Aspects of the present disclosure relate to electrode materials including silicon oxide and single-walled carbon nanotubes (SWCNTs), and in particular, to anodes including the electrode materials, and lithium ion batteries including the anodes.
Lithium (Li) ion electrochemical cells typically require materials that enable high energy density, high power density and high cycling stability. Li ion cells are commonly used in a variety of applications, which include consumer electronics, wearable computing devices, military mobile equipment, satellite communication, spacecraft devices and electric vehicles, and are particularly popular for use in large-scale energy applications such as low-emission electric vehicles, renewable power plants, and stationary electric grids. Additionally, lithium-ion cells are at the forefront of new generation wireless and portable communication applications. One or more lithium ion cells may be used to configure a battery that serves as the power source for any of these applications. It is the explosion in the number of higher energy demanding applications, however, that is accelerating research for yet even higher energy density, higher power density, higher-rate charge-discharge capability, and longer cycle life lithium ion cells. Additionally, with the increasing adoption of lithium-ion technology, there is an ever increasing need to extend today's energy and power densities, as applications migrate to higher current needs, longer run-times, wider and higher power ranges and smaller form factors.
Active anode materials such as silicon are a desirable replacement for current graphite based anodes due to their high lithium storage capacity that can exceed 7× that of graphite (up to 3200 mAh/g). However, due to the large volume expansion of alloy particles upon lithiation, these anode materials typically exhibit extremely poor cycle life due to mechanical stress, low coulombic efficiency and electrical disconnection.
Accordingly, there is a need for an advanced anode active material for use in an electrochemical cell that incorporates carbon materials of defined quality characteristics that favorably impact electrochemical cell cyclability.
An embodiment of the present disclosure provides an electrode material for a lithium ion secondary battery which contains an active material particles comprising an alkali metal or an alkali earth metal silicate, a binder, and single-walled carbon nanotubes (SWCNTs). In one embodiment, the electrode material comprises, based on a total weight of the electrode material, at least about 80 wt % of a combination of graphite particles and the metal silicate particles, from about 1 wt % to about 5 wt % of a binder, and from about 0.05 wt % to about 1 wt % single-walled carbon nanotubes (SWCNTs).
The various embodiments will be described in detail with reference to the accompanying drawings. Wherever possible, the same reference numbers will be used throughout the drawings to refer to the same or like parts. References made to particular examples and implementations are for illustrative purposes, and are not intended to limit the scope of the invention or the claims.
It will be understood that when an element or layer is referred to as being “on” or “connected to” another element or layer, it can be directly on or directly connected to the other element or layer, or intervening elements or layers may be present. In contrast, when an element is referred to as being “directly on” or “directly connected to” another element or layer, there are no intervening elements or layers present. It will be understood that for the purposes of this disclosure, “at least one of X, Y, and Z” can be construed as X only, Y only, Z only, or any combination of two or more items X, Y, and Z (e.g., XYZ, XYY, YZ, ZZ).
Where a range of values is provided, it is understood that each intervening value, to the tenth of the unit of the lower limit unless the context clearly dictates otherwise, between the upper and lower limit of that range and any other stated or intervening value in that stated range is encompassed within the invention. The upper and lower limits of these smaller ranges may independently be included in the smaller ranges is also encompassed within the invention, subject to any specifically excluded limit in the stated range. Where the stated range includes one or both of the limits, ranges excluding either or both of those included limits are also included in the invention. It will also be understood that the term “about” may refer to a minor measurement errors of, for example, +/−5% to 10%.
Words such as “thereafter,” “then,” “next,” etc. are not necessarily intended to limit the order of the steps; these words may be used to guide the reader through the description of the methods. Further, any reference to claim elements in the singular, for example, using the articles “a,” “an” or “the” is not to be construed as limiting the element to the singular.
An “electrode material” is defined as a material that may be configured for use as an electrode within an electrochemical cell, such as a lithium ion rechargeable battery. An “electrode” is defined as either an anode or a cathode of an electrochemical cell. A “composite electrode material” is also defined to include active material particles combined with one of particles, flakes, spheres, platelets, sheets, tubes, fibers, or combinations thereof and that are of an electrically conductive material. The particles, flakes, spheres, platelets, sheets, tubes, fibers or combinations thereof may further be one of flat, crumpled, wrinkled, layered, woven, braided, or combinations thereof.
The electrically conductive material, may be selected from the group consisting of an electrically conductive carbon-based material, an electrically conductive polymer, graphite, a metallic powder, nickel, aluminum, titanium, stainless steel, and any combination thereof. The electrically conductive carbon-based material may further include one of graphite, graphene, diamond, pyrolytic graphite, carbon black, low defect turbostratic carbon, fullerenes, or combinations thereof. An “electrode material mixture” is defined as a combination of materials such as: material particles (either electrochemically active, electrically conductive, composite or combinations thereof), a binder or binders, a non-crosslinking and/or a crosslinking polymer or polymers, which are mixed together for use in forming an electrode for an electrochemical cell. An “electrochemically active material”, “electrode active material” or “active material” is defined herein as a material that inserts and releases ions such as ions in an electrolyte, to store and release an electrical potential. The term “inserts and releases” may be further understood as ions that intercalate and deintercalate, or lithiate and delithiate. The process of inserting and releasing of ions is also understood, therefore, to be intercalation and deintercalation, or lithiation and delithiation. An “active material” or an “electrochemically active material” or an “active material particle”, therefore, is defined as a material or particle capable of repeating ion intercalation and deintercalation or lithium lithiation and delithiation.
As defined herein a secondary electrochemical cell is an electrochemical cell or battery that is rechargeable. “Capacity” is defined herein as a measure of charge stored by a battery as determined by the mass of active material contained within the battery, representing the maximum amount of energy, in ampere-hours (Ah), which can be extracted from a battery at a rated voltage. Capacity may also be defined by the equation: capacity=energy/voltage or current (A)×time (h). “Energy” is mathematically defined by the equation: energy=capacity (Ah)×voltage (V). “Specific capacity” is defined herein as the amount of electric charge that can be delivered for a specified amount of time per unit of mass or unit of volume of active electrode material. Specific capacity may be measured in gravimetric units, for example, (Ah)/g or volumetric units, for example, (Ah)/cc. Specific capacity is defined by the mathematical equation: specific capacity (Ah/kg)=capacity (Ah)/mass (kg). “Rate capability” is the ability of an electrochemical cell to receive or deliver an amount of energy within a specified time period. Alternately, “rate capability” is the maximum continuous or pulsed energy a battery can provide per unit of time.
“C-rate” is defined herein as a measure of the rate at which a battery is discharged relative to its maximum nominal capacity. For example, a 1C current rate means that the discharge current will discharge the entire battery in 1 hour; a C/2 current rate will completely discharge the cell in 2 hours and a 2C rate in 0.5 hours. “Power” is defined as the time rate of energy transfer, measured in Watts (W). Power is the product of the voltage (V) across a battery or cell and the current (A) through the battery or cell. “C-Rate” is mathematically defined as C-Rate (inverse hours)=current (A)/capacity (Ah) or C-Rate (inverse hours)=1/discharge time (h). Power is defined by the mathematical equations: power (W)=energy (Wh)/time (h) or power (W)=current (A)×voltage (V). Coulombic efficiency is the efficiency at which charge is transferred within an electrochemical cell. Coulombic efficiency is the ratio of the output of charge by a battery to the input of charge.
Considerable development in both commercial and academic settings has been focused on designing systems that minimize or accommodate total volume swelling of alloy particles and associated electrochemical losses. This has typically been approached on two fronts. At the particle level, designing particle architectures that confine swelling to small domains to prevent particle fracture and electrical disconnection, and at the electrode level, designing a polymer matrix and conductive network that can accommodate the volume swell of the lithium storing materials while retaining mechanical and electronic integrity during repeated charge/discharge operation of the Li-ion cell.
A popular technique to stabilize the cycle life of alloy active anode materials such as silicon is through the mixture, encapsulation or other incorporation by various carbon materials to provide an electronically conducting surface and facilitate general electronic conduction throughout the electrode particle network. These include CVD amorphous carbon coatings, graphene wrappings, and physical mixing with graphite, conductive carbons, and carbon nanoplatelets. However, active materials may still swell due to their rigid nature and lack of long range order, and particles may still become isolated resulting in storage capacity loss and trapped lithium.
Various embodiments of the present disclosure provide an anode material for Li-ion batteries that includes active material particles comprising an alkali metal or an alkali earth metal silicate and single-wall carbon nanotubes (SWCNTs) that provide long range conductivity in the active material particle network, enabling increased cycle life stability despite the inherent swelling associated with the lithium storing metal alloy particles.
SiO Materials
Silicon and silicon alloys may significantly increase cell capacity when incorporated within an electrode of an electrochemical cell. Silicon and silicon alloys are often incorporated within an electrode comprising graphite, graphene, or other carbon-based active materials. Examples of electrodes comprising carbon-based materials and silicon are provided in U.S. Pat. Nos. 8,551,650, 8,778,538, and 9,728,773 to Kung et al., and U.S. Pat. Nos. 10,135,059 and 10,135,063 to Huang et al., all the contents of which are fully incorporated herein by reference.
Herein, “SiO” materials may refer to silicon and oxygen-containing materials. SiO materials are of interest for use in anode electrodes of lithium-ion batteries, due to having high theoretical energy and power densities. However, the utilization of current commercial SiO materials has been limited due to SiO materials having a low 1st cycle efficiency and a high irreversibility. This low 1st cycle efficiency is due to high irreversible Li+ reaction with the SiO matrix.
In order to decrease the irreversible Li+ reaction with silicon oxide, various embodiments include metalized silicon oxide materials (M-SiO). Herein, M-SiO materials may refer to active materials that are directly reacted with metal-containing precursors, such as alkali and/or alkali earth containing precursors, such as for example, lithium-containing precursors and/or magnesium-containing precursors, to form metalized silicon and oxygen-containing phases, prior to being utilized in a battery as an active material and/or undergoing charge and discharge reactions. In one embodiment, all or some of the metalizing metal may remain in the active material and does not intercalate (i.e., does not insert) or deintercalate during battery charging and discharging. However, in some embodiments, M-SiO materials may include SiO materials that are metalized to include other suitable alkali and/or alkali earth metals, such as sodium, potassium, calcium, or the like. For example, in some embodiments, M-SiO materials may be metalized to include magnesium, lithium, sodium, potassium, calcium, or any combinations thereof. Preferably, M-SiO materials may refer to lithium-metalized SiO (LM-SiO) materials and/or Mg-metalized SiO (MM-SiO) materials.
Electrode materials including M-SiO active materials have been found to provide increased 1st cycle efficiency (FCE), as compared to non-metalized SiO materials. Unfortunately, M-SiO materials have been found to suffer from severe electrical disconnection and rapid capacity loss, often leading to more than 90% capacity fade within 20 cycles. Coating M-SiO materials with carbon and/or other materials, and/or blending M-SiO materials with graphite have been found to slightly reduce the electrical disconnection and capacity loss of active materials, delaying the over 50% capacity fade to ˜50 cycles, which is still highly unsatisfactory cycling stability for commercial applications. Overall, current M-SiO materials do not exhibit electrical stability sufficient for commercialization.
In preferred embodiments, the core particle 102 comprises an M-SiO material. As such, the active material particles 100 are described below with respect to core particles 102 that comprise an M-SiO material.
The active material particles 100 and/or core particles 102 may have an average particle size that ranges from about 1 μm to about 20 μm, such as from about 2 μm to about 15 μm, from about 3 μm to about 10 μm, from about 3 μm to about 7 μm, or about 5 μm. The core particles 102 may include M-SiO materials that include metalized silicon species and silicon (e.g., crystalline and/or amorphous silicon). The metalized silicon species may include metalized silicides and metalized silicates. In some embodiments, the M-SiO materials may also include silicon oxide (SiOx, wherein x ranges from 0.8 to 1.2, such as from 0.9 to 1.1). In various embodiments, the M-SiO materials may include lithiated silicon species. Herein, “lithiated silicon species” may include lithium silicides (LixSi, 0<x<4.4), and/or one or more lithium silicates (Li2Si2O5, Li2SiO3, and/or Li4SiO4, etc.).
Referring to
Referring to
Referring to
In various embodiments, the core particles 102 may represent from about 80 wt % to about 99.5 wt %, such as from about 90 wt % to about 99 wt %, including about 90 wt % to 95 wt % of the total weight of the active material particles 100. In some embodiments the M-SiO material may include from about 40 at % to about 5 at %, such as from 20 at % to about 10 at %, or about 15 at % of lithiated silicon species. In some embodiments the M-SiO material of the core particles 102A may include from about 60 at % to about 95 at %, such as from about 80 at % to about 90 at %, or about 85 at % silicon and SiOx. The M-SiO material of the core particles 102 may have a silicon to oxygen atomic weight ratio ranging from about 1.25:1 to about 1:1.25, such as from about 1.1:1 to about 1:1.1, or of about 1:1. In some embodiments, the M-SiO material of the core particles 102 may comprise approximately equal atomic amounts of crystalline silicon and SiOx.
During an initial charging reaction and/or subsequent charging reactions, the composition of the M-SiO material of the core particles 102A may change due to lithiation and/or other reactions. For example, Si and SiOx may be lithiated to form LixSi domains. In addition, some SiOx may form inactive species, such as lithium silicates and Li2O.
In various embodiments, the coating 110 may be in the form of a shell that completely encapsulates the core particles 102, as shown in
Turbostratic Carbon
In some embodiments, the coating 110 may include a flexible, highly-conductive graphene material, such as graphene, graphene oxide, partially reduced graphene oxide, or combinations thereof. For example, the coating 110 may preferably comprise a flexible, highly conductive graphene material having low-defect turbostratic characteristics, which may be referred to as turbostratic carbon. The low-defect turbostratic carbon may be in the form of platelets comprising from one to about 10 layers of a graphene material, such as graphene, graphene oxide, or reduced graphene oxide. In some embodiments, the low-defect turbostratic carbon may comprise at least 90 wt %, such as from about 90 wt % to about 100 wt % graphene. The graphene material may further comprise a powder, particles, mono-layer sheets, multi-layer sheets, flakes, platelets, ribbons, quantum dots, tubes, fullerenes (hollow graphenic spheres) or combinations thereof.
The turbostratic carbon may be in the form of sheets or platelets that partially overlap to simulate larger size single sheet structures. In some embodiments the platelets have more than one or more layers of a graphene-based material. In some embodiments, the platelets may have sheet size may be on average ≤15 μm. In some embodiments, the platelets may have sheet size may be on average ≤1 μm. In some embodiments, the turbostratic carbon-based material platelets may have low thickness. In some embodiments, a low thickness of the turbostratic carbon-based material platelets may be on average ≤1 μm. In some embodiments, a low thickness of the turbostratic carbon-based material platelets may be on average ≤100 nm.
In various embodiments, the coating 110 may be in the form of a shell that completely encapsulates the particle 100, as shown in
The coating 110 may ensure that the core particles 102 are homogenously/uniformly cycled (movement of electrons and Li-ions in and out of the structure) in all three dimensions, due to its conductive nature, thereby minimizing the stresses exerted on and by the core particle and minimizing particle fracture. Additionally, in the event that a particle 100 does fracture, the flexible coating 110 may operate to electrically connect the fractured silicon oxide material and maintain the overall integrity of the particle 100, thereby leading to significantly improved electrochemical performance.
Reduced graphene oxide (rGO) is a carbon variant that is often referred to as graphene in the industry, however, is unique in final structure and manufacturing process. Graphene oxide is typically manufactured first using a modified Hummers method wherein a graphite material is oxidized and exfoliated into single layers or platelets comprising a few layers of carbon that may comprise various functional groups, including, but not limited to, hydroxyls, epoxides, carbonyls, and carboxyls. These functional groups are then removed through chemical or thermal treatments that convert the insulating graphene oxide into conductive reduced graphene oxide. The reduced graphene oxide is similar to graphene in that it consists of single layers of carbon atom lattices, but differs in that it has mixed sp2 and sp3 hybridization, residual functional groups and often increased defect density resultant from the manufacturing and reduction processes. Reduced graphene oxide is shown in the first bar of
Amorphous carbon is often used as an additive or surface coating for both electrochemical cell anode and cathode material mixtures to enhance electrode conductivity. Typically, amorphous carbons are produced using a chemical vapor deposition (CVD) process wherein a hydrocarbon feedstock gas is flowed into a sealed vessel and carbonized at elevated temperatures onto the surface of a desired powder material. This thermal decomposition process can provide thin amorphous carbon coatings, on the order of a few nanometers thick, which lack any sp2 hybridization as found in crystalline graphene-based materials. Amorphous carbon is shown in the third bar of
Low-defect turbostratic carbon, also referred to as graphene, comprises unique characteristics resultant from its manufacturing processing. One common method of producing this material is through a plasma based CVD process wherein a hydrocarbon feedstock gas is fed through an inert gas plasma in the presence of a catalyst that can nucleate graphene-like carbon structures. By controlling the production parameters, carbon materials having a few layers and absent any AB stacking order between lattices can be produced. These carbon materials are typically highly ordered sp2 carbon lattices with low-defect density.
The low-defect turbostratic carbon of the present disclosure is shown in the center second bar of
Carbon materials with high AB stacking order will still exhibit 2D peaks, however, these 2D peaks exhibit a doublet that breaks the symmetry of the peak. This break in symmetry is exhibited in both AB stacked graphene of a few layers or graphite of many layers. Thus, the 2D peak, which is a very strong indicator of the presence of stacking order regardless of the number of graphene layers present in the material, is of significance when selecting a graphene or graphene-based additive. It is the rotational disorder of the stacking in the low-defect turbostratic carbon of the present disclosure that distinguishes itself from all the other graphene or graphene-based additives used to date, as the rotational disorder of the low-defect turbostratic carbon stacking of the present application is what offers flexibility to the carbon-based particles of the present application, which therein enables the ability of these carbon-based particles to provide and preserve contact with the active core particle of the composite particles comprising the electrode of the electrochemical cell. The result is an electrochemical cell having increased cycle life, better cycle life stability, enhanced energy density, and superior high rate performance.
Raman analysis sample preparation involved taking small aliquots of powders such as active material powders, composite material powders, carbon material powder, and placing these powders individually into a clean glass vial. The sample powder is rinsed with methanol. The powder/methanol solutions are then vortexed briefly and sonicated for approximately 10 minutes. The suspension is then transferred to a microscope slide with a micropipette. The slides are then allowed to air dry completely before conducting the analysis.
The Raman spectroscopy analysis of the present application is conducted using confocal Raman spectroscopy on a Bruker Senterra Raman System under the following test conditions: 532 nm laser, 0.02 mW, 50× objective lens, 90 second integration time, 3 co-additions (3 Raman spectroscopy sample runs) using a 50×1000 μm aperture and a 9-18 cm−1 resolution. As a point of reference, the D band is not active in the Raman scattering of perfect crystals. The D band becomes Raman active in defective graphitic materials due to defect-induced double resonance Raman scattering processes involving the π-π electron transitions. The intensity of the D band relative to the G band increases with the amount of disorder. The intensity ID/IG ratio can thereby be used to characterize a graphene material.
The D and G bands of the amorphous carbon shown in
Table 1 below provides the detail for the Raman spectra of
Careful inspection of these spectra show that when disorder increases, the D band broadens and the relative intensity of the band changes. For the amorphous carbon coated sample, the high intensity (6194.8) and broad D peak indicates a high amount of defects. The G peak being lower in intensity (4908.2) then the D peak (6194.8) indicates a lack of crystallinity. The D peak intensity (9115.5) and G peak intensity (10033.3) of the rGO encapsulated sample are fairly alike. Noticeable, however, is that the D peak intensity (9115.5) of the rGO sample is substantially higher than the D peak intensity (2915.3) of the turbostratic carbon sample indicating that the rGO sample has substantially higher defect density than does the turbostratic carbon sample. Also noticeable is that the G band for the amorphous carbon and the rGO samples are shifted to the right of wavelength 1584 cm−1 to wavelength 1589.4 cm−1 and 1597.82 cm−1 respectively, whereas the G band for the turbostratic carbon sample lies slightly to the left of wavelength of 1584 cm−1 at 1581.32 cm−1. Of significance is that, unlike the amorphous carbon and the rGO samples, the turbostratic carbon (in this case, graphene sample) does not display much, if any, shift in position, reflecting low-defects therein, thus, the turbostratic carbon sample most nearly resembles an almost ‘perfect’ turbostratic carbon material.
Electrode Materials
Various embodiments of the present disclosure provide electrode materials for Li-ion batteries, and in particular, anode electrode compositions. As shown in
As shown in
The electrode materials may include at least 80 wt % of the active material, such as at least 90 wt %, at least 94 wt %, such as 90 to 96.5 wt % of the active material. The active material may include a mixture of active material particles 100 and optionally graphite particles 130. For example, the active material may include from about 5 wt % to about 50 wt %, such as from about 10 wt % to about 30 wt %, from about 15 wt % to about 25 wt % M-SiO, and from about 95 wt % to about 50 wt %, such as from about 90 wt % to about 70 wt %, from about 85 wt % to about 75 wt % graphite. In some preferred embodiments, the active material may include less than 50 wt % M-SiO and more than 50 wt % graphite. Thus, the active material may include more graphite particles 130 than active material particles 100 by weight.
The active material particles 100 may include silicon and metal silicate phases and optionally silicon oxide phases described above. The active material particles 100 may include the optional carbon coating 110, or the carbon coating 110 may be omitted.
The active material particles 100 may have an average particle size that ranges from about 1 μm to about 20 μm, such as from about 1 μm to about 10 μm, from about 3 μm to about 7 μm, or about 5 μm. The active material particles 100 may have a surface area that ranges from about 0.5 m2/g to about 30 m2/g, such as from about 1 m2/g to about 20 m2/g, including from about 5 m2/g to about 15 m2/g.
The graphite may include graphite particles 130 of synthetic or natural origin. The graphite may have an average particle size ranging from about 2 μm to about 30 μm, such as from about 10 μm to about 20 μm, including from about 12 μm to about 18 μm. In one embodiment, the average particle size of the graphite particles 130 may be larger than the average particle size of the silicon oxide particles 100. The graphite particles 130 may have a surface area that ranges from about 0.5 m2/g to about 2.5 m2/g, such as from about 1 m2/g to about 2 m2/g. The graphite particles 130 may be larger than the silicon oxide particles 110.
The electrode material may include any suitable electrode material binder (not shown in
In various embodiments, the electrode material may include from about 1 wt % to about 5 wt %, or from about 2 wt % to about 3 wt % binder.
The SWCNTs 120 may have an average length of greater than about 1 μm. For example, the SWCNTs may have an average length ranging from about 1 μm to about 500 μm, such as from about 1 μm to about 10 μm. The SWCNTs may have an average diameter ranging from about 0.5 nm to about 2.5 nm, such as from about 1 nm to about 2 nm.
The SWCNTs 120 may have an IG/ID ratio or greater than about 5, such as greater than about 6 or greater than about 10, as determined by Raman spectroscopy, with IG being associated with the Raman intensity at wavenumber 1580-1600 cm−1, and ID being associated with the Raman intensity at wavenumber 1330-1360 cm−1, as measured using an incident laser wavelength of 633 nm.
In various embodiments, the electrode material may include from about 0.05 wt % to about 1 wt %, such as from about 0.075 wt % to about 0.9 wt %, from about 0.08 wt % to about 0.25 wt %, or about 0.1 wt % SWCTNs.
The conductive additive (i.e., conductive agent) may include carbon black (e.g., KETJENBLACK or Super-P carbon black), low defect turbostratic carbon, acetylene black, channel black, furnace black, lamp black, thermal black or combinations thereof. The conductive additive may optionally include metal powder, fluorocarbon powder, aluminum powder, nickel powder; nickel flakes, conductive whiskers, zinc oxide whiskers, potassium titanate whiskers, conductive metal oxides, titanium oxide, conductive organic compounds, conductive polyphenylene derivatives, conductive polymers, or combinations thereof.
In various embodiments, the electrode material may include from 0 to about 5 wt %, such as from about 0.1 wt % to about 5 wt %, including from about 0.25 wt % to about 3 wt %, from about 0.5 wt % to about 1.5 wt %, or about 1 wt % conductive additive (i.e., conductive agent) selected from carbon black, an electrically conductive polymer, a metallic powder, or any combination thereof. In some embodiments, the conductive additive may preferably include carbon black.
Anode Formation
According to various embodiments, an anode may be formed using any suitable method known to one or skill in the art. For example, active material particles 100 described above may be mixed with graphite particles 130 to form an active material. In one embodiment, the active material may include less than 50 wt % M-SiO and more than 50 wt % graphite. The active material may be mixed with the SWCNTs, binder and the optional conductive additives to form a solids component. In some embodiments, the active material particles may be coated with turbostratic carbon coating 110 using, for example, a spray drying process, prior to forming the active material. Alternatively, the coating 110 may be omitted.
The solids component may be mixed with a polar solvent such as water or N-Methyl-2-pyrrolidone (NMP), at a solids loading between about 20-60 wt %, to form an electrode slurry. For example, the mixing may include using a planetary mixer and high shear dispersion blade, under vacuum.
The electrode slurry may then be coated onto a metal substrate, such as a copper or stainless steel substrate, at an appropriate mass loading to balance the lithium capacity of the anode with that of a selected cathode. Coating can be conducted using a variety of apparatus such as doctor blades, comma coaters, gravure coaters, and slot die coaters.
After coating, the slurry may be dried to form an anode. For example, the slurry may be dried under forced air, at a temperature ranging from room temperature to about 120° C. The dried slurry may be pressed to reduce the internal porosity, and the electrode may be cut to a desired geometry. Typical anode pressed densities can range from about 1.0 g/cc to about 1.7 g/cc depending on the composition of the electrode and the target application. Cathode pressed densities may range from about 2.7 to about 4.7 g/cc.
In some embodiments, the active material particles may be coated with turbostratic carbon prior to forming the active material. For example, a mixture of active material particles, turbostratic carbon and a solvent may be spray dried, to form a powder, and the powder may then be heat-treated in an inert atmosphere, such as argon gas, to carbonize any remaining surfactant or dispersant. In other embodiments, the active material particles may be coated with turbostratic carbon using a binder and a mechano-fusion process.
Electrochemical Cell Assembly
Construction of an electrochemical cell involves the pairing of a coated anode substrate and a coated cathode substrate that are electronically isolated from each other by a polymer and/or a ceramic electrically insulating separator. The electrode assembly is hermetically sealed in a housing, which may be of various structures, such as but not limited to a coin cell, a pouch cell, or a can cell, and contains a nonaqueous, ionically conductive electrolyte operatively associated with the anode and the cathode. The electrolyte is comprised of an inorganic salt dissolved in a nonaqueous solvent and more preferably an alkali metal salt dissolved in a mixture of low viscosity solvents including organic esters, ethers and dialkyl carbonates and high conductivity solvents including cyclic carbonates, cyclic esters and cyclic amides. A non-limiting example of an electrolyte may include a lithium hexafluorophosphate (LiPF6) or lithium bis(fluorosulfonyl)imide (LiFSi) salt in an organic solvent comprising one of: ethylene carbonate (EC), diethyl carbonate (DEC), dimethyl carbonate (DMC), fluoroethylene carbonate (FEC) or combinations thereof.
Additional solvents useful with the embodiment of the present invention include dialkyl carbonates such as tetrahydrofuran (THF), methyl acetate (MA), diglyme, trigylme, tetragylme, 1,2-dimethoxyethane (DME), 1,2-diethoxyethane (DEE), 1-ethoxy, 2-methoxyethane (EME), ethyl methyl carbonate, methyl propyl carbonate, ethyl propyl carbonate, dipropyl carbonate, and combinations thereof. High permittivity solvents that may also be useful include cyclic carbonates, cyclic esters and cyclic amides such as propylene carbonate (PC), butylene carbonate, acetonitrile, dimethyl sulfoxide, dimethyl formamide, dimethyl acetamide, gamma-valerolactone, gamma-butyrolactone (GBL), N-methyl-2-pyrrolidone (NMP), and combinations thereof.
The electrolyte may also include one or more additives, such as vinylene carbonate (VC), 1,3-propane sulfone (PS), prop-1-ene-1,3-sultone (PES), Flouroethylene carbonate (FEC), and/or propylene carbonate (PC). The electrolyte serves as a medium for migration of lithium ions between the anode and the cathode during electrochemical reactions of the cell, particularly during discharge and re-charge of the cell. The electrochemical cell may also have positive and negative terminal and/or contact structures.
The following examples relate to anode formed using electrode materials of various embodiments of the present disclosure and comparative electrode materials, and are given by way of illustration and not by way of limitation. In the examples, % is percent by weight, g is gram, CE is coulombic efficiency, and mAh/g is capacity.
Exemplary Cells 1-3 (E1, E2, E3)
The active material, SWCNTs, a conductive agent (carbon black), and a binder (CMC/SBR) were mixed to form a solids component. The solids component was mixed with a polar solvent (water or NMP), at a solids loading of between 20 wt % and 60 wt %, in a planetary mixer having a high shear dispersion blade, under vacuum, to form electrode material slurries.
The electrode material slurries were coated on copper current collectors at an appropriate mass loading to balance the lithium capacity of the anode with that of a selected cathode, dried, and pressed to form anodes. The anodes were assembled into half-cells (excess counter electrode material=lithium metal) and electrolyte was provided into each of the half-cells, to form Exemplary Cells 1-3. The anodes of Exemplary Cells 1-3 each included 96 wt % active material, 0.1 wt % SWCNTs, 0.9 wt % carbon black, and 3 wt % CMC/SBR binder.
The anode of Exemplary Cell 1 included 20 wt % LM-SiO, and 76 wt % graphite. The anode of Exemplary Cell 2 included 30 wt % LM-SiO, and 66 wt % graphite. The anode of Exemplary Cell 3 included 30 wt % unmetallized SiO and 66 wt % graphite.
Comparative Cells 1-4 (C1, C2, C3, C4)
Comparative Cells 1-4 were formed in the same manner as Exemplary Cells 1-3. The anode of Comparative Cell 1 included 20 wt % LM-SiO, 76 wt % graphite, 1 wt % carbon black, and did not include CNTs. The anode of Comparative Cell 2 included 30 wt % LM-SiO, 66 wt % graphite, 0.9 wt % carbon black, and 0.1 wt % multi-walled carbon nanotubes (MWCNTs).
The anode of Comparative Cell 3 included 30 wt % LM-SiO, 66 wt % graphite, 1 wt % carbon black, and did not include CNTs. The anode of Comparative Cell 4 included 30 wt % unmetallized SiO, 66 wt % graphite, 1 wt % carbon black, and did not include CNTs.
The following Table 2 shows a half cell cycling protocol applied to the Exemplary and Comparative cells.
Accordingly, mixing with SWCNTs with M-SiO and graphite improves the coulombic efficiency and cycle life of the silicon anode by buffering the volume change of silicon particles during charge/discharge and lowers measurable swelling of the electrode. The addition of SWCNTs to an electrode composition provides relatively long-range conductivity across multiple electrode particles that is flexible enough to sustain a conducting network as particles in the electrode swell. This results in improved capacity retention as the Li-ion cell/electrode is charged and discharged during operation.
The long range conductivity provided by the SWCNTs also unexpectedly enables higher loading of high capacity alloy active materials, preventing capacity fade via electrical disconnection despite more severe overall electrode swelling.
The addition of SWCNTs can also reduce the total carbon black content added for electronic conductivity which consequently reduces the total surface area of the electrode and the amount of polymer binder added for mechanical integrity. Furthermore, carbon black is a nanomaterial that is pore-blocking, occupying interstitial space in between lithium storing active materials. High concentrations of carbon black are undesirable because they prevent proper calendaring (compressing) of the electrodes. Both a reduction in binder content and increase in calendared density provide significant benefits in enabled high energy density Li-ion cells.
Although the foregoing refers to particular preferred embodiments, it will be understood that the invention is not so limited. It will occur to those of ordinary skill in the art that various modifications may be made to the disclosed embodiments and that such modifications are intended to be within the scope of the invention. All of the publications, patent applications and patents cited herein are incorporated herein by reference in their entirety.
Number | Date | Country | |
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63051616 | Jul 2020 | US |