SELF-CROSSLINKING COMPOSITE BINDERS FOR ELECTRODES
20240079593 ยท 2024-03-07
Inventors
Cpc classification
Y02E60/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C08F220/06
CHEMISTRY; METALLURGY
H01M10/0525
ELECTRICITY
H01M4/0471
ELECTRICITY
International classification
H01M4/62
ELECTRICITY
Abstract
Compositions of self-crosslinking composite binders for silicon-based electrodes, associated processes of forming silicon-based electrodes using the composite binders, as well as batteries utilizing the silicon-based electrodes formed using the composite binders are disclosed herein. In certain examples, the composite binder can include a first component configured to provide structural integrity in a silicon-based electrode and a second component configured to form a mesh-like structural network with the first component to provide flexibility of the silicon-based electrode and adhesiveness toward a current collector. The flexible mesh-like structural network is formed via gradient hydrogen bonds between chains of the first component and chains of the second components.
Claims
1. An electrochemical device, comprising: a first electrode; an electrolyte in electrical communication with the first electrode, the electrolyte containing a plurality of metal ions; and a second electrode spaced apart from the first electrode and in electrical communication with the first electrode via the electrolyte, wherein the second electrode contains: multiple micro-sized silicon (Si) particles bound together by a composite binder having a first component and a second component, the first component comprising multiple molecular chains individually with a composition having a formula of: ##STR00003## where each of R.sub.1, R.sub.2, and R.sub.3 is hydrogen or OX, wherein X is hydrogen (H), lithium (Li), sodium (Na), potassium (K), or a functional group having a chemical formula of C.sub.mH.sub.2m+1, where m is an integer in the range from 1 to 10; and the second component comprising multiple molecular chains individually having one or more of glycine, serine, alanine, tyrosine, valine, aspartic acid, glutamic acid, threonine, phenylalanine, isoleucine, leucine, arginine, lysine, methionine, or cysteine; and wherein the molecular chains of the second component crosslinking the molecular chains of the first component to form a mesh-like structural network around at least some of the micro-sized silicon (Si) particles.
2. The electrochemical device of claim 1 wherein the multiple molecular chains of the second component individually include multiple amide and hydroxyl functional groups forming multiple hydrogen bonds with carboxylic functional groups on the multiple molecular chains of the first component.
3. The electrochemical device of claim 1 wherein the multiple molecular chains of the second component individually include multiple amide and hydroxyl functional groups forming multiple hydrogen bonds with carboxylic functional groups on the multiple molecular chains of the first component, and wherein the multiple hydrogen bonds crosslink the molecular chains of the first and second components to form the structural network that is stretchable and contractable during insertion and extraction of the metal ions, respectively.
4. The electrochemical device of claim 1 wherein the multiple molecular chains of the second component individually include multiple amide and hydroxyl functional groups forming multiple hydrogen bonds with carboxylic functional groups on the multiple molecular chains of the first component, and wherein the multiple hydrogen bonds have different bond energy levels.
5. The electrochemical device of claim 1 wherein the multiple molecular chains of the second component individually include multiple amino acids with amide and hydroxyl functional groups forming multiple hydrogen bonds with carboxylic functional groups on the multiple molecular chains of the first component, and wherein the multiple hydrogen bonds have different bond energy levels.
6. The electrochemical device of claim 1 wherein the second component includes one or more of silk fibroin, spider silk protein, wool keratin, soy protein, or silk sericin.
7. The electrochemical device of claim 1 wherein the first component includes poly(acrylic acid) (PAA) and the second component includes one or more of silk fibroin, spider silk protein, wool keratin, soy protein, or silk sericin.
8. The electrochemical device of claim 1 wherein the first component includes poly(acrylic acid) (PAA) and the second component includes silk fibroin, and wherein multiple molecular chains of the silk fibroin individually include multiple amino acids with amide and hydroxyl functional groups forming multiple hydrogen bonds with carboxylic functional groups on multiple molecular chains of the PAA in the first component, and wherein the multiple hydrogen bonds have different bond energy levels.
9. A method of forming an electrode, comprising: mixing a first component and a second component with micro-sized silicon/carbon (Si/C) particles in a solvent to derive a slurry, the first component having multiple molecular chains individually having a formula of: ##STR00004## where each of R.sub.1, R.sub.2, and R.sub.3 is hydrogen or OX, wherein X is hydrogen (H), lithium (Li), sodium (Na), potassium (K), or a functional group having a chemical formula of C.sub.mH.sub.2m+1, where m is an integer in the range from 1 to 10 while the second component comprising multiple molecular chains individually having one or more of glycine, serine, alanine, tyrosine, valine, aspartic acid, glutamic acid, threonine, phenylalanine, isoleucine, leucine, arginine, lysine, methionine, or cysteine; coating a metal foil with the derived slurry; and drying the metal foil coated with the derived slurry under vacuum, thereby crosslinking the molecular chains of the first component with the molecular chains of the second component to form a mesh-like structural network around at least some of the micro-sized silicon (Si) particles.
10. The method of claim 9 wherein: mixing the first component and the second component includes mixing the first component and the second component at a mass ratio between the first component and the second component, thereby forming multiple hydrogen bonds between multiple amide and hydroxyl functional groups of the second component with carboxylic functional groups of the first component, the multiple hydrogen bonds crosslink the molecular chains of the first and second components to form the mesh-like structural network around the multiple silicon/carbon (SiC) particles; and wherein the method further includes adjusting the mass ratio between the first and second components based on a target level of rigidity of the mesh-like structural network.
11. The method of claim 9 wherein: mixing the first component and the second component includes mixing the first component containing poly(acrylic acid) (PAA) and the second component containing silk fibroin at a mass ratio between the first component and the second component, thereby forming multiple hydrogen bonds between multiple amide and hydroxyl functional groups of the silk fibroin with carboxylic functional groups of the PAA, the multiple hydrogen bonds crosslink the molecular chains of the PAA and the silk fibroin to form mesh-like structural network around the multiple silicon/carbon (SiC) particles; and wherein the method further includes adjusting the mass ratio between the PAA and the silk fibroin based on a target level of rigidity of the mesh-like structural network.
12. The method of claim 9 wherein drying the metal foil coated with the derived slurry includes drying the metal foil coated with the derived slurry at a drying temperature, and wherein the method further includes adjusting the drying temperature to achieve a target level of adhesion between the Si/C particles to the metal foil.
13. The method of claim 9 wherein mixing the first component and the second component includes mixing the first component and the second component at a mass ratio between the first component and the second component, and wherein the method further includes adjusting the mass ratio between the first component and the second component based on a target level of adhesion between the Si/C particles to the metal foil.
14. The method of claim 9 wherein mixing the first component and the second component includes mixing the first component and the second component at a mass ratio between the first component and the second component, and wherein the method further includes increasing the mass ratio between the first component and the second component to increase adhesion between the Si/C particles to the metal foil.
15. The method of claim 9 wherein mixing the first component and the second component includes mixing the first component and the second component at a mass ratio between the first component and the second component, and wherein the method further includes decreasing the mass ratio between the first component and the second component to decrease adhesion between the Si/C particles to the metal foil.
16. A composite binder for binding multiple silicon particles together to form one or more electrodes, the composite binder comprising: a first component comprising a composition having a formula of: ##STR00005## where each of R.sub.1, R.sub.2, and R.sub.3 is hydrogen or OX, wherein X is hydrogen (H), lithium (Li), sodium (Na), potassium (K), or a functional group having a chemical formula of C.sub.mH.sub.2m+1, where m is an integer in the range from 1 to 10; a second component having one or more of glycine, serine, alanine, tyrosine, valine, aspartic acid, glutamic acid, threonine, phenylalanine, isoleucine, leucine, arginine, lysine, methionine, or cysteine; and a solvent containing both the first and second components.
17. The composite binder of claim 16 wherein the first component comprises a molecular weight in a range from about 2,000 to about 300,000.
18. The composite binder of claim 16 wherein a concentration of the first or second component in the solvent is about 5 wt % to about 40 wt %.
19. The composite binder of claim 16 wherein a mass ratio of the first component to the second component is in a range from 1 to 0.01.
20. The composite binder of claim 16 wherein a weight percentage of the first or second component is from about 1 wt % to about 20 wt %.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION
[0027] Various embodiments of battery systems, devices, and associated methods of making are described herein. Even though the technology is described below using a lithium-ion battery as an example, in other embodiments, the technology may be applicable in other suitable types of batteries (e.g., batteries containing sodium, potassium, calcium, magnesium, cadmium, selenium, or copper ions), a chemical sensor, a gas separation membrane, an organic thin film transistor, an electromechanical actuator, a fuel cell, and/or other suitable electronic components. In addition, certain embodiments of the self-crosslinking composite binders described herein may also be used to bind carbon, metals, or other suitable types of particles for any suitable applications. In the following description, specific details of examples are included to provide a thorough understanding of certain embodiments of the disclosed technology. A person skilled in the relevant art will also understand that the disclosed technology may have additional embodiments or may be practiced without several of the details of the embodiments described below with reference to
[0028] Lithium-ion batteries typically use carbon-based materials, such as graphite, as anodes. However, carbon-based materials tend to limit charging capacities of lithium-ion batteries. For example, lithiation of a carbon-based anode can produce a charging capacity of about 372 mAh g.sup.?1 while lithiation of silicon (Si) can produce a charging capacity of about 4,200 mAh g.sup.?1. However, lithiation in silicon can involve about 300% volume change. Thus, after a few charge-discharge cycles, a bulk silicon-based anode would be pulverized. Silicon anodes can also form unstable solid-electrolyte interphase layers with electrolytes in lithium-ion batteries. As such, the poor mechanical stability and chemical passivation properties of silicon can render silicon electrodes unsuitable for practical battery systems.
[0029] Several embodiments of the disclosed technology are directed to compositions of self-crosslinking composite binders for silicon-based electrodes, associated processes of forming silicon-based electrodes using the composite binders, as well as batteries utilizing the silicon-based electrodes formed using the composite binders. In certain embodiments, the composite binder can include a first component configured to provide structural integrity to a silicon-based electrode and a second component configured to form a flexible structural network with the first component to provide flexibility of the silicon-based electrode and adhesiveness toward a current collector. In one example, the first component can include PAA while the second component can include SF. It is believed that the flexible structural network can lead to controllable glass transition temperatures, high adhesive strengths, and good electrochemical stability of micro-sized silicon anodes formed using the composite binder, as discussed in more detail below.
[0030]
[0031] The cathode 106 can be constructed from a layered oxide (e.g., lithium cobalt oxide (LiCoO.sub.2)), a polyanion (e.g., lithium iron phosphate (LiFePO.sub.4)), or a spinel (e.g., lithium manganese oxide (LiMn.sub.2O.sub.4)). Other suitable materials for the cathode 106 can include lithium nickel oxide (LiNiO.sub.2), lithium iron phosphate fluoride (Li.sub.2FePO.sub.4F), lithium cobalt nickel manganese oxide (LiCo.sub.1/3Ni.sub.1/3Mn.sub.1/3O.sub.2), Li(Li.sub.aNi.sub.xMn.sub.yCo.sub.z)O.sub.2, and/or other suitable cathode materials (e.g., sulfur, selenium, selenium sulfide, oxygen, or carbon dioxide). Additional examples of metal compositions suitable for the cathode 106 can also include: [0032] LiNiCoAlO.sub.2 having 80% Nickel, 15% Cobalt, and 5% Aluminum [0033] LiCoO.sub.2 having 100% Cobalt [0034] LiMn.sub.2O.sub.4 having 100% Manganese [0035] LiNiMnCoO.sub.2 having 33.3% Nickel, 33.3% Manganese, and 33.3% Cobalt [0036] LiFePO.sub.4 having 100% Iron
[0037] In certain embodiments, the electrolyte 108 can include a non-aqueous solution of organic carbonates such as ethylene carbonate or diethyl carbonate containing complexes of lithium ions. The electrolyte 108 can contain non-coordinating anion salts such as LiPF.sub.6, LiAsF.sub.6, LiClO.sub.4, LiBF.sub.4, and lithium triflate. In other embodiments, the electrolyte 108 may also include an aqueous and/or a partially aqueous solution of lithium salts and/or other suitable compositions (e.g., quasi-solid or solid electrolytes).
[0038] As shown in
[0039] Such lithiation/delithiation at the anode 104 can involve about 300% volume changes when the anode 104 contains bulk or micro-sized silicon. In accordance with several embodiments of the disclosed technology, the anode 104 can be constructed, at least partially, from a self-crosslinking composite binder 120 (shown in
[0040] In certain embodiments, the first component of the composite binder 120 comprises a polymer having the following formula:
##STR00002##
where each of R1, R2, and R3 includes hydrogen or OX, wherein X is H, Li, Na, K, or a functional group having a formula of C.sub.mH.sub.2m+1, m is an integer in the range from 1 to 10. In a particular example, the first composition can include PAA. In other embodiments, the first component can also include other materials to provide suitable target properties to the anode 104.
[0041] In some embodiments, the second component can include one or more amino acids with amide and hydroxyl groups to form self-crosslinking interactions with functional groups (e.g., carboxylic groups) of the first component via inter- and/or intra-chain gradient hydrogen bonds. In one example, the second component can include silk fibroin (SF). In other examples, the second component can also include one or more of spider silk protein, wool keratin, soy protein, or silk sericin. In further embodiments, the composite binder 120 can also include other suitable compositions in lieu of or in addition to the first or second component.
[0042] In certain embodiments, the first component can have a molecular weight in a range from about 2,000 up to about 300,000. Both the first and second components of the composite binder 120 can have a concentration range from about 5 wt % to about 40 wt % in the solvent and a weight percentage in a range from about 1 wt % to about 20 wt %. The mass ratio of the first component to the second component can be in the range from 1 to 0.01. In other embodiments, the molecular weight of the first or second component and the relative concentration or mass ratio of the first and second component can have other suitable values based on identity of the first or second component as well as particular application of the composite binder 120.
[0043] In the following description, an example composite binder 120 using PAA as the first component and using SF as the second component is used to illustrate aspects of the disclosed technology. As discussed in more detail herein, the PAA can form a network that provides structural integrity to the anode 104 while the SF can crosslink with one or more molecular chains of the PAA via gradient hydrogen bonds to form a flexible structural network 130 (shown in
[0044] As such, several embodiments of the lithium-ion battery 100 can have a higher charging capacity than conventional batteries using a carbon-based material for the anode 104. For example, as discussed above, a conventional lithium-ion battery with a carbon-based anode can have a charging capacity of about 372 mAh g.sup.?1 while several embodiments of the lithium-ion battery 100 can have a charging capacity of about 2,000 mAh g.sup.?1. As a result, the charging capacity of the lithium-ion battery 100 may be improved when compared to conventional lithium-ion batteries.
[0045] Several embodiments of the anode 104 of the lithium-ion battery 100 can also have improved charging/discharging cyclability. It is believed that the anode 104 can accommodate the large volume changes associated with lithiation/delithiation because the structural network 130 formed by the first and second components of the composite binder 120 is flexible and thus can contract and expand during lithiation/delithiation. For example, the structural network 130 may contract during lithium insertion and expand during lithium extraction without causing pulverization and/or other structural damage to the anode 104 as a whole. As such, the cyclability of the lithium-ion battery 100 can be improved to render the anode 104 stable for practical battery systems.
[0046]
[0047]
[0048] As shown in
[0049]
Experiments
[0050] Certain experiments were conducted to study the effects of using a composite binder described herein on electromechanical performance of anodes in a lithium-ion battery. In the experiments, PAA/SF composite binders with different concentration or mass ratios were used for illustration purposes. The results of the experiments are presented below in conjunction with
[0051] PAA-only binder film was prepared by contacting a PAA aqueous solution (25 wt %) on the surface of a copper foil, and then dried at 155? C. for 2 hours under vacuum. The dried binder film was then peeled off the copper foil. For PAA/SF composite films, PAA/SF solutions were first prepared by mixing various mass ratios of PAA to SF (5 wt %, average Mw=100 kDa) ranging from 4:1 to 1:2 and then following the same procedures as synthesis of the PAA film. The PAA, PAA/SF, and SF binder films were immersed in electrolyte for 24 hours to study the solubility of the various binders.
Synthesis of Super C45 Electrode
[0052] Conductive carbon (Super C45) nanoparticles were mixed with a binder in a mass ratio of 1:1 with DI water. The obtained slurry was then coated on a copper foil and dried at 155? C. for 2 hours under vacuum. The mass loading of Super C45 electrode was ?0.5 mg cm.sup.?2.
Synthesis of Silicon-Based Electrode
[0053] Micro-sized Si/C particles were synthesized. Si/C particles were mixed with Super C45 and binder in a mass ratio of 6:2:2. DI water was used to adjust the viscosity of the slurry. The obtained Si/C electrode slurry was then coated on a copper foil before drying at 155? C. for 2 hours under vacuum. To study the effect of drying temperature on electrochemical performance of the silicon-based electrode, PAA/SF-based Si/C electrode was prepared using the same method but dried at 115? C. The prepared Si/C electrode was punched into round disks with a diameter of 12 mm. PAA/carboxymethylcellulose sodium salt (CMC) in a mass ratio of 1:1 was used as a reference binder for the Si/C electrode. The mass loading of Si/C in all electrodes was ?1.0?0.2 mg cm.sup.?2. PAA/SF-based Si/C electrode with a high mass ratio of 90:1:9 (active material:carbon additive:binder) was prepared using the same procedure. The mass loading of this PAA/SF-based Si/C electrode was ?1.5 mg cm.sup.?2.
Materials Characterization
[0054] Fourier-transform infrared (FTIR) spectroscopy was performed by a FT-IR spectrometer in the attenuated total reflectance (ATR) mode. The scan range was 600-4,000 cm.sup.?1 with a resolution of 4 cm.sup.?1. The spectra of each sample were collected after 64 scans. The binder films were prepared by dropping binder solutions on a glass slide and dried 155? C. for 2 hours under vacuum. An empty glass slide was used as background during FTIR measurements. To investigate the interaction between Si/C and the binder, Si/C particles were mixed with PAA or SF and then dried at 155? C. under vacuum for 2 hours before FTIR test.
[0055] Differential scanning calorimetry (DSC) analysis was performed under nitrogen atmosphere. The binder film samples were heated from 20? C. to 250? C. and then cooled down to ?90? C. for three cycles at a heating/cooling rate of 10? C. min.sup.?1. The second heating cycle was used to plot DSC traces. X-ray diffraction (XRD) measurement of Si/C particles was performed. Thermogravimetric analysis (TGA) was conducted to determine the content of carbon in the Si/C particles. The temperature range was from room temperature to 750? C. with a heating rate of 10? C. min.sup.?1. FTIR analysis of Si/C particles was performed. Scanning electron microscopy (SEM) images were obtained. 180-degree peeling test of electrodes was performed on a universal testing machine equipped with a 100-Newton load cell. The electrode materials were peeled off from a copper foil with a displacement rate of 60 mm min.sup.?1. Each sample was repeated three times.
X-Ray Photoelectron Spectroscopy (XPS) Analysis
[0056] The cycled Si/C electrodes were rinsed with dimethyl carbonate and dried overnight before XPS measurements. X-ray spot size for the acquisitions was on the order of 700?300 ?m. Pressure in the analytical chamber during spectral acquisition was less than 1?10.sup.?8 Torr. Pass energy for survey spectra (composition) was 80 eV. Pass energy for the high-resolution spectra was 20 eV. The take-off angle (the angle between the sample normal and the input axis of the energy analyzer) was 0? (0-degree take-off angle, ?100 ? sampling depth). For the high-resolution spectra, a Shirley background was used, and all binding energies were referenced to the C Is CC bonds at 284.8 eV.
Battery Assembly
[0057] For half-cell configuration, coin cells were assembled with silicon/carbon (or Super C45) as a working electrode and lithium foil as the counter and reference electrode. A polypropylene membrane was used as a separator. For the full cell configuration, PAA/SF-based Si/C anode (?16 mm, mass loading: 0.27 mg cm.sup.?2) was paired with LiFePO.sub.4 cathode (LFP, ?12 mm, mass loading: 11.16 mg cm.sup.?2, MTI Corp.). The capacity ratio of Si/C anode to LFP cathode was ?1.05. The electrolyte was composed of 1.3 M lithium hexafluorophosphate (LiPF.sub.6) in ethylene carbonate (EC)/diethylene carbonate (DEC) (3:7 by volume) with 10 wt % fluoroethylene carbonate (FEC). The amount of electrolyte used in each cell was 100 ?L.
Electrochemical Measurements
[0058] A galvanostatic lithiation and delithiation test was conducted in a voltage window of 0.01-1.2 V vs. Li/Li.sup.+ at 30? C. The initial cycle was tested at a current density of 0.1 A g.sup.?1, and the following cycles were tested at various C-rates (1.0 C was calculated based on the initial lithiation capacity of each coin cell). Cyclic voltammetry (CV) measurements were performed from open circuit voltage to 0.01 V and from 0.01 V to 1.2 V vs. Li/Li.sup.+ at a scan rate of 0.1 mV s.sup.?1 at 30? C. Electrochemical impedance spectroscopy (EIS) measurements were performed in a frequency range from 5 MHz to 10 mHz with an AC oscillation amplitude of 10 mV. The PAA/SF-based Si/C?LFP full cell was tested in a voltage window of 2.0-4.0 V at 0.1 C (1.0 C=170 mA g.sup.?1). All cells were aged at 50? C. for 2 hours and 30? C. for 22 hours before testing.
DFT Calculations
[0059] The binding energy between PAA and amino acids of SF was calculated by density-functional theory (DFT). All molecular structures (PAA, Gly, Ser, and Ala) were saturated by methyl groups at two ends. The geometries of molecular structures were first optimized at the B3LYP/6-31+G(d,p) level of theory, followed by energy calculation at the B3LYP/6-311++G(2df,2p) level of theory, both with DFT-D3(BJ) dispersion correction. The binding energy (?E.sub.b) of PAA towards amino acid was calculated using the following equation: ?E.sub.b=E.sub.A+B?(E.sub.A+E.sub.B), where E.sub.A+B, E.sub.A, and E.sub.B represent total energy of A-B complex, A component, B component, respectively. A and B can be PAA and amino acids of SF.
Chemical Interactions Between PAA and SF
[0060] As shown in
[0061] To investigate chemical interactions inside a PAA/SF composite binder, the binding energy of PAA towards SF was calculated using DFT. The binding energy of PAA towards PAA itself and towards amino acids of SF follows the decreasing order (kcal mol.sup.?1): PAA-PAA (?19.63)>PAA-Ser (?19.04)>PAA-Gly (?16.46)>PAA-Ala (?14.28). PAA monomer shows a strong binding energy with another PAA monomer via hydrogen bonding between C?O and OH, leading to high rigidness of a binder containing pure PAA. However, PAA shows gradient binding energy towards amino acids of SF ranging from ?14.28 to ?19.04 kcal mol.sup.?1, which is believed to be attributed to the hydrogen bonding between carboxyl (COOH) and different amide (NH) groups. Moreover, this gradient binding energies of PAA/SF are sufficiently strong and thus can effectively maintain good structural integrity of micro-sized silicon electrodes during cycling. In addition, the solubility test shows that PAA, PAA/SF, and SF binders are insoluble and exhibit good stability towards carbonate-based electrolyte, which is also beneficial in maintaining good structural integrity of silicon-based electrode during cycling.
[0062] To further study the chemical interactions between PAA and SF, PAA/SF composite binders were prepared with various mass ratios. Table 1 below shows specific example compositions of the composite binder 120 utilizing PAA and SF. For example, PAA/SF (1/1) was composed of 50 wt % of PAA and 50 wt % of SF.
TABLE-US-00001 TABLE 1 Example PAA/wt % SF/wt % Denoted as Example 1 100 0 PAA Example 2 80 20 PAA/SF (4/1) Example 3 67 33 PAA/SF (2/1) Example 4 50 50 PAA/SF (1/1) Example 5 33 67 PAA/SF (1/2) Example 6 0 100 SF
[0063] In this description, PAA/SF refers to the PAA/SF composite binder in a mass ratio of 2:1 unless otherwise stated. As shown in
[0064] FTIR spectroscopy measurement of sample PAA/SF composite binders were performed. As shown in
[0065] Additionally, the mass ratio of PAA to SF can also affect thermal properties of the PAA/SF composite binders. As shown in
Adhesion Force and Electrochemical Stability of PAA/SF Composite Binder
[0066] To investigate the adhesion force of various binders, micro-sized silicon/carbon (Si/C) electrodes with PAA and PAA/SF binders were prepared. Si/C microparticles were synthesized by the CO.sub.2-thermic oxidation process. The Si/C particles show a particle size of 10-15 ?m and 2.8 wt % of a carbon coating layer. FTIR analysis shows that Si/C particles contain hydroxyl groups on their surface, which can form hydrogen bonding with the carboxyl groups of PAA and amide groups of SF, as illustrated in
[0067] The adhesion force of PAA/SF composite binder was measured by 180-degree peeling test, as shown in
[0068] Besides the mass ratio of PAA to SF, the drying temperature of electrodes also affects the adhesion force and thus electrochemical performance of PAA/SF-based Si/C electrode. Therefore, in certain embodiments, the drying temperature can be adjusted to achieve a target adhesive level of the Si/C electrode to the copper foil (or other suitable metal structure). For the experiments discussed herein, all Si/C electrodes were dried at 155? C. unless otherwise stated in the following section.
[0069] To evaluate the electrochemical stability of PAA/SF composite binders, cyclic voltammetry (CV) measurements of conductive carbon (i.e., Super C45) electrodes were performed with PAA and PAA/SF at a scan rate of 0.1 mV s.sup.?1. PAA-based Super C45 electrode showed gradually increased current density of redox peaks during ten cycles in the voltage range of 0.01-1.2 V vs. Li/Li.sup.+, whereas the PAA/SF-based one showed no redox peaks for ten cycles. Additionally, PAA/SF-based Super C45 electrode showed much lower specific capacity (<100 mAh g.sup.?1) than that of PAA-based one (250 mAh g.sup.?1) at the current density of 40 mA g.sup.?1. The results showed that PAA/SF composite binders have good electrochemical stability.
Structural Characterization of Si/C Electrodes with PAA and PAA/SF Binder
[0070] Binders can provide structural integrity of micro-sized silicon electrodes during repeated (de)lithiation cycling. During the initial cycle at a current density of 0.1 A g.sup.?1, PAA/SF-based Si/C electrode delivered a lithiation capacity of 3,415 mAh g.sup.?1 with an initial Coulombic efficiency (ICE) of 85%, which is comparable to those of PAA-based one (3,466 mAh g.sup.?1 and 86%). However, the cycled PAA-based Si/C electrode showed several cracks on the surface and big gaps between electrode materials and the copper foil. This observation is caused by the rigidness and weak adhesion force of the PAA. In contrast, PAA/SF-based electrode showed a compact surface and cross-section after the first cycle, indicating strong adhesive binding of the PAA/SF composite binder.
[0071]
[0072] On the other hand, example Si/C electrodes with PAA/SF composite binders delivered a specific capacity of 776 mAh g.sup.?1 with an average CE of 99.6% after 500 cycles, which is higher than those of PAA-based electrode. Moreover, PAA/SF-based electrodes showed reversible voltage curves with a smaller overpotential when compared with PAA-based one. The morphologies of cycled Si/C electrodes with PAA and PAA/SF binders were further examined. After 500 cycles, PAA-based electrode showed wrinkles and large cracks through the electrode because of the poor adhesion force of PAA, leading to fast capacity decay during long cycling. However, the PAA/SF-based electrode still maintained an intact surface and cross section after 500 cycles, suggesting good structural integrity of electrode because of the strong adhesion force of the PAA/SF binder.
[0073] To further demonstrate the effect of binder on electrochemical property of Si/C electrodes, the cycling performance of example Si/C electrodes fabricated with other binders including PAA/SF(1/1), PAA/SF(1/2), and PAA/CMC were measured. Example Si/C electrodes with PAA/SF(1/1) and PAA/SF(1/2) binder showed an initial CE of 79.7% and 70.4% at 0.1 A g.sup.?1, respectively. When tested at 0.5 C, PAA/SF(1/1)-based electrode exhibited a specific capacity of 1,200 mAh g.sup.?1 after 100 cycles at 0.5 C but showed gradual capacity decay in the following cycles. Moreover, the PAA/SF(1/2)-based electrode showed very fast capacity decay even after the first cycle at 0.5 C, which can be attributed to the reduced binding ability of PAA/SF with the increase of SF. Also, the Si/C electrode with PAA/CMC binder achieved an initial CE of 86.8% at 0.1 A g.sup.?1 but showed gradual capacity decay with a low specific capacity (<500 mAh g.sup.?1) at 0.5 C after 500 cycles compared with PAA/SF-based one.
Electrochemical Performance of Si/C Electrodes with PAA and PAA/SF Binder
[0074] In addition to structural integrity of example Si/C electrodes, electrochemical performances of the example Si/C electrodes with PAA and PAA/SF binder were evaluated. During the first lithiation process, PAA/SF-based Si/C electrode showed a cathodic peak at 0.79 V vs. Li/Li.sup.+, as shown in
[0075]
[0076] From the foregoing, it will be appreciated that specific embodiments of the technology have been described herein for purposes of illustration, but that various modifications may be made without deviating from the disclosure. In addition, many of the elements of one embodiment may be combined with other embodiments in addition to or in lieu of the elements of the other embodiments. Accordingly, the disclosure is not limited except as by the appended claims.