) at a rate of C/10 for five indicated different tin/silicon compositions.  FIG. 5A  is at the second cycle and  FIG. 5B  is at the twentieth cycle. 
           [0017]      FIG. 6  is a graph of Charge capacity, mAh/g vs. Cycle number for five indicated different tin/silicon compositions. 
       
    
    
     DESCRIPTION OF PREFERRED EMBODIMENTS 
       [0018]    An exemplary and generalized illustration of a lithium-ion battery  10  is depicted in  FIG. 1 . The lithium-ion battery  10  shown here includes several thin rectangular-shaped electrochemical battery cells  12  that are each bracketed by metallic current collectors. The electrochemical battery cells  12  are stacked side-by-side in a modular configuration and, in this example, connected in parallel. A lithium-ion battery  10  may be formed of many like electrochemical cells in electrical series or in parallel connection to form a lithium ion battery that exhibits the voltage and current capacity demanded for a particular application. It should be understood the lithium ion battery  10  shown here is only a schematic illustration.  FIG. 1  is presented to show the relative position and physical interactions of the various components that constitute the electrochemical battery cells  12  (i.e., the electrodes and the separator); it is not intended to inform the relative sizes of the electrochemical battery cells&#39; components, to define the number of electrochemical battery cells  12  in the lithium ion battery  10 , or to limit the wide variety of structural configurations the lithium ion battery  10  may assume. 
         [0019]    The electrochemical cell  12  (one indicated) contained in the lithium ion battery  10  includes a negative electrode  14 , a positive electrode  16 , and the separator  18  situated between the two opposing electrodes  14 ,  16 . Each of the negative electrode  14 , the positive electrode  16 , and the separator  18  is wetted with a liquid electrolyte solution that enables the transport of lithium ions between the electrodes  14 ,  16 . A negative-electrode metallic current collector  20  (typically, copper) that includes a negative polarity tab  22  is located between the back-to-back negative electrodes  14  of adjacent electrochemical cells  12 . Likewise, a positive-side metallic current collector  24  (typically, aluminum) that includes a positive polarity tab  26  is located between neighboring positive electrodes  16 . The negative polarity tab  22  is electrically coupled to a negative terminal  28  and the positive polarity tab  26  is electrically coupled to a positive terminal  30 . Each electrode material  14 ,  16  is typically formed on or bonded to its respective metallic current collector  20 ,  24 . An applied compressive force usually presses the metallic current collectors  20 ,  24  and their electrodes  14 ,  16  against the separator  18  to achieve intimate interfacial contact between adjacent contacting components. Negative terminal  28  and positive terminal  30  are connected to an electrical power consuming load  50 . For example, a suitable battery pack comprising many like individual cells may be provided to power an electric traction motor to drive the wheels in an automotive vehicle. In such a battery pack many cells are connected in groups in electrical parallel arrangement for providing suitable energy capacity and many groups are connected in series to provide a suitable electrical voltage potential. 
         [0020]    An exploded cross-sectional view of the electrochemical battery cell  12  and its associated metallic current collectors  20 ,  24  is generally illustrated in  FIG. 2 . The negative electrode  14  includes an inner face surface  32  and an outer face surface  34  relative to the location of the separator  18 . The positive electrode  14  similarly includes an inner face surface  36  and an outer face surface  38 . The inner face surface  32  of the negative electrode  14  may, but is not required to, encompass a larger two-dimensional surface area than the inner face surface  36  of the positive electrode  16 , as shown. When assembled into the electrochemical battery cell  12 , the inner face surfaces  32 ,  36  of the negative and positive electrodes  14 ,  16  confront one another and are pressed against a negative-side major face surface  40  and a positive-side major face surface  42  of the separator  18 , respectively. Such pressed-engagement occurs generally uniformly along the entire interface of the major face surfaces  40 ,  42  of the separator  18  and the corresponding portions of the inner face surfaces  32 ,  36  of the electrodes  14 ,  16 . The negative-side metallic current collector  20  is formed on or joined to the outer face surface  34  of the negative electrode  14  and the positive-side metallic current collector  24  is formed on or joined in electrical contact with the outer face surface  38  of the positive electrode  16 . In many embodiments of this invention a composite tin-silicon negative electrode material is formed directly on the surfaces of a copper negative electrode current collector  20  Both of the metallic current collectors  20 ,  24  engage their respective electrode outer face surfaces  34 ,  38  over an appreciable interfacial surface area to facilitate the efficient collection and conduction of free electrons. 
         [0021]    In many lithium-ion batteries the elements of electrochemical cells  12  are made of materials such that they are generally thin and flexible. By way of illustrative example, a typical thickness (T in  FIG. 2 ) of the electrochemical cell  12  extending from the outer face surface  34  of the negative electrode  12  to the outer face surface  38  of the positive electrode  16  may about 80 μm to about 350 μm. Each electrode  14 ,  16  may be about 30 μm to 150 μm thick and the separator  18  may be about 20 μm to 50 μm thick. The metallic current collectors  20 ,  24  may be about 5 μm to 20 μm thick. The relatively thin and flexible nature of the elements of the electrochemical cell  12  and its associated metallic current collectors  20 ,  24  allows them to be rolled, folded, bent, or otherwise maneuvered into a variety of lithium-ion battery configurations depending on design specifications and spatial constraints. The lithium ion battery  10  may, for example, include a number of distinct electrochemical cells  12  that have been fabricated, cut, aligned, and laid-up next to one another or, in an alternative embodiment, the cells  12  may be derived from a continuous layer that is folded back-and-forth over itself many times. 
         [0022]    While lithium-ion batteries have been continually developed and used, for example, to power traction motors and the like for automotive vehicles, lithium-sulfur batteries are now being considered for such applications. As described, lithium-sulfur cells also employ a lithium-containing negative electrode (anode), and electrode material, that functions electrochemically like the negative electrode of a lithium-ion cell or battery. Accordingly, the silicon-tin compositions and microstructures described further in this specification are suitable for the intercalation of lithium whether the negative electrode material is used in a lithium-ion battery or in a lithium-sulfur battery. When a negative electrode is being prepared with a layer of the silicon-tin composites of this invention as the negative electrode material, it is necessary to provide for the introduction of a predetermined quantity of lithium into the electrode materials of the cell. In a preferred embodiment, a specified quantity of lithium may be incorporated (lithiated) into the silicon-tin composite material, for example, by electrochemical insertion, electroplating, vacuum deposition, or physical contact with lithium metal in the presence of a suitable electrolyte. In another embodiment, a suitable quantity of lithium may be introduced into the sulfur-containing positive electrode material before the assembly of the elements of the lithium-sulfur cell. During initial charging of the assembled cell or battery, lithium would be transported through the electrolyte and inserted into the composite silicon-tin negative electrode material. 
         [0023]    Practices of this invention are directed to the formation of higher current capacity and more durable materials for negative electrodes of lithium-ion and lithium-sulfur electrochemical cells. Phase separated composites of tin and silicon are prepared for this purpose. 
         [0024]    Several combinations of atomic proportions of Si and Sn were co-deposited as composite thin films in a Gamma 1000 sputtering system (Surrey Nanosystems, UK). Twelve thin film combinations of silicon and tin were prepared, including respectively, in atomic percent, 22.7%, 27.2%, 34.4%, 39.9%, 42.7%, 48.1%, 57.6%, 64.4%, 66.3%, 71.5%, 77.3, and 81.8% silicon and the balance tin. In each preparation a roughened copper foil was used to provide good adhesion between the sputtered Si—Sn thin films and the copper current collector. The deposition plasma for each constituent material (Si and Sn) was created with RF and DC power, respectively, applied to two magnetron guns under an argon flow of 14 sccm. The deposition rates of tin and silicon were separately controlled to obtain the above specified different atomic proportions of these elements. The dynamic pressure during the growth of the films was 3 mTorr, and the substrate was kept at room temperature. 
         [0025]    Ex situ X-ray diffraction (XRD) was used to study the structures of the thin films deposited on the Cu current collectors. All samples were examined using Cu Kα radiation in a Bruker AXS general area detector diffractometer system (GADDS). The diffraction images were collected for a period of 5 min with a 0.5-mm collimator and a sample-to-detector distance of 150 mm. The composition of each sample pad was determined by electron probe microanalysis (EPMA), while selected samples were characterized with JEOL 2100F AC transmission electron microscope operating at 200 kV. Scanning transmission electron microscopy (STEM) images were collected using a high angle annular dark field (HAADF) detector. 
         [0026]    All electrochemical experiments were carried out in Swagelok cells inside an argon-filled glove box. Pure lithium metal was used for the counter electrode for the half-cell tests. The electrolyte solution was 1 M LiPF 6  in ethylene carbonate (EC) and dimethyl carbonate (DMC) (1:1 v/v). A Celgard 3501 (1 μm thick microporous polypropylene film with 40% porosity) was used as the separator. Galvanostatic tests for all samples were performed with an Arbin BT-2000 battery testing station at a cycling voltage between 10 mV to 1.5 V (relative to a Li/Li +  electrode). 
         [0027]    The XRD results included the strong Cu diffraction peaks observed from the substrate and revealed several Sn peaks, indicating that the Sn phase was crystalline. No Si diffraction peaks were detected, indicating the amorphous nature of the Si. This was expected since the deposition temperature is too low for Si to develop a crystalline phase. No peaks representing any other Si—Sn phase were observed in any of the sputtered samples examined, which clearly demonstrated that the Si and Sn were phase separated, in agreement with the known immiscibility of Si and Sn. This nanostructure induced by phase separation is very critical to significantly improve its electrochemical performance. The overall mechanism for this will be further described in this specification. 
         [0028]    Based on the well-known Scherrer equation, the average Sn crystallite size estimated from the several X-ray diffraction patterns in was 20 to 50 nm. Those sputtered films containing higher Si contents led to smaller Sn grains, as confirmed from the SEM images in  FIGS. 3A-3C , which show that the surface morphology associated with the Sn grain size becomes rougher with increasing Si content. With the high sensitivity to atomic number contrast, detailed insight was gained with HAADF STEM imaging. As shown in  FIGS. 4A and 4B , the phase separation between the Sn (bright features) and the Si (dark features) results in discrete amorphous Si nanoparticles dispersed in a continuous crystalline Sn matrix. The Si particle size ranged from 30 to 70 nm for high Si contents (about sixty atomic percent silicon in  FIG. 4A ), with an average value of 50 nm, and decreased with decreasing amounts of Si in the alloy (about thirty atomic percent silicon in  FIG. 4B ). The Sn thickness between the Si particles was around 20 nm for the high Si content alloy, and increased with decreasing Si. 
         [0029]    The effects of Si/Sn composition ratios on galvanostatic charge/discharge behaviors were evaluated. A comparison of Si—Sn films with five of the different Si/Sn composition ratios at a charge rate of C/10 is shown in  FIG. 5A  (2 nd  cycle) and  5 B (20 th  cycle). During the initial cycles (as represented in the second cycle,  FIG. 5A ), the cell capacities are higher with increasing Si content, since the theoretical capacity of Li 15 Si 4  (3580 mAh/g) is much larger than that of Li 4,4 Sn (992 mAh/g). However, at very high Si content (Si 92 /Sn 8 ), the capacity was lower (around 2400 mAh/g,  FIG. 6 ) suggesting that not all the Si is accessible to accommodate the Li-ions due to the dramatic volume change that occurs, and also the high intrinsic resistance of Si. Referring still to  FIGS. 5A and 5B , the voltage profiles of Si—Sn alloys also reflected the charge characteristics of each individual Si and Sn phase. For example, for a high Sn content, one can clearly observe multiple constant-voltage plateaus for crystalline Sn. These plateaus correspond to different solid-solution regions wherein each plateau represents regions of co-existence of two-phases: Li 22 Sn 5 —Li 7 Sn 3 , Li 7 Sn 3 —LiSn, LiSn—Li 2 Sn 5 , and Li 2 Sn 5 —Sn, during the Li +  extraction process from 0 to 1V. As the Sn content decreases, the constant-voltage plateaus of Sn become less visible while a broad constant voltage plateau becomes apparent near 0.4 V. This broad featureless voltage characteristic is a typical representation of amorphous Si during charge (Si alloy delithiation process). This distinguishing characteristic feature from both Si and Sn further demonstrates that the Si and Sn were phase separated from each other. 
         [0030]    We also investigated the effects of Si/Sn composition ratios on cycling stability.  FIG. 5B  shows the charge characteristics of Si—Sn films after 20 cycles. The constant-voltage plateaus of crystalline Sn faded upon cycling; indicating that the Sn is tending to became amorphous. The cycling performance of all five Si—Sn samples is also summarized in  FIG. 6 . While the capacity retention of 65:35 and 46:54 at. % (Sn:Si) ratios were better than those with high Si content, the 46 Sn:54 Si ratio was the most promising composition because of its high specific charge capacity. At 1400 mAh/g, the electrode reached 90% of its theoretical capacity (1550 mAh/g). This composition offers a good balance between electrical conductivity and the ability to accommodate the large volume expansion. 
         [0031]    In general, it is preferred to employ silicon/tin compositions which are close to a fifty-fifty atomic percent mixture of the two elements. Suitable mixtures include forty to sixty atomic percent of silicon and the balance tin. These compositions are found to provide improved charge capacity for a greater number of charge and discharge cycles. The compositions are prepared by a method that forms thin films of the silicon/tin composite with the elements in separated phases in which the silicon phase is amorphous and the tin phase is initially crystalline. Preferably, the amorphous silicon phase is dispersed in a crystalline tin matrix phase. 
         [0032]    The phase separated tin-silicon compositions may be prepared by a rapid solidification process from a homogenous melt of suitable proportions of tin and silicon. For example, the process may be practiced as follows: 
         [0033]    1. Elemental silicon and tin are melted together in a predetermined atomic proportion. In many embodiments of the invention prepared proportions lie in the range of forty to sixty atomic percent silicon and the balance tin. 
         [0034]    2. The melt is progressively rapidly solidified to form particles, flakes, or ribbons. 
         [0035]    3. The particles are comminuted, such as by cryogenic ball milling at a suitably low temperature below 0° C. and down to −30° C. in inert atmosphere in order to avoid oxidation of the particles, to form generally uniformly shaped particles of one to five microns or so (or smaller) in largest dimension. 
         [0036]    4. In some embodiments, the particles may be annealed, if necessary, to induce phase separation by forming nanoscale islands of amorphous silicon phases embedded in a tin matrix. Such phase separated composite particles of silicon and tin are considered the active material for a negative electrode of a lithium-ion cell or a lithium-sulfur cell. 
         [0037]    5. The particles of active material are bonded to a suitable metal current collector, preferably a copper current collector in forming a negative electrode. For example, particles of active electrode material may be mixed with a suitable polymeric binder, such as polyvinylidene difluoride (PVDF) and carbon black in a weight ratio for example of 80:10:10. An inert liquid vehicle may be temporarily used for distributing the mixture over one or both opposing surfaces of a thin current collector strip. The liquid vehicle is removed and the mixture bonded to the collector film surfaces with the polymer binder. The electrical conductivity of the silicon-tin composite is further increased by the particles of carbon black. 
         [0038]    Thus, the phase separated films are suitably formed over a predetermined area and to a determined thickness on a copper current collector for assembly as the negative electrode material into lithium-ion electrochemical cells or lithium-sulfur electrochemical cells. Lithium may be introduced into the silicon-tin composite negative electrode material during the making of the electrode or during initial charging or other operation of the cell. The total amount of the negative electrode material and its lithium content is selected to provide a desired electrode capacity for the respective cell. 
         [0039]    Practices of the invention have been described for purposes of illustration and not of limitation of the scope of the invention.