Patent Publication Number: US-2021167361-A1

Title: Silicon-based energy storage devices with anhydride containing electrolyte additives

Description:
BACKGROUND 
     Field 
     The present application relates generally to electrolytes for energy storage devices. In particular, the present application relates to electrolytes and additives for use in lithium (Li)-ion energy storage devices with silicon-based anode materials. 
     Description of the Related Art 
     The present application relates generally to electrolytes for energy storage devices. In particular, the present application relates to electrolytes and additives for use in lithium-ion energy storage devices with silicon-based anode materials. 
     DESCRIPTION OF THE RELATED ART 
     As the demands for both zero-emission electric vehicles and grid-based energy storage systems increase, lower costs and improvements in energy density, power density, and safety of lithium (Li)-ion batteries are highly desirable. Enabling the high energy density and safety of Li-ion batteries requires the development of high-capacity, and high-voltage cathodes, high-capacity anodes and accordingly functional electrolytes with high voltage stability, interfacial compatibility with electrodes and safety. 
     A lithium-ion battery typically includes a separator and/or electrolyte between an anode and a cathode. In one class of batteries, the separator, cathode and anode materials are individually formed into sheets or films. Sheets of the cathode, separator and anode are subsequently stacked or rolled with the separator separating the cathode and anode (e.g., electrodes) to form the battery. Typical electrodes include electro-chemically active material layers on electrically conductive metals (e.g., aluminum and copper). Films can be rolled or cut into pieces which are then layered into stacks. The stacks are of alternating electro-chemically active materials with the separator between them. 
     Si is one of the most promising anode materials for Li-ion batteries due to its high specific gravimetric and volumetric capacity (3579 mAh/g and 2194 mAh/cm 3  vs. 372 mAh/g and 719 mAh/cm 3  for graphite), and low lithiation potential (&lt;0.4 V vs. Li/Li+). Among the various cathodes presently available, layered lithium transition-metal oxides such as Ni-rich Li[Ni x Co y Mn(Al) 1-x-y ]O 2  (NCM or NCA) are the most promising ones due to their high theoretical capacity (˜280 mAh/g) and relatively high average operating potential (3.6 V vs Li/Li + ). Coupling Si anodes with high-voltage Ni rich NCM (or NCA) cathodes can deliver more energy than conventional Li-ion batteries with graphite-based anodes, due to the high capacity of these new electrodes. However, both Si-based anodes and high-voltage Ni rich NCM (or NCA) cathodes face formidable technological challenges, and long-term cycling stability with high-Si anodes paired with NCM or NCA cathodes has yet to be achieved. 
     For anodes, silicon-based materials can provide significant improvement in energy density. However, the large volumetric expansion (&gt;300%) during the Li alloying/dealloying processes can lead to disintegration of the active material and the loss of electrical conduction paths, thereby reducing the cycling life of the battery. In addition, an unstable solid electrolyte interphase (SEI) layer can develop on the surface of the cycled anodes, and leads to an endless exposure of Si particle surfaces to the liquid electrolyte. This results in an irreversible capacity loss at each cycle due to the reduction at the low potential where the liquid electrolyte reacts with the exposed surface of the Si anode. In addition, oxidative instability of the conventional non-aqueous electrolyte takes place at voltages beyond 4.5 V, which can lead to accelerated decay of cycling performance. Because of the generally inferior cycle life of Si compared to graphite, only a small amount of Si or Si alloy is used in conventional anode materials. 
     The NCM (or NCA) cathode usually suffers from an inferior stability and a low capacity retention at a high cut-off potential. The reasons can be ascribed to the unstable surface layer&#39;s gradual exfoliation, the continuous electrolyte decomposition, and the transition metal ion dissolution into electrolyte solution. In order to make good use of Si anode//NCM or NCA cathode-based Li-ion battery systems, the aforementioned barriers need to be overcome. 
     One strategy for overcoming these barriers includes exploring new electrolyte additives in order to make good use of Si anode//NCM or NCA cathode-based full cells. The next generation of electrolyte additives to be developed should be able to form a uniform, stable SEI layer on the surface of Si anodes. This layer should have low impedance and be electronically insulating, but ionically conductive to Li-ion. Additionally, the SEI layer formed by the additive should have excellent elasticity and mechanical strength to overcome the problem of expansion and shrinkage of the Si anode volume. On the cathode side, the ideal additives should be oxidized preferentially to the solvent molecule in the bare electrolyte, resulting in a protective cathode electrolyte interphase (CEI) film formed on the surface of the NCM (or NCA). At the same time, it should help alleviate the dissolution phenomenon of transition metal ions and decrease surface resistance on cathode side. In addition, they could help improve the physical properties of the electrolyte such as ionic conductivity, viscosity, and wettability. 
     SUMMARY 
     In some aspects, energy storage devices are provided. In some embodiments, the energy storage device includes a first electrode and a second electrode, wherein at least one of the first electrode and the second electrode is a Si-based electrode. I In some embodiments, the energy storage device includes a separator between the first electrode and the second electrode. In some embodiments, the energy storage device includes an electrolyte. In some embodiments, the energy storage device includes at least one electrolyte additive comprising a compound of Formula (A): 
     
       
         
         
             
             
         
       
     
     In some embodiments, A is 
     
       
         
         
             
             
         
       
     
     In some embodiments, each Y and Z is independently selected from 
     
       
         
         
             
             
         
       
     
     In some embodiments, i is 1 or 2. In some embodiments, each R and R 2  is independently selected from the group consisting of —R a  and —OR b . In some embodiments, each R a  and R b  is independently selected from the group consisting of a C1-C14 alkyl, a C2-C6 alkenyl, a C2-C6 alkynyl, a C1-C14 heteroalkyl with 1 or more O heteroatoms, a C3-C6 cycloalkyl, an unsaturated C3-C6 cycloalkyl, a C5-C10 polycyclic cycloalkyl, a C5-C6 aromatic and a C5-C6 heteroaromatic, wherein members of the group may be optionally substituted by alkyl, alkenyl, alkynyl, —Cl, —F, —CHF 2 , —CF 3 , —CN, sulfonyl, carbonyl, carboxyl, cycloalkyl, polycyclic cycloalkyl, heterocycloalkyl, aromatic and heteroaromatic groups, and wherein the optional substituents may be further optionally substituted by —Cl, —F and aromatic groups. 
     In some embodiments, the second electrode is a Si-dominant electrode. In some embodiments, the second electrode comprises a self-supporting composite material film. In some embodiments, the composite material film comprises greater than 0% and less than about 90% by weight of silicon particles, and greater than 0% and less than about 90% by weight of one or more types of carbon phases, wherein at least one of the one or more types of carbon phases is a substantially continuous phase that holds the composite material film together such that the silicon particles are distributed throughout the composite material film. 
     In some embodiments, the electrolyte further comprises fluoroethylene carbonate (FEC). In some embodiments, the electrolyte is substantially free of non-fluorine containing cyclic carbonate. 
     In some embodiments, the electrolyte additive is selected from the group consisting of pentafluoropropionic anhydride (PFPA); heptafluorobutyric anhydride (HFBA); 3H-Perfluoropropanoic anhydride; 3,3,3-Trifluoropropanoic anhydride; 4,4,4-Trifluorobutyric anhydride; 2-(Trifluoromethoxy)acetic anhydride; 5,5,5-Trifluoropentanoic anhydride; 4,4,5,5,5-Pentafluoropentanoic anhydride; Penta-fluoropentanoicanhydride; Nonafluoropentanoic anhydride; Perfluorohexanoic anhydride; 2-(Trifluoromethyl)-3,3,3-trifluoropropionic anhydride; 4,4,4-Trifluoro-3-(trifluoromethyl)butyric anhydride; 4,4,5,5,6,6,6-Heptafluorohexanoic anhydride; 5H-Perfluoropentanoic anhydride; 4,4,5,5,6,6,7,7,7-Nonafluoroheptanoic anhydride; 4,5,5,6,6,6-Hexafluoro-4-(trifluoromethyl) hexanoic anhydride; Perfluorodecanoic anhydride; Perfluorooctanoic anhydride; Perfluoroheptanoic anhydride; Perfluoro-3,5,5-trimethylhexanoic anhydride; 2,2,2-trifluoroacetic propionic anhydride; 2,2,3,3-Tetrafluoro-3-(trifluoromethoxy)propionic anhydride; Perfluoro(4-methoxybutanoic) anhydride; Nonafluoro-3,6-dioxaheptanoic anhydride; Undecafluoro-2-methyl-3-oxahexanoic anhydride; 4-(Heptafluoroisopropoxy)hexafluorobutanoic anhydride; Perfluoro-3,6,9-trioxadecanoic anhydride; Perfluoro(2,5-dimethyl-3,6-dioxanonanoic anhydride); 2-(Trifluoromethoxy)aceticanhydride; Perfluoro-3,6-dioxadecanoicanhydride; Perfluoro(2,5,8-trimethyl-3,6,9-trioxadodecanoic) anhydride; methyl 3-(ethylsulfanyl)-2,2,3,3-tetrafluoropropanoate; 2-ethoxy-2-oxoacetic anhydride; Methoxyacetic anhydride; (2-ethoxyacetyl) 2-ethoxyacetate; (2-acetyloxyacetyl) 2-acetyloxyacetate; Anhydride of malonic acid monoethyl ester; Trifluoroperacetic anhydride; acrylic anhydride; methacrylic anhydride; pent-4-enoic anhydride; Sorbic anhydride; Itaconic anhydride; 2-Hexenoic anhydride; Hex-2-enoyl hex-2-enoate; Furylacrylic acid anhydride; Cinnamic anhydride; acrylic benzoic anhydride; acrylic-trifluoroacetic anhydride; cyclopropanecarboxylic acid anhydride; cyclopentanecarboxylic anhydride; 2-cyclopropylacetic anhydride; cyclohexanecarboxylic anhydride; 2,2-Dimethyl-3-(2-methyl-1-propen-1-yl)cyclopropanecarboxylic anhydride; Adamantane-1-carboxylic acid anhydride; cyclohexene-1-carbonyl cyclohexene-1-carboxylate; [2-(tetrazol-1-yl)acetyl] 2-(tetrazol-1-yl)acetate; cis,cis-2-benzoylcyclopropanecarboxylic acid, anhydride; 3-(2,2-Dichloroethenyl)-2,2-dimethyl-cyclopropanecarboxylic acid anhydride; Trifluoromethanesulfonic acid anhydride; Triflic anhydride; Pentafluoroethanesulfonic acid anhydride; Nonafluorobutanesulfonic anhydride; 2-cyano-Acetic acid; anhydride with acetic acid; and 2-cyanoacetic anhydride. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  depicts a cross-sectional schematic diagram of an example of a Li-ion battery  300  implemented as a pouch cell. 
         FIGS. 2A and 2B  show the dQ/dV curves during Charge (A) and Discharge (B) of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 3A and 3B  show capacity retention (A) and normalized capacity retention (B) of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 4A and 4B  shows average resistance during 10 sec pulse for the charge (A) and discharge (B) processes of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 5A and 5B  shows average resistance during 30 sec pulses for the charge (A) and discharge (B) processes of an embodiment of Si-dominant anode/NCM-622 cathode full cells, respectively. 
         FIGS. 6A and 6B  show the dQ/dV curves during Charge (A) and Discharge (B) of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 7A and 7B  show capacity retention (A) and normalized capacity retention (B) of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 8A and 8B  show average resistance during 10 sec pulse for the charge (A) and discharge (B) processes of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 9A and 9B  show average resistance during 30 sec pulses for the charge (A) and discharge (B) processes of an embodiment of Si-dominant anode/NCM-622 cathode full cells, respectively. 
         FIGS. 10A and 10B  show the dQ/dV curves during Charge (A) and Discharge (B) of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 11A and 11B  show capacity retention (A) and normalized capacity retention (B) of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 12A and 12B  show average resistance during 10 sec pulse for the charge (A) and discharge (B) processes of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 13A and 13B  show average resistance during 30 sec pulses for the charge (A) and discharge (B) processes of an embodiment of Si-dominant anode/NCM-622 cathode full cells, respectively. 
         FIGS. 14A and 14B  show the dQ/dV curves during Charge (A) and Discharge (B) of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 15A and 15B  show capacity retention (A) and normalized capacity retention (B) of an embodiment of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 16A and 16B  show average resistance during 10 sec pulse for the charge (A) and discharge (B) processes of an embodiment of Si-dominant anode//NCM-622 cathode full cells, respectively. 
         FIGS. 17A and 17B  show average resistance during 30 sec pulses for the charge (A) and discharge (B) processes of an embodiment of Si-dominant anode/NCM-622 cathode full cells, respectively. 
     
    
    
     DETAILED DESCRIPTION 
     Definitions 
     The term “alkyl” refers to a straight or branched, saturated, aliphatic radical having the number of carbon atoms indicated. The alkyl moiety may be branched or straight chain. For example, C1-C6 alkyl includes, but is not limited to, methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl, pentyl, isopentyl, hexyl, etc. Other alkyl groups include, but are not limited to heptyl, octyl, nonyl, decyl, etc. Alkyl can include any number of carbons, such as 1-2, 1-3, 1-4, 1-5, 1-6, 1-7, 1-8, 1-9, 1-10, 1-11, 1-12 2-3, 2-4, 2-5, 2-6, 3-4, 3-5, 3-6, 4-5, 4-6 and 5-6. The alkyl group is typically monovalent, but can be divalent, such as when the alkyl group links two moieties together. 
     The term “fluoro-alkyl” refers to an alkyl group where one, some, or all hydrogen atoms have been replaced by fluorine. 
     The term “alkylene” refers to an alkyl group, as defined above, linking at least two other groups, i.e., a divalent hydrocarbon radical. The two moieties linked to the alkylene can be linked to the same atom or different atoms of the alkylene. For instance, a straight chain alkylene can be the bivalent radical of —(CH 2 ) n —, where n is 1, 2, 3, 4, 5, 6, 7, 8, 9, or 10. Alkylene groups include, but are not limited to, methylene, ethylene, propylene, isopropylene, butylene, isobutylene, sec-butylene, pentylene and hexylene. 
     The term “alkoxy” refers to alkyl group having an oxygen atom that either connects the alkoxy group to the point of attachment or is linked to two carbons of the alkoxy group. Alkoxy groups include, for example, methoxy, ethoxy, propoxy, iso-propoxy, butoxy, 2-butoxy, iso-butoxy, sec-butoxy, tert-butoxy, pentoxy, hexoxy, etc. The alkoxy groups can be further substituted with a variety of substituents described within. For example, the alkoxy groups can be substituted with halogens to form a “halo-alkoxy” group, or substituted with fluorine to form a “fluoro-alkoxy” group. 
     The term “alkenyl” refers to either a straight chain or branched hydrocarbon of 2 to 6 carbon atoms, having at least one double bond. Examples of alkenyl groups include, but are not limited to, vinyl, propenyl, isopropenyl, 1-butenyl, 2-butenyl, isobutenyl, butadienyl, 1-pentenyl, 2-pentenyl, isopentenyl, 1,3-pentadienyl, 1,4-pentadienyl, 1-hexenyl, 2-hexenyl, 3-hexenyl, 1,3-hexadienyl, 1,4-hexadienyl, 1,5-hexadienyl, 2,4-hexadienyl, or 1,3,5-hexatrienyl. Alkenyl groups can also have from 2 to 3, 2 to 4, 2 to 5, 3 to 4, 3 to 5, 3 to 6, 4 to 5, 4 to 6 and 5 to 6 carbons. The alkenyl group is typically monovalent, but can be divalent, such as when the alkenyl group links two moieties together. 
     The term “alkenylene” refers to an alkenyl group, as defined above, linking at least two other groups, i.e., a divalent hydrocarbon radical. The two moieties linked to the alkenylene can be linked to the same atom or different atoms of the alkenylene. Alkenylene groups include, but are not limited to, ethenylene, propenylene, isopropenylene, butenylene, isobutenylene, sec-butenylene, pentenylene and hexenylene. 
     The term “alkynyl” refers to either a straight chain or branched hydrocarbon of 2 to 6 carbon atoms, having at least one triple bond. Examples of alkynyl groups include, but are not limited to, acetylenyl, propynyl, 1-butynyl, 2-butynyl, isobutynyl, sec-butynyl, butadiynyl, 1-pentynyl, 2-pentynyl, isopentynyl, 1,3-pentadiynyl, 1,4-pentadiynyl, 1-hexynyl, 2-hexynyl, 3-hexynyl, 1,3-hexadiynyl, 1,4-hexadiynyl, 1,5-hexadiynyl, 2,4-hexadiynyl, or 1,3,5-hexatriynyl. Alkynyl groups can also have from 2 to 3, 2 to 4, 2 to 5, 3 to 4, 3 to 5, 3 to 6, 4 to 5, 4 to 6 and 5 to 6 carbons. The alkynyl group is typically monovalent, but can be divalent, such as when the alkynyl group links two moieties together. 
     The term “alkynylene” refers to an alkynyl group, as defined above, linking at least two other groups, i.e., a divalent hydrocarbon radical. The two moieties linked to the alkynylene can be linked to the same atom or different atoms of the alkynylene. Alkynylene groups include, but are not limited to, ethynylene, propynylene, butynylene, sec-butynylene, pentynylene and hexynylene. 
     The term “cycloalkyl” refers to a saturated or partially unsaturated, monocyclic, fused bicyclic, bridged polycyclic, or spiro ring assembly containing from 3 to 12, from 3 to 10, or from 3 to 7 ring atoms, or the number of atoms indicated. Monocyclic rings include, for example, cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, and cyclooctyl. Bicyclic and polycyclic rings include, for example, norbornane, decahydronaphthalene and adamantane. For example, C3-C8 cycloalkyl includes cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cyclooctyl, and norbornane. As used herein, the term “fused” refers to two rings which have two atoms and one bond in common. For example, in the following structure, rings A and B are fused 
     
       
         
         
             
             
         
       
     
     As used herein, the term “bridged polycyclic” refers to compounds wherein the cycloalkyl contains a linkage of one or more atoms connecting non-adjacent atoms. The following structures 
     
       
         
         
             
             
         
       
     
     are examples of “bridged” rings. As used herein, the term “spiro” refers to two rings which have one atom in common and the two rings are not linked by a bridge. Examples of fused cycloalkyl groups are decahydronaphthalenyl, dodecahydro-1H-phenalenyl and tetradecahydroanthracenyl; examples of bridged cycloalkyl groups are bicyclo[1.1.1]pentyl, adamantanyl, and norbornanyl; and examples of spiro cycloalkyl groups include spiro[3.3]heptane and spiro[4.5]decane. 
     The term “cycloalkylene” refers to a cycloalkyl group, as defined above, linking at least two other groups, i.e., a divalent hydrocarbon radical. The two moieties linked to the cycloalkylene can be linked to the same atom or different atoms of the cycloalkylene. Cycloalkylene groups include, but are not limited to, cyclopropylene, cyclobutylene, cyclopentylene, cyclohexylene, and cyclooctylene. 
     The term “aryl” refers to a monocyclic or fused bicyclic, tricyclic or greater, aromatic ring assembly containing 6 to 16 ring carbon atoms. For example, aryl may be phenyl, benzyl or naphthyl, preferably phenyl. Aryl groups can be mono-, di- or tri-substituted by one, two or three radicals. Preferred as aryl is naphthyl, phenyl or phenyl mono- or disubstituted by alkoxy, phenyl, halogen, alkyl or trifluoromethyl, especially phenyl or phenyl-mono- or disubstituted by alkoxy, halogen or trifluoromethyl, and in particular phenyl. 
     The term “arylene” refers to an aryl group, as defined above, linking at least two other groups. The two moieties linked to the arylene are linked to different atoms of the arylene. Arylene groups include, but are not limited to, phenylene. 
     The term “heteroaryl” refers to a monocyclic or fused bicyclic or tricyclic aromatic ring assembly containing 5 to 16 ring atoms, where from 1 to 4 of the ring atoms are a heteroatom each N, O or S. For example, heteroaryl includes pyridyl, indolyl, indazolyl, quinoxalinyl, quinolinyl, isoquinolinyl, benzothienyl, benzofuranyl, furanyl, pyrrolyl, thiazolyl, benzothiazolyl, oxazolyl, isoxazolyl, triazolyl, tetrazolyl, pyrazolyl, imidazolyl, thienyl, or any other radicals substituted, especially mono- or di-substituted, by e.g. alkyl, nitro or halogen. Pyridyl represents 2-, 3- or 4-pyridyl, advantageously 2- or 3-pyridyl. Thienyl represents 2- or 3-thienyl. Quinolinyl represents preferably 2-, 3- or 4-quinolinyl. Isoquinolinyl represents preferably 1-, 3- or 4-isoquinolinyl. Benzopyranyl, benzothiopyranyl represents preferably 3-benzopyranyl or 3-benzothiopyranyl, respectively. Thiazolyl represents preferably 2- or 4-thiazolyl, and most preferred 4-thiazolyl. Triazolyl is preferably 1-, 2- or 5-(1,2,4-triazolyl). Tetrazolyl is preferably 5-tetrazolyl. 
     Preferably, heteroaryl is pyridyl, indolyl, quinolinyl, pyrrolyl, thiazolyl, isoxazolyl, triazolyl, tetrazolyl, pyrazolyl, imidazolyl, thienyl, furanyl, benzothiazolyl, benzofuranyl, isoquinolinyl, benzothienyl, oxazolyl, indazolyl, or any of the radicals substituted, especially mono- or di-substituted. 
     The term “heteroalkyl” refers to an alkyl group having from 1 to 3 heteroatoms such as N, O and S. The heteroatoms can also be oxidized, such as, but not limited to, —S(O)— and —S(O) 2 —. For example, heteroalkyl can include ethers, thioethers, alkyl-amines and alkyl-thiols. 
     The term “heteroalkylene” refers to a heteroalkyl group, as defined above, linking at least two other groups. The two moieties linked to the heteroalkylene can be linked to the same atom or different atoms of the heteroalkylene. 
     The term “heterocycloalkyl” refers to a ring system having from 3 ring members to about 20 ring members and from 1 to about 5 heteroatoms such as N, O and S. The heteroatoms can also be oxidized, such as, but not limited to, —S(O)— and —S(O) 2 —. For example, heterocycle includes, but is not limited to, tetrahydrofuranyl, tetrahydrothiophenyl, morpholino, pyrrolidinyl, pyrrolinyl, imidazolidinyl, imidazolinyl, pyrazolidinyl, pyrazolinyl, piperazinyl, piperidinyl, indolinyl, quinuclidinyl and 1,4-dioxa-8-aza-spiro[4.5]dec-8-yl. 
     The term “heterocycloalkylene” refers to a heterocyclalkyl group, as defined above, linking at least two other groups. The two moieties linked to the heterocycloalkylene can be linked to the same atom or different atoms of the heterocycloalkylene. 
     The term “optionally substituted” is used herein to indicate a moiety that can be unsubstituted or substituted by one or more substituent. When a moiety term is used without specifically indicating as substituted, the moiety is unsubstituted. 
     DESCRIPTION 
     To overcome the current obstacles associated with developing high-energy Li-ion full-cells with Si-based anodes, the next generation of oxidation-stable electrolytes or electrolyte additives are developed. The electrolyte or electrolyte additives can form a stable, electronically insulating but ionically conducting SEI layer on the surface of Si anodes. Additionally, these electrolytes or additives may also help modify cathode surfaces, forming stable CEI layers. These could enable the electrochemical stability of Li-ion batteries when cycled at higher voltages and help with calendar life of the batteries. In addition, to alleviate battery safety concerns, these additives may impart an increased thermal stability to the organic components of the electrolyte, drive a rise in the flash point of the electrolyte formulations, increase the flame-retardant effectiveness and enhance thermal stability of SEI or CEI layers on the surface of electrodes. 
     In the present disclosure, the use of chemical compounds comprising anhydride electrolyte additives for energy storage devices with Si-dominant anodes are described. In some embodiments, the Si-dominant anode comprises about 50% to about 95%, about 50% to about 90%, about 50% to about 80%, about 50% to about 70%, about 50% to about 60%, about 55% to about 95%, about 55% to about 90%, about 55% to about 85%, about 55% to about 80%, about 55% to about 75%, about 55% to about 70%, or about 55% to about 65% by weight of Si. Due to their unique chemical structures and functional groups, anhydride containing electrolyte additives may bring the following benefits: (i) stabilize solid/electrolyte interface film to reduce electrolyte reactions (oxidation on the NCM or NCA cathode and reduction on the Si anode), prevent or reduce Si anode volume expansion, and protect against transition metal ion dissolution from NCM or NCA cathode; and (ii) reduce the flammability and enhance the thermal stability of organic electrolytes and increase the safety of electrolyte solutions. Due to their versatility in reaction chemistry and overall stability in electrochemical environments, as well as excellent flame resistance or fire retardant properties, introducing anhydride containing electrolyte additives into electrolyte solutions may help improve both overall electrochemical performance and safety of Si anode-based Li-ion batteries. 
     Typical carbon anode electrodes include a current collector such as a copper sheet. Carbon is deposited onto the collector along with an inactive binder material. Carbon is often used because it has excellent electrochemical properties and is also electrically conductive. If the current collector layer (e.g., copper layer) was removed, the carbon would likely be unable to mechanically support itself. Therefore, conventional electrodes require a support structure such as the collector to be able to function as an electrode. In some embodiments, the electrode (e.g., anode or cathode) compositions described in this application can produce electrodes that are self-supported. The need for a metal foil current collector is eliminated or minimized because conductive carbonized polymer is used for current collection in the anode structure as well as for mechanical support. In typical applications for the mobile industry, a metal current collector is typically added to ensure sufficient rate performance. The carbonized polymer can form a substantially continuous conductive carbon phase in the entire electrode as opposed to particulate carbon suspended in a non-conductive binder in one class of conventional Li-ion battery electrodes. Advantages of a carbon composite blend that utilizes a carbonized polymer can include, for example, 1) higher capacity, 2) enhanced overcharge/discharge protection, 3) lower irreversible capacity due to the elimination (or minimization) of metal foil current collectors, and 4) potential cost savings due to simpler manufacturing. 
     Anode electrodes currently used in the rechargeable Li-ion cells typically have a specific capacity of approximately 200 milliamp hours per gram (including the metal foil current collector, conductive additives, and binder material). In order to increase volumetric and gravimetric energy density of Li-ion batteries, silicon may be used as the active material for the cathode or anode. Several types of silicon materials, e.g., silicon nanopowders, silicon nanowires, porous silicon, and ball-milled silicon, are viable candidates as active materials for the negative or positive electrode. Small particle sizes (for example, sizes in the nanometer range) generally can increase cycle life performance. They also can display very high initial irreversible capacity. However, small particle sizes also can result in very low volumetric energy density (for example, for the overall cell stack) due to the difficulty of packing the active material. Larger particle sizes, (for example, sizes in the micron range) generally can result in higher density anode material. However, the expansion of the silicon active material can result in poor cycle life due to particle cracking. For example, silicon can swell in excess of 300% upon Li insertion. Because of this expansion, anodes including silicon should be allowed to expand while maintaining electrical contact between the silicon particles. 
     Cathode electrodes described herein may include metal oxide cathode materials, such as lithium Cobalt Oxide (LiCoO 2 ) (LCO), Ni-rich oxides, high voltage cathode materials, lithium rich oxides, nickel-rich layered oxides, Li-rich layered oxides, high-voltage spinel oxides, and high-voltage polyanionic compounds. Ni-rich oxides and/or high voltage cathode materials may include NCM and NCA. One example of NCM material includes LiNi 0.6 Co 0.2 Mn 0.2 O 2  (NCM-622). Li-rich oxides may include xLi 2 Mn 3 O 2 .(1−x)LiNi a Co b Mn c O 2 . Ni-rich layered oxides may include LiNi 1+x M 1−x O z  (where M=Co, Mn or Al). Li rich layered oxides may include LiN 1+x M 1−x O 2  (where M=Co, Mn or Ni). High-voltage spinel oxides may include LiNi 0.5 Mn 1.5 O 4 . High-voltage polyanionic compounds may include phosphates, sulfates, silicates. 
     As described herein and in U.S. patent application Ser. Nos. 13/008,800 and 13/601,976, entitled “Composite Materials for Electrochemical Storage” and “Silicon Particles for Battery Electrodes,” respectively, certain embodiments utilize a method of creating monolithic, self-supported anodes using a carbonized polymer. Because the polymer is converted into an electrically conductive and electrochemically active matrix, the resulting electrode is conductive enough that, in some embodiments, a metal foil or mesh current collector can be omitted or minimized. The converted polymer also acts as an expansion buffer for silicon particles during cycling so that a high cycle life can be achieved. In certain embodiments, the resulting electrode is an electrode that is comprised substantially of active material. In further embodiments, the resulting electrode is substantially active material. The electrodes can have a high energy density of between about 500 mAh/g to about 1200 mAh/g that can be due to, for example, 1) the use of silicon, 2) elimination or substantial reduction of metal current collectors, and 3) being comprised entirely or substantially entirely of active material. 
     As described herein and in U.S. patent application Ser. No. 14/800,380, entitled “Electrolyte Compositions for Batteries,” the entirety of which is hereby incorporated by reference, composite materials can be used as an anode in most conventional Li-ion batteries; they may also be used as the cathode in some electrochemical couples with additional additives. The composite materials can also be used in either secondary batteries (e.g., rechargeable) or primary batteries (e.g., non-rechargeable). In some embodiments, the composite materials can be used in batteries implemented as a pouch cell, as described in further details herein. In certain embodiments, the composite materials are self-supported structures. In some embodiments, the composite materials are self-supported monolithic structures. For example, a collector may be included in the electrode comprised of the composite material. In certain embodiments, the composite material can be used to form carbon structures discussed in U.S. patent application Ser. No. 12/838,368 entitled “Carbon Electrode Structures for Batteries,” the entirety of which is hereby incorporated by reference. Furthermore, the composite materials described herein can be, for example, silicon composite materials, carbon composite materials, and/or silicon-carbon composite materials. 
     In some embodiments, a largest dimension of the silicon particles can be less than about 40 μm, less than about 1 μm, between about 10 nm and about 40 μm, between about 10 nm and about 1 μm, less than about 500 nm, less than about 100 nm, and about 100 nm. All, substantially all, or at least some of the silicon particles may comprise the largest dimension described above. For example, an average or median largest dimension of the silicon particles can be less than about 40 μm, less than about 1 μm, between about 10 nm and about 40 μm, between about 10 nm and about 1 μm, less than about 500 nm, less than about 100 nm, and about 100 nm. The amount of silicon in the composite material can be greater than zero percent by weight of the mixture and composite material. In certain embodiments, the mixture comprises an amount of silicon, the amount being within a range of from about 0% to about 90% by weight, including from about 30% to about 80% by weight of the mixture. The amount of silicon in the composite material can be within a range of from about 0% to about 35% by weight, including from about 0% to about 25% by weight, from about 10% to about 35% by weight, and about 20% by weight. In further certain embodiments, the amount of silicon in the mixture is at least about 30% by weight. Additional embodiments of the amount of silicon in the composite material include more than about 50% by weight, between about 30% and about 80% by weight, between about 50% and about 70% by weight, and between about 60% and about 80% by weight. Furthermore, the silicon particles may or may not be pure silicon. For example, the silicon particles may be substantially silicon or may be a silicon alloy. In one embodiment, the silicon alloy includes silicon as the primary constituent along with one or more other elements. 
     As described herein, micron-sized silicon particles can provide good volumetric and gravimetric energy density combined with good cycle life. In certain embodiments, to obtain the benefits of both micron-sized silicon particles (e.g., high energy density) and nanometer-sized silicon particles (e.g., good cycle behavior), silicon particles can have an average particle size in the micron range and a surface including nanometer-sized features. In some embodiments, the silicon particles have an average particle size (e.g., average diameter or average largest dimension) between about 0.1 μm and about 30 μm or between about 0.1 μm and all values up to about 30 μm. For example, the silicon particles can have an average particle size between about 0.5 μm and about 25 μm, between about 0.5 μm and about 20 μm, between about 0.5 μm and about 15 μm, between about 0.5 μm and about 10 μm, between about 0.5 μm and about 5 μm, between about 0.5 μm and about 2 μm, between about 1 μm and about 20 μm, between about 1 μm and about 15 μm, between about 1 μm and about 10 μm, between about 5 μm and about 20 μm, etc. Thus, the average particle size can be any value between about 0.1 μm and about 30 μm, e.g., 0.1 μm, 0.5 μm, 1 μm, 5 μm, 10 μm, 15 μm, 20 μm, 25 μm, and 30 μm. 
     The composite material can be formed by pyrolyzing a polymer precursor, such as polyamide acid. The amount of carbon obtained from the precursor can be about 50 weight percent by weight of the composite material. In certain embodiments, the amount of carbon from the precursor in the composite material is about 10% to about 25% by weight. The carbon from the precursor can be hard carbon. Hard carbon can be a carbon that does not convert into graphite even with heating in excess of 2800 degrees Celsius. Precursors that melt or flow during pyrolysis convert into soft carbons and/or graphite with sufficient temperature and/or pressure. Hard carbon may be selected since soft carbon precursors may flow and soft carbons and graphite are mechanically weaker than hard carbons. Other possible hard carbon precursors can include phenolic resins, epoxy resins, and other polymers that have a very high melting point or are crosslinked. In some embodiments, the amount of hard carbon in the composite material has a value within a range of from about 10% to about 25% by weight, about 20% by weight, or more than about 50% by weight. In certain embodiments, the hard carbon phase is substantially amorphous. In other embodiments, the hard carbon phase is substantially crystalline. In further embodiments, the hard carbon phase includes amorphous and crystalline carbon. The hard carbon phase can be a matrix phase in the composite material. The hard carbon can also be embedded in the pores of the additives including silicon. The hard carbon may react with some of the additives to create some materials at interfaces. For example, there may be a silicon carbide layer between silicon particles and the hard carbon. 
     In certain embodiments, graphite particles are added to the mixture. Advantageously, graphite can be an electrochemically active material in the battery as well as an elastic deformable material that can respond to volume change of the silicon particles. Graphite is the preferred active anode material for certain classes of Li-ion batteries currently on the market because it has a low irreversible capacity. Additionally, graphite is softer than hard carbon and can better absorb the volume expansion of silicon additives. In certain embodiments, a largest dimension of the graphite particles is between about 0.5 microns and about 20 microns. All, substantially all, or at least some of the graphite particles may comprise the largest dimension described herein. In further embodiments, an average or median largest dimension of the graphite particles is between about 0.5 microns and about 20 microns. In certain embodiments, the mixture includes greater than 0% and less than about 80% by weight of graphite particles. In further embodiments, the composite material includes about 40% to about 75% by weight graphite particles. 
     In certain embodiments, conductive particles which may also be electrochemically active are added to the mixture. Such particles can enable both a more electronically conductive composite as well as a more mechanically deformable composite capable of absorbing the large volumetric change incurred during lithiation and de-lithiation. In certain embodiments, a largest dimension of the conductive particles is between about 10 nanometers and about 7 millimeters. All, substantially all, or at least some of the conductive particles may comprise the largest dimension described herein. In further embodiments, an average or median largest dimension of the conductive particles is between about 10 nm and about 7 millimeters. In certain embodiments, the mixture includes greater than zero and up to about 80% by weight conductive particles. In further embodiments, the composite material includes about 45% to about 80% by weight conductive particles. The conductive particles can be conductive carbon including carbon blacks, carbon fibers, carbon nanofibers, carbon nanotubes, graphite, etc. Many carbons that are considered as conductive additives that are not electrochemically active become active once pyrolyzed in a polymer matrix. Alternatively, the conductive particles can be metals or alloys including copper, nickel, or stainless steel. 
     The composite material may also be formed into a powder. For example, the composite material can be ground into a powder. The composite material powder can be used as an active material for an electrode. For example, the composite material powder can be deposited on a collector in a manner similar to making a conventional electrode structure, as known in the industry. In some embodiments, the full capacity of the composite material may not be utilized during use of the battery to improve battery life (e.g., number charge and discharge cycles before the battery fails or the performance of the battery decreases below a usability level). For example, a composite material with about 70% by weight silicon particles, about 20% by weight carbon from a precursor, and about 10% by weight graphite may have a maximum gravimetric capacity of about 2000 mAh/g, while the composite material may only be used up to a gravimetric capacity of about 550 to about 850 mAh/g. Although, the maximum gravimetric capacity of the composite material may not be utilized, using the composite material at a lower capacity can still achieve a higher capacity than certain Li-ion batteries. In certain embodiments, the composite material is used or only used at a gravimetric capacity below about 70% of the composite material&#39;s maximum gravimetric capacity. For example, the composite material is not used at a gravimetric capacity above about 70% of the composite material&#39;s maximum gravimetric capacity. In further embodiments, the composite material is used or only used at a gravimetric capacity below about 50% of the composite material&#39;s maximum gravimetric capacity or below about 30% of the composite material&#39;s maximum gravimetric capacity. 
     Electrolyte 
     An electrolyte for a Li-ion battery can include a solvent and a Li ion source, such as a Li-containing salt. The composition of the electrolyte may be selected to provide a Li-ion battery with improved performance. In some embodiments, the electrolyte may contain an electrolyte additive. As described herein, a Li-ion battery may include a first electrode, a second electrode, a separator between the first electrode and the second electrode, and an electrolyte in contact with the first electrode, the second electrode, and the separator. The electrolyte serves to facilitate ionic transport between the first electrode and the second electrode. In some embodiments, the first electrode and the second electrode can refer to anode and cathode or cathode and anode, respectively. 
     In some embodiments, the electrolyte for a Li-ion battery may include a solvent comprising a fluorine-containing component, such as a fluorine-containing cyclic carbonate, a fluorine-containing linear carbonate, and/or a fluoroether. In some embodiments, the electrolyte can include more than one solvent. For example, the electrolyte may include two or more co-solvents. In some embodiments, at least one of the co-solvents in the electrolyte is a fluorine-containing compound. In some embodiments, the fluorine-containing compound may be fluoroethylene carbonate (FEC), 1,1,2,2-tetrafluoroethyl 2,2,3,3-tetrafluoropropyl ether, or difluoroethylene carbonate (F2EC). In some embodiments, the co-solvent may be selected from the group consisting of FEC, ethyl methyl carbonate (EMC), 1,1,2,2-tetrafluoroethyl 2,2,3,3-tetrafluoropropyl ether, F2EC, ethylene carbonate (EC), diethyl carbonate (DEC), dimethyl carbonate (DMC), propylene carbonate (PC), and gamma-Butyrolactone (GBL). In some embodiments, the electrolyte contains FEC. In some embodiments, the electrolyte contains both EMC and FEC. In some embodiments, the electrolyte may further contain 1,1,2,2-tetrafluoroethyl 2,2,3,3-tetrafluoropropyl ether, EC, DEC, DMC, PC, GBL, and/or F2EC as a co-solvent. In some embodiments, the electrolyte is free or substantially free of non-fluorine-containing cyclic carbonates, such as EC, GBL, and PC. 
     As used herein, a co-solvent of an electrolyte has a concentration of at least about 10% by volume (vol %). In some embodiments, a co-solvent of the electrolyte may be about 20 vol %, about 40 vol %, about 60 vol %, or about 80 vol %, or about 90 vol % of the electrolyte. In some embodiments, a co-solvent may have a concentration from about 10 vol % to about 90 vol %, from about 10 vol % to about 80 vol %, from about 10 vol % to about 60 vol %, from about 20 vol % to about 60 vol %, from about 20 vol % to about 50 vol %, from about 30 vol % to about 60 vol %, or from about 30 vol % to about 50 vol %. 
     For example, in some embodiments, the electrolyte may contain a fluorine-containing cyclic carbonate, such as FEC, at a concentration of about 10 vol % to about 60 vol %, including from about 20 vol % to about 50 vol %, and from about 20 vol % to about 40 vol %. In some embodiments, the electrolyte may comprise a linear carbonate that does not contain fluorine, such as EMC, at a concentration of about 40 vol % to about 90 vol %, including from about 50 vol % to about 80 vol %, and from about 60 vol % to about 80 vol %. In some embodiments, the electrolyte may comprise other solvents, such as 1,1,2,2-tetrafluoroethyl 2,2,3,3-tetrafluoropropyl ether at a concentration of from about 10 vol % to about 30 vol %, including from about 10 vol % to about 20 vol %. 
     In some embodiments, the electrolyte is substantially free of cyclic carbonates other than fluorine-containing cyclic carbonates (i.e., non-fluorine-containing cyclic carbonates). Examples of non-fluorine-containing carbonates include EC, PC, GBL, and vinylene carbonate (VC). 
     Electrolyte Additives 
     In some embodiments, the electrolyte may further comprise one or more additives. As used herein, an additive of the electrolyte refers to a component that makes up less than 10% by weight (wt %) of the electrolyte. In some embodiments, the amount of each additive in the electrolyte may be from about 0.2 wt % to about 1 wt %, 0.1 wt % to about 2 wt %, 0.2 wt % to about 9 wt %, from about 0.5 wt % to about 9 wt %, from about 1 wt % to about 9 wt %, from about 1 wt % to about 8 wt %, from about 1 wt % to about 8 wt %, from about 1 wt % to about 7 wt %, from about 1 wt % to about 6 wt %, from about 1 wt % to about 5 wt %, from about 2 wt % to about 5 wt %, or any value in between. In some embodiments, the total amount of the additive(s) may be from about 1 wt % to about 9 wt %, from about 1 wt % to about 8 wt %, from about 1 wt % to about 7 wt %, from about 2 wt % to about 7 wt %, or any value in between. 
     Anhydride Compound 
     In some embodiments, anhydride can be a compound of Formula (A) having the structure: 
     
       
         
         
             
             
         
       
     
     In some embodiments of Formula (A), A is 
     
       
         
         
             
             
         
       
     
     In some embodiments of Formula (A), each Y and Z is independently selected from 
     
       
         
         
             
             
         
       
     
     In some embodiments of Formula (A), i is 1 or 2. 
     In some embodiments of Formula (A), each R 1  and R 2  is independently selected from the group consisting of —R a  and —OR b . In some embodiments of Formula (A), each R a  and R b  is independently selected from the group consisting of a C1-C14 alkyl, a C2-C6 alkenyl, a C2-C6 alkynyl, a C1-C14 heteroalkyl with 1 or more O heteroatoms, a C3-C6 cycloalkyl, an unsaturated C3-C6 cycloalkyl, a C5-C10 polycyclic cycloalkyl, a C5-C6 aromatic and a C5-C6 heteroaromatic, wherein members of the group may be optionally substituted by alkyl, alkenyl, alkynyl, —Cl, —F, —CHF 2 , —CF 3 , —CN, sulfonyl, carbonyl, carboxyl, cycloalkyl, polycyclic cycloalkyl, heterocycloalkyl, aromatic and heteroaromatic groups, and wherein the optional substituents may be further optionally substituted by —Cl, —F and aromatic groups. 
     The electrolyte or additive may comprise an anhydride. In some embodiments, the additive may be an additive chemical compound comprising anhydride. In some embodiments, the anhydride may be included in the electrolyte as a co-solvent. In other embodiments, the anhydride may be included in the electrolyte as an additive. For example, the electrolyte may contain an anhydride as a co-solvent at a concentration of about 10 vol % or more. In other embodiments, the electrolyte may contain an anhydride compound as an additive at less than 10 weight %. 
     In some embodiments, the anhydride compound is selected from PFPA; HFBA; 3H-Perfluoropropanoic anhydride; 3,3,3-Trifluoropropanoic anhydride; 4,4,4-Trifluorobutyric anhydride; 2-(Trifluoromethoxy)acetic anhydride; 5,5,5-Trifluoropentanoic anhydride; 4,4,5,5,5-Pentafluoropentanoic anhydride; Penta-fluoropentanoicanhydride; Nonafluoropentanoic anhydride; Perfluorohexanoic anhydride; 2-(Trifluoromethyl)-3,3,3-trifluoropropionic anhydride; 4,4,4-Trifluoro-3-(trifluoromethyl)butyric anhydride; 4,4,5,5,6,6,6-Heptafluorohexanoic anhydride; 5H-Perfluoropentanoic anhydride; 4,4,5,5,6,6,7,7,7-Nonafluoroheptanoic anhydride; 4,5,5,6,6,6-Hexafluoro-4-(trifluoromethyl) hexanoic anhydride; Perfluorodecanoic anhydride; Perfluorooctanoic anhydride; Perfluoroheptanoic anhydride; Perfluoro-3,5,5-trimethylhexanoic anhydride; 2,2,2-trifluoroacetic propionic anhydride; 2,2,3,3-Tetrafluoro-3-(trifluoromethoxy)propionic anhydride; Perfluoro(4-methoxybutanoic) anhydride; Nonafluoro-3,6-dioxaheptanoic anhydride; Undecafluoro-2-methyl-3-oxahexanoic anhydride; 4-(Heptafluoroisopropoxy)hexafluorobutanoic anhydride; Perfluoro-3,6,9-trioxadecanoic anhydride; Perfluoro(2,5-dimethyl-3,6-dioxanonanoic anhydride); 2-(Trifluoromethoxy)aceticanhydride; Perfluoro-3,6-dioxadecanoicanhydride; Perfluoro(2,5,8-trimethyl-3,6,9-trioxadodecanoic) anhydride; methyl 3-(ethylsulfanyl)-2,2,3,3-tetrafluoropropanoate; 2-ethoxy-2-oxoacetic anhydride; Methoxyacetic anhydride; (2-ethoxyacetyl) 2-ethoxyacetate; (2-acetyloxyacetyl) 2-acetyloxyacetate; Anhydride of malonic acid monoethyl ester; Trifluoroperacetic anhydride; acrylic anhydride; methacrylic anhydride; pent-4-enoic anhydride; Sorbic anhydride; Itaconic anhydride; 2-Hexenoic anhydride; Hex-2-enoyl hex-2-enoate; Furylacrylic acid anhydride; Cinnamic anhydride; acrylic benzoic anhydride; acrylic-trifluoroacetic anhydride; cyclopropanecarboxylic acid anhydride; cyclopentanecarboxylic anhydride; 2-cyclopropylacetic anhydride; cyclohexanecarboxylic anhydride; 2,2-Dimethyl-3-(2-methyl-1-propen-1-yl)cyclopropanecarboxylic anhydride; Adamantane-1-carboxylic acid anhydride; cyclohexene-1-carbonyl cyclohexene-1-carboxylate; [2-(tetrazol-1-yl)acetyl] 2-(tetrazol-1-yl)acetate; cis,cis-2-benzoylcyclopropanecarboxylic acid, anhydride; 3-(2,2-Dichloroethenyl)-2,2-dimethyl-cyclopropanecarboxylic acid anhydride; Trifluoromethanesulfonic acid anhydride; Triflic anhydride; Pentafluoroethanesulfonic acid anhydride; Nonafluorobutanesulfonic anhydride; 2-cyano-Acetic acid; anhydride with acetic acid; and 2-cyanoacetic anhydride. 
     Example structures of anhydride compounds and are shown below: 
     
       
         
         
             
             
         
       
       
         
         
             
             
         
       
       
         
         
             
             
         
       
       
         
         
             
             
         
       
       
         
         
             
             
         
       
       
         
         
             
             
         
       
       
         
         
             
             
         
       
       
         
         
             
             
         
       
       
         
         
             
             
         
       
       
         
         
             
             
         
       
       
         
         
             
             
         
       
     
     In some embodiments, a Li-containing salt for a Li-ion battery may comprise lithium hexafluorophosphate (LiPF 6 ). In some embodiments, a Li-containing salt for a Li-ion battery may comprise one or more of lithium tetrafluoroborate (LiBF 4 ), lithium hexafluoroarsenate monohydrate (LiAsF 6 ), lithium perchlorate (LiClO 4 ), Lithium bis(trifluoromethanesulfonyl)imide (LiTFSI), Lithium bis(fluorosulfonyl)imide (LiFSI), lithium bis(oxalato)borate (LiBOB), lithium difluoro(oxalate)borate (LiDFOB), lithium triflate (LiCF 3 SO 3 ), and lithium 2-trifluoromethyl-4,5-dicyanoimidazole (LiTDI), etc. In some embodiments, the electrolyte can have a salt concentration of about 1 mole/L (M). 
     These electrolyte additives, along with the electrolytes, can react with silicon on an anode to form a SEI layer that can crack and/or continue to grow as the silicon containing anode expands and contracts during cycling. Furthermore, these electrolyte additives, along with the electrolytes, can react with metal oxides on a cathode to form a CEI layer that can suppress further decomposition of the electrode on the surface of the cathode. Without being bound to the theory or mode of operation, it is believed that the presence of an anhydride compound in the electrolyte can result in a SEI and or CEI layer with improved performance. An SEI layer comprising an anhydride may demonstrate improved chemical stability and increased density, for example, compared to SEI layers formed by electrolytes without additives or with traditional additives. As such, the change in thickness and surface reactivity of the interface layer are limited, which may in turn facilitate reduction in capacity fade and/or generation of excessive gaseous byproducts during operation of the Li-ion battery. A CEI layer comprising an anhydride compound may demonstrate may help minimize the transition metal ion dissolutions and structure changes on cathode side and may provide favorable kinetics resulting in improved cycling stability and rate capability. In some embodiments, electrolyte solvents comprising an anhydride compound may be less flammable and more flame retardant. 
     In some embodiments, a Li-ion battery comprising an electrolyte composition according to one or more embodiments described herein, and an anode having a composite electrode film according to one or more embodiments described herein, may demonstrate reduced gassing and/or swelling at about room temperature (e.g., about 20° C. to about 25° C.) or elevated temperatures (e.g., up to temperatures of about 85° C.), increased cycle life at about room temperature or elevated temperatures, and/or reduced cell growth/electrolyte consumption per cycle, for example compared to Li-ion batteries comprising conventionally available electrolyte compositions in combination with an anode having a composite electrode film according to one or more embodiments described herein. In some embodiments, a Li-ion battery comprising an electrolyte composition according to one or more embodiments described herein and an anode having a composite electrode film according to one or more embodiments described herein may demonstrate reduced gassing and/or swelling across various temperatures at which the battery may be subject to testing, such as temperatures between about −20° C. and about 130° C. (e.g., compared to Li-ion batteries comprising conventionally available electrolyte compositions in combination with an anode having a composite electrode film according to one or more embodiments described herein). 
     Gaseous byproducts may be undesirably generated during battery operation, for example, due to chemical reactions between the electrolyte and one or more other components of the Li-ion battery, such as one or more components of a battery electrode. Excessive gas generation during operation of the Li-ion battery may adversely affect battery performance and/or result in mechanical and/or electrical failure of the battery. For example, undesired chemical reactions between an electrolyte and one or more components of an anode may result in gas generation at levels which can mechanically (e.g., structural deformation) and/or electrochemically degrade the battery. In some embodiments, the composition of the anode and the composition of the electrolyte can be selected to facilitate desired gas generation performance. 
     Energy Storage Device 
     The electrolytes and electrolyte additives described herein may be advantageously utilized within an energy storage device. In some embodiments, energy storage devices may include batteries, capacitors, and battery-capacitor hybrids. In some embodiments, the energy storage device comprise Li. In some embodiments, the energy storage device may comprise at least one electrode, such as an anode and/or cathode. In some embodiments, at least one electrode may be a Si-based electrode. In some embodiments, the Si-based electrode is a Si-dominant electrode, where silicon is the majority of the active material used in the electrode (e.g., greater than 50% silicon). In some embodiments, the energy storage device comprises a separator. In some embodiments, the separator is between a first electrode and a second electrode. 
     In some embodiments, the energy storage device comprises an electrolyte. In some embodiments, the electrolyte comprises a solvent, solvent additive and/or compound as described previously herein. For example, in some embodiments, the electrolyte comprises an anhydride compound as described previously herein. 
     Pouch Cell 
     As described herein, a battery can be implement as a pouch cell.  FIG. 1  shows a cross-sectional schematic diagram of an example of a Li-ion battery  300  implemented as a pouch cell, according to some embodiments. The battery  300  comprises an anode  316  in contact with a negative current collector  308 , a cathode  304  in contact with a positive current collector  310 , a separator  306  disposed between the anode  316  and the cathode  304 . In some embodiments, a plurality of anodes  316  and cathode  304  may be arranged into a stacked configuration with a separator  306  separating each anode  316  and cathode  304 . Each negative current collector  308  may have one anode  316  attached to each side; each positive current collector  310  may have one cathode  304  attached to each side. The stacks are immersed in an electrolyte  314  and enclosed in a pouch  312 . The anode  302  and the cathode  304  may comprise one or more respective electrode films formed thereon. The number of electrodes of the battery  300  may be selected to provide desired device performance. 
     With further reference to  FIG. 1 , the separator  306  may comprise a single continuous or substantially continuous sheet, which can be interleaved between adjacent electrodes of the electrode stack. For example, the separator  306  may be shaped and/or dimensioned such that it can be positioned between adjacent electrodes in the electrode stack to provide desired separation between the adjacent electrodes of the battery  300 . The separator  306  may be configured to facilitate electrical insulation between the anode  302  and the cathode  304 , while permitting ionic transport between the anode  302  and the cathode  304 . In some embodiments, the separator  306  may comprise a porous material, including a porous polyolefin material. 
     The Li-ion battery  300  may include an electrolyte  314 , for example an electrolyte having a composition as described herein. The electrolyte  314  is in contact with the anode  302 , the cathode  304 , and the separator  306 . 
     With continued reference to  FIG. 1 , the anode  302 , cathode  304  and separator  306  of the Li-ion battery  300  may be enclosed in a housing comprising a pouch  312 . In some embodiments, the pouch  312  may comprise a flexible material. For example, the pouch  312  may readily deform upon application of pressure on the pouch  312 , including pressure exerted upon the pouch  312  from within the housing. In some embodiments, the pouch  312  may comprise aluminum. For example, the pouch  312  may comprise a laminated aluminum pouch. 
     In some embodiments, the Li-ion battery  300  may comprise an anode connector (not shown) and a cathode connector (not shown) configured to electrically couple the anodes and the cathodes of the electrode stack to an external circuit, respectively. The anode connector and a cathode connector may be affixed to the pouch  312  to facilitate electrical coupling of the battery  300  to an external circuit. The anode connector and the cathode connector may be affixed to the pouch  312  along one edge of the pouch  312 . The anode connector and the cathode connector can be electrically insulated from one another, and from the pouch  312 . For example, at least a portion of each of the anode connector and the cathode connector can be within an electrically insulating sleeve such that the connectors can be electrically insulated from one another and from the pouch  312 . 
     EXAMPLES 
     The below example devices and processes for device fabrication generally described below, and the performances of Li-ion batteries with different electrolytes and electrolyte additives are evaluated. 
     Example 1 
     In Example 1, 1 wt. % and 2 wt. % pentafluoropropionic anhydride (PFPA) was used as an electrolyte additive and added to 1.2M LiPF 6  in FEC/EMC (3/7 wt %)-based electrolytes for Si-dominant anode//NCM-622 cathode full 5 layer pouch cells, and compared to a control without an electrolyte additive. The full cells were tested at 1 C/0.5 C charge/discharge processes with the working voltage window of 4.2V to 3.0V. These results showed improved electrochemical performances of full cells with PFPA electrolyte additives compared with the control. 
     Example 2 
     In Example 2, 0.5 wt. %, 1 wt. %, 0.1 wt. % and 0.2 wt. % of acrylic anhydride (AA) was used as an electrolyte additive and added to 1.2M LiPF 6  in FEC/EMC (3/7 wt. %)-based electrolytes for Si-dominant anodes//NCM cathode full 5 layer pouch cells, and compared to a control without an electrolyte additive. The full cells were tested using a 1 C/0.5 C charge/discharge cycle regime with the working voltage window of 4.2V to 3.0V. Some of the results show clearly improved electrochemical performance compared with the control. 
     In  FIGS. 2A-5B , the electrolytes used were: 1) a control with 1.2 M LiPF 6  in FEC/EMC (3/7 wt. %) (shown as a dotted line); and 2) 1.2M LiPF 6  in FEC/EMC (3/7 wt. %)+0.5 wt. % AA (shown as a solid line). The Si-dominant anodes contain about 80 wt. % Si, 5 wt % graphite and 15 wt. % glass carbon (from resin), and are laminated on 15 μm Cu foil. The average loading is about 3.8 mg/cm 2 . The cathodes contain about 92 wt. % NCM-622, 4 wt. % Super P and 4 wt. % PVDF5130, and are laminated on 15 μm Al foil. The average loading is about 23 mg/cm 2 . 
       FIGS. 2A and 2B  show the dQ/dV curves during Charge (A) and Discharge (B) of Si-dominant anode//NCM-622 cathode full cells, respectively, where control cells and cells containing 0.5 wt. % AA are tested. The dQ/dV data for both control and 0.5 wt. % AA additive-containing cells were obtained through the following testing protocol: Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes. The 1 st  formation cycle dQ/dV curves in  FIG. 2A  show that the 0.5 wt. % AA additive-containing cells have strong multiple decomposition peaks at very early stages compared with the controls. These results indicate that the AA additive can be decomposed prior to the main electrolyte solutions at the 1 st  cycle charging processes and form an artificial SEI film on the surface of the Si-dominant anodes. 
       FIGS. 3A and 3B  show capacity retention (A) and normalized capacity retention (B) of Si-dominant anode//NCM-622 cathode full cells, respectively, where control cells and cells containing 0.5 wt. % AA are tested. The long-term cycling for both control and 0.5 wt. % AA additive-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms Internal Resistance (IR) Check, 100 ms IR Check, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. After each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 0.5 wt. % AA-containing cells were formed for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes. 
       FIGS. 3A and 3B  indicate that when adding 0.5 wt. % AA into 1.2 M LiPF 6  in FEC/EMC (3/7 wt %)-based electrolytes, the corresponding cell capacity retention is improved compared with reference electrolyte-based control cells. 
       FIGS. 4A and 4B  shows average resistance during 10 sec pulse for the charge (A) and discharge (B) processes of Si-dominant anode//NCM-622 cathode full cells, respectively, where control cells and cells containing 0.5 wt. % AA are tested. The long-term cycling for both control and 0.5 wt. % AA-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. But after each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 0.5 wt % AA-containing cells were formed for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes. The Res fields are values calculated by using data points of voltage and current. It linearly interpolates for a voltage at 10 s in the charge/discharge step between the two data points before and after that time. Then it takes the difference between that voltage and the last voltage during rest when current is 0 and divides it by the charge or discharge current. Res_10 s_C is calculated using discharge data (for the charged state). Res_10 s_DC is calculated using charge data (for the cell state at the beginning of the cycle). 
     The results shown in  FIGS. 4A and 4B  indicate that 0.5 wt. % AA-containing cells have smaller average resistance after 10 s charge and discharge processes compared with reference electrolyte-based control cells after about 250 cycles. 
       FIGS. 5A and 5B  shows average resistance during 30 sec pulses for the charge (A) and discharge (B) processes of Si-dominant anode/NCM-622 cathode full cells, respectively, where control cells and cells containing 0.5 wt. % AA are tested. The long-term cycling for both control and 0.5 wt. % AA-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. But after each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 0.5 wt % AA-containing cells were formatted for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes. The Res fields are values calculated by using data points of voltage and current. It linearly interpolates for a voltage at 30 s in the charge/discharge step between the two data points before and after that time. Then it takes the difference between that voltage and the last voltage during rest when current is 0 and divides it by the charge or discharge current. Res_30 s_C is calculated using discharge data (for the charged state). Res_30 s_DC is calculated using charge data (for the cell state at the beginning of the cycle). 
     The results of  FIGS. 5A and 5B  show that 0.5 wt. % AA-containing cells have smaller average resistance after 30 s charge and discharge processes compared with reference electrolyte-based control cells after about 250 cycles. 
     Example 3 
     In Example 3, 0.5 wt. %, 1 wt. %, and 2 wt. % of PFPA, HFBA or CPCAA were used as electrolyte additives and added into 1.2M LiPF 6  in FEC/EMC (3/7 wt %)-based electrolytes for Si-dominant anode//NCM cathode full 5 layer pouch cells, and compared to a control without an electrolyte additive. The full cells were tested using a 1 C/0.5 C charge/discharge cycle regime with the working voltage window of 4.2V to 3.0V. Some of the results show clearly improved electrochemical performance compared with the control. 
     In  FIGS. 6A-9B , the electrolytes used were: 1) a control with 1.2 M LiPF 6  in FEC/EMC (3/7 wt. %) (shown as a dotted line); and 2) 1.2M LiPF 6  in FEC/EMC (3/7 wt. %)+1 wt. % PFPA (shown as a solid line). The Si-dominant anodes contain about 80 wt. % Si, 5 wt % graphite and 15 wt. % glass carbon (from resin), and are laminated on 15 μm Cu foil. The average loading is about 3.8 mg/cm 2 . The cathodes contain about 92 wt. % NCM-622, 4 wt. % Super P and 4 wt. % PVDF5130, and are laminated on 15 μm Al foil. The average loading is about 23 mg/cm 2 . 
       FIGS. 6A and 6B  show the dQ/dV curves during Charge (A) and Discharge (B) of Si-dominant anode//NCM-622 cathode full cells, respectively, where control cells and cells containing 1 wt. % PFPA are tested. The dQ/dV data for both control and the 1 wt. % PFPA additive-containing cells were obtained through the following testing protocol: Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes. 
     The 1 st  formation cycle dQ/dV curves in  FIG. 6A  show that 1 wt. % PFPA additive-containing cells have strong multiple decomposition peaks at very early stages compared with the controls. These results indicate that the PFPA additive can be decomposed on the surface of Si anodes prior to the main electrolyte solutions during the 1 st  cycle charging processes and form an SEI film before the electrode reacts with other electrolyte components. 
       FIGS. 7A and 7B  show capacity retention (A) and normalized capacity retention (B) of Si-dominant anode//NCM-622 cathode full cells, respectively, where control cells and cells containing 1 wt. % PFPA are tested. The long-term cycling for both control and 1 wt. % PFPA additive-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. After each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 1 wt. % PFPA-containing cells were formatted for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes.  FIGS. 7A and 7B  indicate that when adding 1 wt. % PFPA into 1.2 M LiPF 6  in FEC/EMC (3/7 wt %)-based electrolytes, the cell capacity retention is improved compared with reference electrolyte-based control cells. 
       FIGS. 8A and 8B  show average resistance during 10 sec pulse for the charge (A) and discharge (B) processes of Si-dominant anode//NCM-622 cathode full cells, respectively, where control cells and cells containing 1 wt. % PFPA are tested. The long-term cycling for both control and 1 wt. % PFPA-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. After each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 1 wt. % PFPA-containing cells were formed for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes. The Res fields are values calculated by using data points of voltage and current. It linearly interpolates for a voltage at 10 s in the charge/discharge step between the two data points before and after that time. Then it takes the difference between that voltage and the last voltage during rest when current is 0 and divides it by the charge or discharge current. Res_10 s_C is calculated using discharge data (for the charged state). Res_10 s_DC is calculated using charge data (for the cell state at the beginning of the cycle). The results of  FIGS. 8A and 8B  show that 1 wt. % PFPA-containing cells have smaller average resistance after 10 s charge and discharge processes compared with reference electrolyte-based control cells after about 200 cycles. 
       FIGS. 9A and 9B  show average resistance during 30 sec pulses for the charge (A) and discharge (B) processes of Si-dominant anode/NCM-622 cathode full cells, respectively, where control cells and cells containing 1 wt. % PFPA are tested. The long-term cycling for both control and 1 wt. % PFPA-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. After each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 1 wt. % PFPA-containing cells were formed for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes. The Res fields are values calculated by using data points of voltage and current. It linearly interpolates for a voltage at 30 s in the charge/discharge step between the two data points before and after that time. Then it takes the difference between that voltage and the last voltage during rest when current is 0 and divides it by the charge or discharge current. Res_30 s_C is calculated using discharge data (for the charged state). Res_30 s_DC is calculated using charge data (for the cell state at the beginning of the cycle). The results of  FIGS. 9A and 9B  show that 1 wt. % PFPA-containing cells have smaller average resistance after 30 s charge and discharge processes compared with reference electrolyte-based control cells after about 200 cycles. 
     In  FIGS. 10A-13B , the electrolytes used were: 1) a control with 1.2 M LiPF 6  in FEC/EMC (3/7 wt. %) (shown as a dotted line); and 2) 1.2M LiPF 6  in FEC/EMC (3/7 wt. %)+1 wt. % HFBA (shown as a solid line). The Si-dominant anodes contain about 80 wt. % Si, 5 wt % graphite and 15 wt. % glass carbon (from resin), and are laminated on 15 μm Cu foil. The average loading is about 3.8 mg/cm 2 . The cathodes contain about 92 wt. % NCM-622, 4 wt. % Super P and 4 wt. % PVDF5130, and are laminated on 15 μm Al foil. The average loading is about 23 mg/cm 2 . 
       FIGS. 10A and 10B  show the dQ/dV curves during Charge (A) and Discharge (B) of Si-dominant anode//NCM-622 cathode full cells, respectively, where control cells and cells containing 1 wt. % HFBA are tested. The dQ/dV data for both control and 1 wt. % HFBA additive-containing cells were obtained through the following testing protocol: Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes. The 1 st  formation cycle dQ/dV curves in  FIG. 10A  show that 1 wt. % HFBA additive-containing systems have strong multiple decomposition peaks at very early stages compared with control ones. These results indicate that the HFBA additive is decomposed before the main electrolyte solutions and forms an artificial SEI film on the surface of the Si anodes during the 1 st  cycle charging processes. 
       FIGS. 11A and 11B  show capacity retention (A) and normalized capacity retention (B) of Si-dominant anode//NCM-622 cathode full cells, where control cells and cells containing 1 wt. % HFBA are tested. The long-term cycling for both control and 1 wt. % HFBA additive-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. After each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 1 wt. % HFBA-containing cells were formed for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes.  FIGS. 11A and 11B  indicate that when adding 1 wt. % HFBA into 1.2 M LiPF 6  in FEC/EMC (3/7 wt %)-based electrolytes, the cell capacity retention is improved compared with reference electrolyte-based control cells. 
       FIGS. 12A and 12B  show average resistance during 10 sec pulse for the charge (A) and discharge (B) processes of Si-dominant anode//NCM-622 cathode full cells, respectively, where control cells and cells containing 1 wt. % HFBA are tested. The long-term cycling for both control and 1 wt. % HFBA-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. After each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 1 wt. % HFBA-containing cells were formed for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes. The Res fields are values calculated by using data points of voltage and current. It linearly interpolates for a voltage at 10 s in the charge/discharge step between the two data points before and after that time. Then it takes the difference between that voltage and the last voltage during rest when current is 0 and divides it by the charge or discharge current. Res_10 s_C is calculated using discharge data (for the charged state). Res_10 s_DC is calculated using charge data (for the cell state at the beginning of the cycle). The results in  FIGS. 12A and 12B  show that 1 wt. % HFBA-containing cells have smaller average resistance after 10 s charge and discharge processes compared with reference electrolyte-based control cells after about 250 cycles. 
       FIGS. 13A and 13B  show average resistance during 30 sec pulses for the charge (A) and discharge (B) processes of Si-dominant anode/NCM-622 cathode full cells, where control cells and cells containing 1 wt. % HFBA was tested. The long-term cycling for both control and 1 wt. % HFBA-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. But after each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 1 wt. % HFBA-containing cells were formed for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes. The Res fields are values calculated by using data points of voltage and current. It linearly interpolates for a voltage at 30 s in the charge/discharge step between the two data points before and after that time. Then it takes the difference between that voltage and the last voltage during rest when current is 0 and divides it by the charge or discharge current. Res_30 s_C is calculated using discharge data (for the charged state). Res_30 s_DC is calculated using charge data (for the cell state at the beginning of the cycle). The results in  FIGS. 13A and 13B  show that 1 wt. % HFBA-containing cells have smaller average resistance after 30 s charge and discharge processes compared with reference electrolyte-based control cells after about 250 cycles. 
     In  FIGS. 14A-17B , the electrolytes used were: 1) a control with 1.2 M LiPF 6  in FEC/EMC (3/7 wt. %) (shown as a dotted line); and 2) 1.2M LiPF 6  in FEC/EMC (3/7 wt. %)+2 wt. % HFBA (shown as a solid line). The Si-dominant anodes contain about 80 wt. % Si, 5 wt % graphite and 15 wt. % glass carbon (from resin), and are laminated on 15 μm Cu foil. The average loading is about 3.8 mg/cm 2 . The cathodes contain about 92 wt. % NCM-622, 4 wt. % Super P and 4 wt. % PVDF5130, and are laminated on 15 μm Al foil. The average loading is about 23 mg/cm 2 . 
       FIGS. 14A and 14B  show the dQ/dV curves during Charge (A) and Discharge (B) of Si-dominant anode//NCM-622 cathode full cells, respectively, where control cells and cells containing 2 wt % HFBA are tested. The dQ/dV data for both control and 2 wt. % HFBA additive-containing cells were obtained through the following testing protocol: Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes. The 1 st  formation cycle dQ/dV curves in  FIG. 14A  show that 2 wt. % HFBA additive-containing systems have strong multiple decomposition peaks at very early stages compared with control ones. These results indicate that the HFBA additive could be decomposed before the main electrolyte solution and form an artificial SEI film on the surface of the Si-dominant anode during the 1 st  cycle charging processes. 
       FIGS. 15A and 15B  show capacity retention (A) and normalized capacity retention (B) of Si-dominant anode//NCM-622 cathode full cells, respectively, where control cells and cells containing 2 wt. % HFBA are tested. The long-term cycling for both control and 2 wt. % HFBA additive-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. But after each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 2 wt. % HFBA-containing cells were formed for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes.  FIGS. 15A and 15B  indicate that when adding 2 wt. % HFBA into 1.2 M LiPF 6  in FEC/EMC (3/7 wt %)-based electrolytes, the cell capacity retention is improved compared with reference electrolyte-based control cells. 
       FIGS. 16A and 16B  show average resistance during 10 sec pulse for the charge (A) and discharge (B) processes of Si-dominant anode//NCM-622 cathode full cells, where control cells and cells containing 2 wt. % HFBA are tested. The long-term cycling for both control and 2 wt. % HFBA-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. But after each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 2 wt. % HFBA-containing cells were formed for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes. The Res fields are values calculated by using data points of voltage and current. It linearly interpolates for a voltage at 10 s in the charge/discharge step between the two data points before and after that time. Then it takes the difference between that voltage and the last voltage during rest when current is 0 and divides it by the charge or discharge current. Res_10 s_C is calculated using discharge data (for the charged state). Res_10 s_DC is calculated using charge data (for the cell state at the beginning of the cycle). The results in  FIGS. 16A and 16B  show that 2 wt. % HFBA-containing cells have smaller average resistance after 10 s charge and discharge processes compared with reference electrolyte-based control cells after about 250 cycles. 
       FIGS. 17A and 17B  show average resistance during 30 sec pulses for the charge (A) and discharge (B) processes of Si-dominant anode/NCM-622 cathode full cells, respectively, where control cells and cells containing 2 wt. % HFBA are tested. The long-term cycling for both control and 2 wt. % HFBA-containing cells include: (i) At the 1 st  cycle, charge at 0.5 C to 4.2 V for 5 hours, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.2 C to 2.75 V, rest 5 minutes, 1 ms IR, 100 ms IR; and (ii) from the 2 nd  cycle, charge at 1 C to 4.2 V until 0.05 C, rest 5 minutes, 1 ms IR, 100 ms IR, discharge at 0.5 to 3.0 V, rest 5 minutes, 1 ms IR, 100 ms IR. After each 49 cycles, the test conditions in the 1 st  cycle were repeated. 
     In addition, both control and 2 wt. % HFBA-containing cells were formed for 6 cycles at the following conditions before long-term cycling: (i) At the 1 st  cycle, Rest 5 minutes, charge at 0.025 C to 25% nominal capacity, charge at 0.2 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.2 C to 3.0 V, rest 5 minutes; and (ii) from 2 nd  to 6 th  cycles, charge at 0.5 C to 4.2 V until 0.05 C, rest 5 minutes, discharge at 0.5 C to 3.3 V, rest 5 minutes. The Res fields are values calculated by using data points of voltage and current. It linearly interpolates for a voltage at 30 s in the charge/discharge step between the two data points before and after that time. Then it takes the difference between that voltage and the last voltage during rest when current is 0 and divides it by the charge or discharge current. Res_30 s_C is calculated using discharge data (for the charged state). Res_30 s_DC is calculated using charge data (for the cell state at the beginning of the cycle). The results in  FIGS. 17A and 17B  show that 2 wt. % HFBA-containing cells have smaller average resistance after 30 s charge and discharge processes compared with reference electrolyte-based control cells after about 250 cycles. 
     The aforementioned results show that the involvement of some of the proposed multifunctional linear anhydride-based additives into standard electrolyte formulations can help reduce the interfacial resistance between electrolyte/electrodes and improve the cycle life of Si-dominant anode-based Li-ion batteries. Without being bound to theory, it is assumed that the functional linear anhydrides may have high reduction potentials and may be relatively easy to be decomposed into structures such as oligo- or polymeric molecules that can enable cation conduction between the anode and the electrolyte. For example, the functional linear anhydrides containing carbon-carbon double or triple bonds could provide an easy route for polymerization under reducing conditions. The molecules with electronegative fluorine could initiate SEI creation on the surface of the Si anodes. As a result, on the Si anode side, these functional anhydride-based additives are crucial in the formation of a relatively stable, thin and beneficial SEI layer capable of limiting electrolyte decomposition during cell cycling. At the same time, the anhydride group may have a beneficial influence on the NCM cathode/electrolyte interfaces. For example, it could be reduced significantly on the surface of electrodes and help reduce the self-discharge of the cell. The additives could also form a passivation film mainly composed of organic compounds (mainly O═C—O containing species) on the NCM (or other claimed Li metal oxide cathodes such as NCA, LCO, LiNMO, Li-rich ones, etc) cathode surface and inhibit the continuous electrolyte decomposition at the cathode surface. All of these may contribute to the resistance reduction between electrolyte/electrode interfaces, and the overall cycle performance improvements in Si-dominant anode//Ni-rich NMC or NCA cathode full cells. 
     Various embodiments have been described above. Although the invention has been described with reference to these specific embodiments, the descriptions are intended to be illustrative and are not intended to be limiting. Various modifications and applications may occur to those skilled in the art without departing from the true spirit and scope of the invention as defined in the appended claims.