This document summarizes a study that characterized graphite anodes from lithium-ion battery cells after fast charging. Multi-scale characterization techniques revealed increased disorder near the edges of graphite particles in anodes that experienced lithium plating during fast charging. Specifically, transmission electron microscopy showed wavy graphite fringes and higher d-spacings near particle edges, indicating greater lattice disorder extending 20 nm into the bulk. This disorder hinders lithium ion intercalation and favors lithium plating during repeated fast charging. Scanning electron microscopy also showed fast-charged anodes were thicker due to accumulated electrolyte reduction products in pores.
2021 a new in situ and operando measurement method to determine the electri...Ary Assuncao
This document summarizes a new method for measuring the electrical conductivity of the negative active material in lead-acid batteries during operation. The method uses a model electrode with four embedded probe wires to conduct in-situ four-point probe measurements of resistance during battery cycling. Numerical simulations support the analysis of measurement results. Using this method, the document studies the evolution of discharge capacity, electrical resistance, and electrical conductivity over 10 cycles and correlates the results to known structural changes in the active material that occur during cycling.
This document summarizes manipulation strategies for two-dimensional amorphous nanomaterials (2D ANMs) to enhance their performance in electrochemical energy storage and conversion applications. It discusses two main categories of manipulation: 1) geometric configuration design, including spatial structure design (e.g. creating porous structures) and coordination environment design (e.g. defect creation); and 2) component interaction, including elemental doping/coupling and heterophase compositing. Recent examples manipulating 2D ANMs through these approaches for applications in batteries, supercapacitors and electrocatalysis are reviewed. The document concludes by discussing opportunities to further optimize manipulation of 2D ANMs.
The document describes a study that uses design of experiments (DoE) to optimize slurry-cast cathodes for solid-state batteries. Various combinations of polymer binder type and content and conductive carbon additive type and content were tested as cathode composites. Electrochemical and mechanical performance data from the experiments were analyzed using statistical software to identify optimal combinations. The predictions identified polyisobutene as the best binder and vapor-grown carbon fibers as the best additive to maximize specific capacity. Hydrogenated nitrile butadiene rubber and vapor-grown carbon fibers provided the best combination to maximize capacity retention. Additional tests were conducted to understand changes during cycling.
2021 influence of basic carbon additives on the electrochemical performance ...Ary Assuncao
This study investigates the effect of carbon surface basicity on the electrochemical performance and dynamic charge acceptance of lead-carbon batteries. Five activated carbons with different pH values ranging from 9.5 to 11.1 were prepared by ammonia and hydrogen gas treatments. Cyclic voltammetry showed that the hydrogen evolution reaction activity increased with higher carbon surface basicity. Testing of lead-carbon electrodes found a correlation between carbon pH and dynamic charge acceptance, with higher pH carbons showing improved charge currents and final dynamic charge acceptance. The carbon content also affected charge currents during simulated microcycles, demonstrating that surface chemistry and amount of carbon additive both influence the electrochemical properties and performance of lead-carbon batteries.
2021 understanding li-based battery materials via electrochemical impedance...Ary Assuncao
The document discusses the use of electrochemical impedance spectroscopy (EIS) to understand lithium-based battery materials. It states that while EIS is a powerful technique, its potential has not been fully exploited for batteries. It provides examples of advanced EIS measurement approaches and physics-based modeling that can provide new insights. These include using specialized electrode configurations, complementary techniques, and transmission line modeling to deconvolute overlapping impedance spectra features into fundamental electrochemical processes. The document advocates designing experiments with well-controlled conditions and advanced data analysis to further unlock insights from EIS into battery mechanisms.
1. The document describes a new nanohybrid material composed of polyoxomolybdate, polypyrrole, and graphene oxide for use as a high-power symmetric supercapacitor electrode.
2. The nanohybrid was synthesized via a one-pot reaction where polyoxomolybdate acted as an oxidizing agent to polymerize pyrrole monomers onto graphene oxide nanosheets.
3. Structural and morphological analysis showed the nanohybrid had an excellent architecture with good interfacial contact between components, enabling fast redox reactions for high capacitive performance.
2022 recent advances on quasi-solid-state electrolytes for supercapacitorsAry Assuncao
This document reviews recent advances in quasi-solid-state electrolytes for supercapacitors. Quasi-solid-state electrolytes provide advantages over liquid electrolytes such as reduced leakage and safety concerns while maintaining high ionic conductivity. The document summarizes different types of quasi-solid-state electrolytes including gel-polymer electrolytes and discusses their properties. It also performs a bibliographic analysis of over 300 references on parameters like ionic conductivity, capacitance, stability, and working voltage window of various quasi-solid-state electrolytes. The document concludes that gel-polymer electrolytes and aqueous-based electrolytes show promise for flexible supercapacitors but that further development is needed to improve performance.
This document summarizes a study that compared a single chamber microbial fuel cell (SC-MFC) to a double chamber microbial fuel cell (DC-MFC) using different electron acceptors. The SC-MFC used oxygen from the air as the cathode, while the DC-MFC used diluted hydrogen peroxide. Testing found the DC-MFC produced a higher open circuit voltage of 448mV compared to 200mV for the SC-MFC. The DC-MFC also generated more power, with a maximum power of 7.57mW and coulombic efficiency of 9.2%, versus 0.46mW and 1.88% respectively for the SC-MFC. This suggests hydrogen per
2021 a new in situ and operando measurement method to determine the electri...Ary Assuncao
This document summarizes a new method for measuring the electrical conductivity of the negative active material in lead-acid batteries during operation. The method uses a model electrode with four embedded probe wires to conduct in-situ four-point probe measurements of resistance during battery cycling. Numerical simulations support the analysis of measurement results. Using this method, the document studies the evolution of discharge capacity, electrical resistance, and electrical conductivity over 10 cycles and correlates the results to known structural changes in the active material that occur during cycling.
This document summarizes manipulation strategies for two-dimensional amorphous nanomaterials (2D ANMs) to enhance their performance in electrochemical energy storage and conversion applications. It discusses two main categories of manipulation: 1) geometric configuration design, including spatial structure design (e.g. creating porous structures) and coordination environment design (e.g. defect creation); and 2) component interaction, including elemental doping/coupling and heterophase compositing. Recent examples manipulating 2D ANMs through these approaches for applications in batteries, supercapacitors and electrocatalysis are reviewed. The document concludes by discussing opportunities to further optimize manipulation of 2D ANMs.
The document describes a study that uses design of experiments (DoE) to optimize slurry-cast cathodes for solid-state batteries. Various combinations of polymer binder type and content and conductive carbon additive type and content were tested as cathode composites. Electrochemical and mechanical performance data from the experiments were analyzed using statistical software to identify optimal combinations. The predictions identified polyisobutene as the best binder and vapor-grown carbon fibers as the best additive to maximize specific capacity. Hydrogenated nitrile butadiene rubber and vapor-grown carbon fibers provided the best combination to maximize capacity retention. Additional tests were conducted to understand changes during cycling.
2021 influence of basic carbon additives on the electrochemical performance ...Ary Assuncao
This study investigates the effect of carbon surface basicity on the electrochemical performance and dynamic charge acceptance of lead-carbon batteries. Five activated carbons with different pH values ranging from 9.5 to 11.1 were prepared by ammonia and hydrogen gas treatments. Cyclic voltammetry showed that the hydrogen evolution reaction activity increased with higher carbon surface basicity. Testing of lead-carbon electrodes found a correlation between carbon pH and dynamic charge acceptance, with higher pH carbons showing improved charge currents and final dynamic charge acceptance. The carbon content also affected charge currents during simulated microcycles, demonstrating that surface chemistry and amount of carbon additive both influence the electrochemical properties and performance of lead-carbon batteries.
2021 understanding li-based battery materials via electrochemical impedance...Ary Assuncao
The document discusses the use of electrochemical impedance spectroscopy (EIS) to understand lithium-based battery materials. It states that while EIS is a powerful technique, its potential has not been fully exploited for batteries. It provides examples of advanced EIS measurement approaches and physics-based modeling that can provide new insights. These include using specialized electrode configurations, complementary techniques, and transmission line modeling to deconvolute overlapping impedance spectra features into fundamental electrochemical processes. The document advocates designing experiments with well-controlled conditions and advanced data analysis to further unlock insights from EIS into battery mechanisms.
1. The document describes a new nanohybrid material composed of polyoxomolybdate, polypyrrole, and graphene oxide for use as a high-power symmetric supercapacitor electrode.
2. The nanohybrid was synthesized via a one-pot reaction where polyoxomolybdate acted as an oxidizing agent to polymerize pyrrole monomers onto graphene oxide nanosheets.
3. Structural and morphological analysis showed the nanohybrid had an excellent architecture with good interfacial contact between components, enabling fast redox reactions for high capacitive performance.
2022 recent advances on quasi-solid-state electrolytes for supercapacitorsAry Assuncao
This document reviews recent advances in quasi-solid-state electrolytes for supercapacitors. Quasi-solid-state electrolytes provide advantages over liquid electrolytes such as reduced leakage and safety concerns while maintaining high ionic conductivity. The document summarizes different types of quasi-solid-state electrolytes including gel-polymer electrolytes and discusses their properties. It also performs a bibliographic analysis of over 300 references on parameters like ionic conductivity, capacitance, stability, and working voltage window of various quasi-solid-state electrolytes. The document concludes that gel-polymer electrolytes and aqueous-based electrolytes show promise for flexible supercapacitors but that further development is needed to improve performance.
This document summarizes a study that compared a single chamber microbial fuel cell (SC-MFC) to a double chamber microbial fuel cell (DC-MFC) using different electron acceptors. The SC-MFC used oxygen from the air as the cathode, while the DC-MFC used diluted hydrogen peroxide. Testing found the DC-MFC produced a higher open circuit voltage of 448mV compared to 200mV for the SC-MFC. The DC-MFC also generated more power, with a maximum power of 7.57mW and coulombic efficiency of 9.2%, versus 0.46mW and 1.88% respectively for the SC-MFC. This suggests hydrogen per
The document describes the design and application of powder composite electrodes made of Cu, Co, Ni, Pt and Ir for use in electrosynthesis and electroanalysis in alkaline solutions. The electrodes were prepared by mixing 95% metal powder with 5% polyvinyl chloride binder. Characterization showed the electrodes had a rough, porous surface and good electrochemical stability, with higher current densities than metal sheet electrodes. Cyclic voltammetry testing demonstrated the composite electrodes had good stability over multiple cycles for electrooxidation reactions like ethanol oxidation in KOH solution. The composite electrodes are suitable for electrochemistry research applications requiring stable, conductive electrodes.
This document summarizes the electrochemical synthesis and corrosion inhibiting properties of a poly N-methyl aniline coating doped with di-N-propyl malonic acid on stainless steel. Cyclic voltammetry was used to polymerize N-methyl aniline in a solution containing di-N-propyl malonic acid on a stainless steel electrode. An adherent red polymer film was obtained. Electrochemical impedance spectroscopy and potentiodynamic polarization techniques showed that this polymer coating provided excellent corrosion protection of stainless steel in 0.5M sulfuric acid solution, with inhibition efficiencies above 99% as indicated by large increases in charge transfer resistance and decreases in corrosion current density compared to uncoated stainless steel.
This document summarizes an experiment studying the origins of large voltage hysteresis in metal fluoride lithium-ion battery conversion electrodes. Specifically, it examines iron fluoride (FeF3) as a model system using in situ X-ray absorption spectroscopy, transmission electron microscopy, density functional theory calculations, and galvanostatic intermittent titration technique. The results reveal that the phase evolution during charging and discharging is actually symmetrical, with the same intermediate phases forming. However, the spatial distribution of the electrochemically active phases differs due to kinetic effects. This leads to differences in ohmic voltage drop, reaction overpotential, and compositional inhomogeneity, causing the large observed voltage hysteresis which is kinetic rather than thermodynamic in nature
This document summarizes the synthesis, characterization, and evaluation of various IrO2-based binary metal oxide electrocatalysts for the oxygen evolution reaction. IrO2, IrxRu1-xO2, IrxSnx-1O2 and IrxTax-1O2 (where x is between 1 and 0.7) were synthesized via an adapted Adams fusion method. X-ray diffraction and electron microscopy showed the materials formed nanocrystalline solid solutions. Electrochemical testing found that adding RuO2, SnO2, or Ta2O5 to IrO2 improved its catalytic performance for oxygen evolution. Specifically, Ir0.7Ru0.3O2 exhibited the best
This document summarizes research on using electrodeposited manganese dioxide (MnO2) coatings on porous carbon substrates for capacitive deionization (CDI) applications. Two carbon substrates with different surface areas and morphologies were coated with MnO2 using galvanostatic and cyclic voltammetric deposition. Characterization of the coated electrodes found mixed MnO2 phases present. Testing in half-cell configurations showed that maximum ion uptake per mass was not necessarily optimal for practical CDI applications, where performance per electrode area is more important. The results suggest the structure and deposition method can impact how effectively the electrode volume participates in ion removal reactions.
This document describes how synchrotron-based X-ray spectroscopy techniques like XANES and STXM can provide insights into structure-performance relationships in battery materials to enable faster optimization. These techniques allow mapping of local chemistry, bonding structure, and phase distributions. Studies have shown how surface coatings and composite designs can influence properties like conductivity and stability. Chemical mapping of electrodes also revealed non-uniform reactions related to "hot spots" that correlate with performance. Faster screening of materials and correlation of structural properties with electrochemical data could significantly reduce battery development timelines.
IrO2 as an anodic electrocatalyst for the oxygen evolution reaction (OER) in solid polymer electrolyte (SPE)
electrolysers was synthesised by adapting the Adams fusion method. Optimisation of the IrO2 electrocatalyst was achieved
by varying the synthesis duration (0.5 – 4 hours) and temperature (250 - 500°C). The physical properties of the
electrocatalysts were characterised by scanning electron microscopy (SEM), transmission electron microscopy (TEM) and
x-ray diffraction (XRD). Electrochemical characterisation of the electrocatalysts toward the OER was evaluated by
chronoamperometry (CA). CA analysis revealed the best electrocatalytic activity towards the OER for IrO2 synthesised
for 2 hours at 350oC which displayed a better electrocatalytic activity than the commercial IrO2 electrocatalyst used in this
study. XRD and TEM analyses revealed an increase in crystallinity and average particle size with increasing synthesis
duration and temperature which accounted for the decreasing electrocatalytic activity. At 250°C the formation of an active
IrO2 electrocatalyst was not favoured.
Depositacion electroforetica dentro de campos electricos moduladosMario ML
This document reviews electrophoretic deposition (EPD) under modulated electric fields such as pulsed direct current (PDC) and alternating current (AC). Classical EPD uses continuous direct current which can lead to issues depositing from aqueous suspensions due to water electrolysis. Modulated electric fields can reduce electrolysis and produce more uniform coatings. PDC and AC offer advantages over continuous DC like reducing bubble formation and particle aggregation. While deposition rates may decrease under modulated fields, they allow for depositing biochemical and biological materials in more active states. The document discusses EPD mechanisms and modulated field types, and their applications including in biotechnology.
The document discusses nanoparticles for small molecule electrocatalysis, specifically focusing on oxygen evolution reaction (OER) using Ni-Co hydroxides and oxides. It first provides background on OER and discusses how Co3O4, metal-doped Co3O4, and NiCo2O4 can be used as catalysts. It then outlines the purpose and scope of studying the composition dependence of Ni-Co hydroxides and oxides for OER using stainless steel mesh. The document reviews relevant theory around OER mechanisms and properties of different catalyst materials.
This document summarizes Bing Hsieh's research journey from 1990 to 2014. It covers his work in conducting polymers for OLEDs from 1990-2002, then toner and cartridge recycling from 2003-2007. From 2008-2011 he worked on solid electrolytes and ionic liquids for lithium batteries. From 2011-2014 his focus was on printed organic electronics and graphene supercapacitors. The document provides details on his research into issues with printed transistors, block copolymers as solid electrolytes, dendrite formation in batteries, and preliminary work printing graphene oxide inks for supercapacitors. Diagrams and images supplement the technical descriptions.
The document summarizes research on the electrochemical deposition of lead dioxide nanostructured thin films. Key findings include:
- Lead dioxide nanostructures were successfully deposited on gold-coated substrates by anodic electrochemical deposition using nitric acid and lead chloride as reactants. The morphology was influenced by deposition parameters like potential, temperature, and pH.
- Deposition at higher temperatures (60°C vs room temperature) resulted in faster growth rates and denser nanostructures, as seen by SEM images.
- Both anodic and cathodic deposition were studied. Cathodic deposition allowed formation of different lead oxide phases depending on conditions, while anodic deposition selectively formed PbO2.
- The work provides a
Image reversal resist photolithography of silicon based platinum and silver m...Journal Papers
This document discusses the fabrication of silicon-based platinum and silver microelectrodes using an image reversal photolithography process and lift-off technique. It aims to optimize the process parameters, particularly the resist slope, to reduce defects from metal ears or tears after lift-off. A design of experiments approach was used to analyze factors influencing the resist slope, including spin speed, prebake temperature, exposure times, and develop time. The study found that prebake temperature most significantly impacted the resist slope. Optimization resulted in a resist slope angle of 40.2 degrees, compared to 92.4 degrees previously, allowing for a cleaner lift-off without defects. The fabricated microelectrodes were then tested using cyclic voltammetry
Synthesis and optimisation of ir o2 electrocatalysts by adams fusion method f...materials87
The document describes the synthesis and optimization of iridium dioxide (IrO2) electrocatalysts for oxygen evolution reaction (OER) in solid polymer electrolyte electrolyzers. IrO2 was synthesized using an Adams fusion method by varying synthesis duration (0.5-4 hours) and temperature (250-500°C). Characterization showed that increasing synthesis time and temperature improved crystallinity and increased particle size. Electrochemical testing revealed that IrO2 synthesized for 2 hours at 350°C exhibited the best electrocatalytic activity toward OER compared to a commercial IrO2 catalyst. Higher temperatures and longer times favored larger, more crystalline particles but decreased surface area and activity.
Synthesis and optimisation of ir o2 electrocatalysts by adams fusion method f...sudesh789
This document discusses the synthesis and optimization of iridium dioxide (IrO2) electrocatalysts for use in solid polymer electrolyte electrolyzers through an adaptation of the Adams fusion method. The synthesis duration and temperature were varied to determine their effect on the physical and electrochemical properties of the IrO2 catalysts. X-ray diffraction analysis showed that increasing the synthesis duration and temperature increased the crystallinity and particle size of the IrO2. Chronoamperometry testing revealed that a synthesis of 2 hours at 350°C produced an IrO2 catalyst with better electrocatalytic activity for oxygen evolution than a commercial IrO2 catalyst.
This document describes the fabrication and electrochemical characterization of carbon nanowalls grown on polycrystalline diamond (CNWs-on-diamond) electrodes. CNWs-on-diamond electrodes were synthesized by DC-PECVD and showed lower background current and larger potential window than CNWs-on-silicon electrodes in cyclic voltammetry measurements. SEM and Raman spectroscopy confirmed the growth of carbon nanowalls on the diamond substrate. The CNWs-on-diamond hybrid structure demonstrates potential for use as an electrode in electrochemical applications and biosensors due to the combined properties of diamond and carbon nanowalls.
This document describes research on fabricating a novel graphene electrode embedded with zirconium dioxide nanoparticles for electrochemical capacitors. The electrode showed a maximum specific capacitance of 11.84 F g−1. SEM images showed ions redepositing as agglomerates on the electrode surface after one charge/discharge cycle, accompanied by a decrease in surface area. Electrochemical tests confirmed pseudocapacitive behavior and low resistance. The research aims to investigate how electrolyte ion and active material redeposition affects the electrode's charge distribution ability.
This document describes research on a new chemically modified electrode incorporating zeolite ZSM-5 for determining the drug piroxicam. Specifically:
- A carbon ceramic electrode was modified by incorporating zeolite ZSM-5 using a sol-gel method, creating a carbon ceramic zeolite modified electrode (CCZME).
- The voltammetric behavior of piroxicam at the CCZME was investigated, showing the electrode exhibited catalytic activity toward electrooxidation of piroxicam.
- Under optimized conditions, the CCZME allowed determination of piroxicam using differential pulse voltammetry and hydrodynamic amperometry, with good linear ranges and detection limits.
2014 Journal of Power Sources 247 (2014) 572-578Alexis B. B
The document summarizes research on the durability of a nickelealuminum layered double hydroxide/carbon (NieAl LDH/C) composite as a cathode material in nickel metal hydride batteries. The composite was prepared using a liquid phase deposition method and optimized to contain 19.2 mol% aluminum. Electrochemical testing was conducted over 869 charge/discharge cycles at two different current regimes: 5 mA for 300 cycles in half-cell conditions and 5.8 mA for 569 cycles in battery regime. The composite exhibited good lifespan and stability, maintaining a capacity retention above 380 mAh/g. Cyclic voltammetry and X-ray diffraction analysis showed that the a-Ni
Proton‐functionalized graphitic carbon nitride for efficient metal‐free disin...Journal Papers
This document summarizes a study on using proton-functionalized graphitic carbon nitride (P-CN) as a metal-free photocatalyst for disinfecting Escherichia coli (E. coli) bacteria under low-power light irradiation. P-CN demonstrated 100% disinfection of E. coli within 4 hours under 23W light bulb irradiation. Testing with scavengers showed that hydroxyl radicals (·OH) played a major role in the disinfection process, while superoxide (·O2-) played a minimal role. P-CN exhibited higher disinfection efficiency compared to unmodified graphitic carbon nitride, due to the introduction of protons enhancing conductivity and charge transfer in P-CN. This
This document summarizes research on the electrical conductivity of Ba-Sr-Co-Fe cathode materials for solid oxide fuel cells (SOFCs). Single phase cubic Ba0.5Sr0.5Co1-xFexO3-δ compositions were synthesized via gel combustion and cation complexation routes. Electrical conductivity measurements showed that conductivity initially increased with temperature up to a maximum then decreased, attributed to oxygen loss from the lattice. Fe substitution had little effect on conductivity. While BSCF shows potential as an SOFC cathode, further work is needed to increase conductivity to meet requirements of current IT-SOFCs.
This document summarizes research into enhancing magnesium ion conductivity in secondary batteries through the addition of water to electrolytes. Electrochemical impedance spectroscopy data showed that the addition of water reduced impedance of magnesium ion movement by up to an order of magnitude compared to non-aqueous electrolytes. Further experiments are needed to fully understand how water affects electrolytic, charge transfer, and diffusional impedance and the cycling performance of aqueous electrolytes. Additional electrolyte systems also need to be tested to determine which are most compatible with water.
The document describes the design and application of powder composite electrodes made of Cu, Co, Ni, Pt and Ir for use in electrosynthesis and electroanalysis in alkaline solutions. The electrodes were prepared by mixing 95% metal powder with 5% polyvinyl chloride binder. Characterization showed the electrodes had a rough, porous surface and good electrochemical stability, with higher current densities than metal sheet electrodes. Cyclic voltammetry testing demonstrated the composite electrodes had good stability over multiple cycles for electrooxidation reactions like ethanol oxidation in KOH solution. The composite electrodes are suitable for electrochemistry research applications requiring stable, conductive electrodes.
This document summarizes the electrochemical synthesis and corrosion inhibiting properties of a poly N-methyl aniline coating doped with di-N-propyl malonic acid on stainless steel. Cyclic voltammetry was used to polymerize N-methyl aniline in a solution containing di-N-propyl malonic acid on a stainless steel electrode. An adherent red polymer film was obtained. Electrochemical impedance spectroscopy and potentiodynamic polarization techniques showed that this polymer coating provided excellent corrosion protection of stainless steel in 0.5M sulfuric acid solution, with inhibition efficiencies above 99% as indicated by large increases in charge transfer resistance and decreases in corrosion current density compared to uncoated stainless steel.
This document summarizes an experiment studying the origins of large voltage hysteresis in metal fluoride lithium-ion battery conversion electrodes. Specifically, it examines iron fluoride (FeF3) as a model system using in situ X-ray absorption spectroscopy, transmission electron microscopy, density functional theory calculations, and galvanostatic intermittent titration technique. The results reveal that the phase evolution during charging and discharging is actually symmetrical, with the same intermediate phases forming. However, the spatial distribution of the electrochemically active phases differs due to kinetic effects. This leads to differences in ohmic voltage drop, reaction overpotential, and compositional inhomogeneity, causing the large observed voltage hysteresis which is kinetic rather than thermodynamic in nature
This document summarizes the synthesis, characterization, and evaluation of various IrO2-based binary metal oxide electrocatalysts for the oxygen evolution reaction. IrO2, IrxRu1-xO2, IrxSnx-1O2 and IrxTax-1O2 (where x is between 1 and 0.7) were synthesized via an adapted Adams fusion method. X-ray diffraction and electron microscopy showed the materials formed nanocrystalline solid solutions. Electrochemical testing found that adding RuO2, SnO2, or Ta2O5 to IrO2 improved its catalytic performance for oxygen evolution. Specifically, Ir0.7Ru0.3O2 exhibited the best
This document summarizes research on using electrodeposited manganese dioxide (MnO2) coatings on porous carbon substrates for capacitive deionization (CDI) applications. Two carbon substrates with different surface areas and morphologies were coated with MnO2 using galvanostatic and cyclic voltammetric deposition. Characterization of the coated electrodes found mixed MnO2 phases present. Testing in half-cell configurations showed that maximum ion uptake per mass was not necessarily optimal for practical CDI applications, where performance per electrode area is more important. The results suggest the structure and deposition method can impact how effectively the electrode volume participates in ion removal reactions.
This document describes how synchrotron-based X-ray spectroscopy techniques like XANES and STXM can provide insights into structure-performance relationships in battery materials to enable faster optimization. These techniques allow mapping of local chemistry, bonding structure, and phase distributions. Studies have shown how surface coatings and composite designs can influence properties like conductivity and stability. Chemical mapping of electrodes also revealed non-uniform reactions related to "hot spots" that correlate with performance. Faster screening of materials and correlation of structural properties with electrochemical data could significantly reduce battery development timelines.
IrO2 as an anodic electrocatalyst for the oxygen evolution reaction (OER) in solid polymer electrolyte (SPE)
electrolysers was synthesised by adapting the Adams fusion method. Optimisation of the IrO2 electrocatalyst was achieved
by varying the synthesis duration (0.5 – 4 hours) and temperature (250 - 500°C). The physical properties of the
electrocatalysts were characterised by scanning electron microscopy (SEM), transmission electron microscopy (TEM) and
x-ray diffraction (XRD). Electrochemical characterisation of the electrocatalysts toward the OER was evaluated by
chronoamperometry (CA). CA analysis revealed the best electrocatalytic activity towards the OER for IrO2 synthesised
for 2 hours at 350oC which displayed a better electrocatalytic activity than the commercial IrO2 electrocatalyst used in this
study. XRD and TEM analyses revealed an increase in crystallinity and average particle size with increasing synthesis
duration and temperature which accounted for the decreasing electrocatalytic activity. At 250°C the formation of an active
IrO2 electrocatalyst was not favoured.
Depositacion electroforetica dentro de campos electricos moduladosMario ML
This document reviews electrophoretic deposition (EPD) under modulated electric fields such as pulsed direct current (PDC) and alternating current (AC). Classical EPD uses continuous direct current which can lead to issues depositing from aqueous suspensions due to water electrolysis. Modulated electric fields can reduce electrolysis and produce more uniform coatings. PDC and AC offer advantages over continuous DC like reducing bubble formation and particle aggregation. While deposition rates may decrease under modulated fields, they allow for depositing biochemical and biological materials in more active states. The document discusses EPD mechanisms and modulated field types, and their applications including in biotechnology.
The document discusses nanoparticles for small molecule electrocatalysis, specifically focusing on oxygen evolution reaction (OER) using Ni-Co hydroxides and oxides. It first provides background on OER and discusses how Co3O4, metal-doped Co3O4, and NiCo2O4 can be used as catalysts. It then outlines the purpose and scope of studying the composition dependence of Ni-Co hydroxides and oxides for OER using stainless steel mesh. The document reviews relevant theory around OER mechanisms and properties of different catalyst materials.
This document summarizes Bing Hsieh's research journey from 1990 to 2014. It covers his work in conducting polymers for OLEDs from 1990-2002, then toner and cartridge recycling from 2003-2007. From 2008-2011 he worked on solid electrolytes and ionic liquids for lithium batteries. From 2011-2014 his focus was on printed organic electronics and graphene supercapacitors. The document provides details on his research into issues with printed transistors, block copolymers as solid electrolytes, dendrite formation in batteries, and preliminary work printing graphene oxide inks for supercapacitors. Diagrams and images supplement the technical descriptions.
The document summarizes research on the electrochemical deposition of lead dioxide nanostructured thin films. Key findings include:
- Lead dioxide nanostructures were successfully deposited on gold-coated substrates by anodic electrochemical deposition using nitric acid and lead chloride as reactants. The morphology was influenced by deposition parameters like potential, temperature, and pH.
- Deposition at higher temperatures (60°C vs room temperature) resulted in faster growth rates and denser nanostructures, as seen by SEM images.
- Both anodic and cathodic deposition were studied. Cathodic deposition allowed formation of different lead oxide phases depending on conditions, while anodic deposition selectively formed PbO2.
- The work provides a
Image reversal resist photolithography of silicon based platinum and silver m...Journal Papers
This document discusses the fabrication of silicon-based platinum and silver microelectrodes using an image reversal photolithography process and lift-off technique. It aims to optimize the process parameters, particularly the resist slope, to reduce defects from metal ears or tears after lift-off. A design of experiments approach was used to analyze factors influencing the resist slope, including spin speed, prebake temperature, exposure times, and develop time. The study found that prebake temperature most significantly impacted the resist slope. Optimization resulted in a resist slope angle of 40.2 degrees, compared to 92.4 degrees previously, allowing for a cleaner lift-off without defects. The fabricated microelectrodes were then tested using cyclic voltammetry
Synthesis and optimisation of ir o2 electrocatalysts by adams fusion method f...materials87
The document describes the synthesis and optimization of iridium dioxide (IrO2) electrocatalysts for oxygen evolution reaction (OER) in solid polymer electrolyte electrolyzers. IrO2 was synthesized using an Adams fusion method by varying synthesis duration (0.5-4 hours) and temperature (250-500°C). Characterization showed that increasing synthesis time and temperature improved crystallinity and increased particle size. Electrochemical testing revealed that IrO2 synthesized for 2 hours at 350°C exhibited the best electrocatalytic activity toward OER compared to a commercial IrO2 catalyst. Higher temperatures and longer times favored larger, more crystalline particles but decreased surface area and activity.
Synthesis and optimisation of ir o2 electrocatalysts by adams fusion method f...sudesh789
This document discusses the synthesis and optimization of iridium dioxide (IrO2) electrocatalysts for use in solid polymer electrolyte electrolyzers through an adaptation of the Adams fusion method. The synthesis duration and temperature were varied to determine their effect on the physical and electrochemical properties of the IrO2 catalysts. X-ray diffraction analysis showed that increasing the synthesis duration and temperature increased the crystallinity and particle size of the IrO2. Chronoamperometry testing revealed that a synthesis of 2 hours at 350°C produced an IrO2 catalyst with better electrocatalytic activity for oxygen evolution than a commercial IrO2 catalyst.
This document describes the fabrication and electrochemical characterization of carbon nanowalls grown on polycrystalline diamond (CNWs-on-diamond) electrodes. CNWs-on-diamond electrodes were synthesized by DC-PECVD and showed lower background current and larger potential window than CNWs-on-silicon electrodes in cyclic voltammetry measurements. SEM and Raman spectroscopy confirmed the growth of carbon nanowalls on the diamond substrate. The CNWs-on-diamond hybrid structure demonstrates potential for use as an electrode in electrochemical applications and biosensors due to the combined properties of diamond and carbon nanowalls.
This document describes research on fabricating a novel graphene electrode embedded with zirconium dioxide nanoparticles for electrochemical capacitors. The electrode showed a maximum specific capacitance of 11.84 F g−1. SEM images showed ions redepositing as agglomerates on the electrode surface after one charge/discharge cycle, accompanied by a decrease in surface area. Electrochemical tests confirmed pseudocapacitive behavior and low resistance. The research aims to investigate how electrolyte ion and active material redeposition affects the electrode's charge distribution ability.
This document describes research on a new chemically modified electrode incorporating zeolite ZSM-5 for determining the drug piroxicam. Specifically:
- A carbon ceramic electrode was modified by incorporating zeolite ZSM-5 using a sol-gel method, creating a carbon ceramic zeolite modified electrode (CCZME).
- The voltammetric behavior of piroxicam at the CCZME was investigated, showing the electrode exhibited catalytic activity toward electrooxidation of piroxicam.
- Under optimized conditions, the CCZME allowed determination of piroxicam using differential pulse voltammetry and hydrodynamic amperometry, with good linear ranges and detection limits.
2014 Journal of Power Sources 247 (2014) 572-578Alexis B. B
The document summarizes research on the durability of a nickelealuminum layered double hydroxide/carbon (NieAl LDH/C) composite as a cathode material in nickel metal hydride batteries. The composite was prepared using a liquid phase deposition method and optimized to contain 19.2 mol% aluminum. Electrochemical testing was conducted over 869 charge/discharge cycles at two different current regimes: 5 mA for 300 cycles in half-cell conditions and 5.8 mA for 569 cycles in battery regime. The composite exhibited good lifespan and stability, maintaining a capacity retention above 380 mAh/g. Cyclic voltammetry and X-ray diffraction analysis showed that the a-Ni
Proton‐functionalized graphitic carbon nitride for efficient metal‐free disin...Journal Papers
This document summarizes a study on using proton-functionalized graphitic carbon nitride (P-CN) as a metal-free photocatalyst for disinfecting Escherichia coli (E. coli) bacteria under low-power light irradiation. P-CN demonstrated 100% disinfection of E. coli within 4 hours under 23W light bulb irradiation. Testing with scavengers showed that hydroxyl radicals (·OH) played a major role in the disinfection process, while superoxide (·O2-) played a minimal role. P-CN exhibited higher disinfection efficiency compared to unmodified graphitic carbon nitride, due to the introduction of protons enhancing conductivity and charge transfer in P-CN. This
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1. Journal of The Electrochemical
Society
OPEN ACCESS
Increased Disorder at Graphite Particle Edges Revealed by Multi-length
Scale Characterization of Anodes from Fast-Charged Lithium-Ion Cells
To cite this article: Saran Pidaparthy et al 2021 J. Electrochem. Soc. 168 100509
View the article online for updates and enhancements.
This content was downloaded from IP address 186.211.111.10 on 07/12/2021 at 13:16
3. plating. Hence, an in-depth understanding of changes in the graphite
particles subjected to fast charging is crucial for the development of
materials that enable intercalation and mitigate deterioration of cell
performance during the electrochemical cycling.
In this work, we examine the morphological, chemical, and
structural changes to the graphite materials and electrodes, using a
suite of electrochemical and physicochemical techniques. The
characterization was performed across multiple length-scales on
as-prepared electrodes and on numerous electrodes harvested from
cycled cells; only representative data from the various techniques
are shown to highlight key changes that result from the cycling. The
data in this manuscript are from an as-prepared graphite (Gr-AP)
electrode that was never exposed to the electrolyte, graphite
electrode with no plating (Gr-NP) harvested from a cell after a
few low-rate cycles and graphite electrode with lithium plating (Gr-
LP) harvested from a fast-charged cell. For purposes of clarity and
contrast, we show only the Gr-AP and Gr-LP data in the main text;
data from the Gr-NP sample are included in the Supporting
Information (SI). Note that all Tables and Figures in the SI are
marked with the designator S, as in Fig. S1 (available online at
stacks.iop.org/JES/168/100509/mmedia).
We start by describing electrochemical tests, conducted on full
cells with LiNi0.5Co0.2Mn0.3O2 (NCM523) cathodes and graphite
(Gr) anodes, which include charging rates up to 6 C (here, 1 C is the
current needed to fully discharge the cell in 1 h). Following this, we
compare electrochemical behavior of the Gr-AP electrode with that
of the Gr-LP electrode. Then, after presenting high-resolution X-ray
diffraction (XRD) data from the materials, we show microscopy and
spectroscopy results obtained on electrode cross-sections fabricated
via ion milling and on sections prepared with a focused ion beam
(FIB). At the bulk-scale, we use scanning electron microscopy
(SEM) and energy dispersive X-ray spectroscopy (EDS) to probe the
morphological and chemical changes in cross-sections of the
graphite anode. At the nano- to atomic-scale, we rely on both
conventional transmission electron microscopy (TEM) and scanning
TEM (STEM) to reveal local structural disorder and chemical
variation within individual graphite particle sections through a
combination of high-resolution imaging, EDS, and scanning electron
nanodiffraction (SEND). Our investigations reveal that anodes from
the fast-charged cells have lower capacity, present a sloping voltage
profile, display an increase in thickness and show greater lattice
disorder in localized areas near the graphite particle edges.
Experimental Section
Electrode materials, cell assembly and electrochemical
testing.—In the NCM523//Gr cells, the positive electrode has a
71 μm thick coating, with 90 wt% Li(Ni0.5Co0.2Mn0.3)O2 (Toda),
5 wt% C45 carbon (Timcal) and 5 wt% PVDF binder (KF-9300,
Kureha), on a 20 μm thick Al current collector.10
The negative
electrode has a 70 μm thick coating, with ∼92 wt% SLC1506T
graphite (Superior Graphite), 2 wt% C45 carbon and 6 wt% PVDF
binder, on a 10 μm thick Cu current collector. The electrolyte (aka
Gen 2, purchased from Tomiyama) is a solution of 1.2 M lithium
hexafluorophosphate (LiPF6) salt dissolved in a 3:7 w/w solvent
mixture of ethylene carbonate (EC) and ethyl methyl carbonate
(EMC). Celgard 2320 is the separator between the electrodes. Before
cell assembly, the electrodes and separator are dried in vacuum
ovens set at 120 °C and 70 °C, respectively. The 3-electrode
measurements are conducted in custom-made stainless-steel cells,
which are assembled and tested inside an Ar-atmosphere glove box.
The reference electrode (RE) probe is placed between two separa-
tors, sandwiched between 20.3 cm2
disks of the oxide-positive and
graphite-negative electrodes (Fig. 1): the RE consists of a copper
wire (25 μm diameter) with a thin layer of Li metal plated on the
exposed tip.9
Electrochemical cycling is typically conducted at 30 °C with a
Maccor Model 2400 cycler. The Gr-NP electrode is from a cell that
experienced two C/10 and five C/2 cycles between 3 and 4.2 V at 30
°C. The Gr-LP electrode was harvested from a cell that experienced
multiple sequences of an “escalating C-rate” protocol (Fig. 1). To
accelerate cell aging, three of the sequences were at 30 °C, one at 40
°C and one at 50 °C. Including the initial cycles and periodic
reference performance tests (C/25 rate), the cell experienced a total
of 50 cycles; of these, 25 charge segments were at rates of 2 C and
above.
After cycling, cells were discharged to (and held for 10 h at) 3 V
before disassembly in an argon-atmosphere glove box. Various
diagnostic tests were conducted on the harvested cell materials to
determine the effect of cycling on the graphite material. For the
electrochemical tests, 2032-type coin cells were assembled with 1.6
cm2
area harvested-electrode samples, lithium metal counter elec-
trode, fresh Celgard 2320 separator, and fresh Gen2 electrolyte.
Cross-section polishing.—Cross-sections of the graphite elec-
trode samples were prepared via argon ion milling using the Gatan
Model 685.O Precision Etching Coating System II (PECS II). The
electrode was gently handled with metal tweezers and cut with sharp
metal scissors to leave at least one flat-side of ∼5 mm; all metal
tools were cleaned using an ethanol and acetone rinse prior to
handling the electrode. The cut electrode was mounted onto the
PECS II sample blade (Gatan, Product No. 693.08500) using fast-
drying silver paint (Ted Pella, Product No. 16040–30) and adjusted
with a micrometer to ensure ∼200 μm overhang of the flat-side of
the electrode from the top of the sample blade. Once the electrode
was secure on the blade, the electrode/blade polishing sample was
placed onto the cross-section specimen mount (Gatan, Product No.
Figure 1. In this escalating C-rate experiment, the NCM523//Gr cell is
charged with increasing currents to a fixed capacity of 87 mAh g−1
. Each
charge is followed by 1 h rest and C/5 discharge to 3 V and a hold. The cell
voltage changes during the cycles are shown in (a), while the graphite-
electrode potential changes are shown in (b). Lithium plating on the graphite
particles becomes likely when the electrode potential dips below 0 V vs
Li/Li+
; this Li-plating condition (LPC) is indicated by the dotted line in (b).
In the above experiment, Li-plating on the graphite electrode becomes likely
when the charge rate exceeds ∼2 C.
Journal of The Electrochemical Society, 2021 168 100509
4. 685.08540) and loaded into the PECS II instrument. After the sample
was loaded, the instrument was set to “Etch by Time” with a “Single
Modulation” etching condition, a Gun Tilt angle of 0° for both ion
guns, and a rotation rate of 0.5 RPM. The ion milling was performed
in two stages: first, a high-voltage milling at 8 kV (with current
readings in the range 20–40 μA) that was run for 4 h to create a
rough cross-section; second, a low-voltage milling at 4 kV (with
current readings of 7–15 μA) that ran for 30 min to apply a low-kV
fine polishing.
Synchrotron powder diffraction.—Powder diffraction data were
collected at beamline 11-BM of the Advanced Photon Source,
Argonne National Laboratory. Coatings from the as-prepared
electrodes and cycled electrodes, scraped of the copper current
collectors, were loaded into sealed capillaries for examination. An
X-ray wavelength of 0.41283 Å was used to collect the diffraction
data, over an angular range from –6.0° to 28.0° with a step size of
0.001° and a time per step of 0.1 s.
Scanning electron microscopy and energy-dispersive X-ray
spectroscopy.—Both imaging and elemental examinations were
performed using a JEOL 7000 F analytical SEM. The electrode
samples were prepared in the following ways: (1) for top-down
imaging, a small portion of the electrode is mounted onto a flat
sample holder via carbon tape; (2) for cross-sectional imaging, the
samples prepared by the PECS II ion milling are loaded onto a
standard cross-section specimen mount designed for the SEM. For
the SEM imaging, the instrument was set to 7 kV and operated under
secondary electron imaging mode with a medium probe current of
∼0.3 nA. For EDS acquisition, the sample was aligned to an optimal
working distance of 10 mm and the probe current was adjusted to a
setting of ∼15 nA. The mapping data were acquired using the
ThermoFisher NSS 2.0 software using its “Spectral Imaging” mode.
The datasets were summed for 150 frames, each acquired for 10 s
per frame with a 50 μs dwell time. The mapping data are reported as
counts per element and the quantification was performed by the
software automatically using a built-in database and algorithm based
on the standard phi-rho-z method. The line profile data for the cross-
section samples are acquired using the “X-ray Linescans” mode with
a single scan with 50 points from the bottom to the top of the anode
with a dwell time of 10 s per point. Line profile data are further
binned for every 5 μm step.
Focused-ion beam milling.—Samples for nano- to atomic-scale
electron imaging and diffraction were prepared with a ThermoFisher
Scientific Scios 2 FIB-SEM. The electrodes were cut with sharp
metal scissors and mounted onto a flat sample holder via carbon tape
and loaded into the instrument. The cross-section samples were
selected from areas near the electrode surface and prepared via
standard focused-ion beam lift-out procedure provided by
ThermoFisher Scientific onboard user guidance (included with the
instrument software). The samples were mounted onto one of four
posts of a PELCO FIB lift-out TEM copper grid and thinned to a
final thickness around 100–200 nm.
Transmission electron microscopy.—Transmission electron mi-
croscopy (TEM) was performed on a Hitachi 9500 TEM equipped
with a LaB6 emitter and operated at 300 kV. Image acquisition was
done using the K2 direct electron detector operated in counting
mode.
Scanning transmission electron microscopy, energy dispersive
X-ray spectroscopy, and scanning electron nanodiffraction.—
Nano- and atomic-scale imaging, chemical analysis, diffraction
data were acquired using the ThermoFisher Scientific Titan
Themis Z STEM equipped with a Schottky field emission gun
operated at 300 kV accelerating voltage. The electrode sample was
loaded into a standard double-tilt holder and, during operation, tilted
close to the 100
〈 〉 zone axis or the 210
〈 〉 zone axis (with respect to
the Graphite-2H phase), as both orientations allowed us to track the
graphite interplanar spacing in both imaging and diffraction modes.
Imaging was performed at 15–30 pA screen current with a
convergence angle of 18.0 mrad and acquired using a high-angle
annular dark field (HAADF) detector. The EDS acquisition was
performed using the above mentioned imaging conditions via the
Velox software (ThermoFisher Scientific) with an acquisition time
of ∼1 h using a continuous scan with a frame time of ∼1 s. SEND
data were collected in microprobe STEM (μP STEM) mode with a
convergence angle of 0.46 mrad. The SEND probe size is 1.7–-
1.8 nm at full-width half maximum. The diffraction datasets were
acquired at a camera length of 145 mm over a real-space scan area of
Figure 2. (a) Capacity-potential profiles of the graphite electrode from a NCM532//Gr cell with a reference electrode. The lithiation profiles are at the indicated
rates; the 0.2 C rate delithiation profile shown is after lithiation at the 2 C rate followed by a 1 h rest. (b) Profiles for as-prepared (black) and harvested electrodes
(red); the latter are from a cell subjected to multiple “escalating C-rate” cycling. The as-prepared electrode data are at C/100 rate, whereas the harvested electrode
plots are at both C/100 (solid) and C/10 (dashed) rates. In both (a) and (b), the specific capacities are obtained by dividing the cell capacity (mAh) by the graphite
weight (gGr
−1
) in the anode.
Journal of The Electrochemical Society, 2021 168 100509
5. 150 nm × 150 nm using 75 × 75 total steps with drift correction
performed after each line acquisition.
Results and Discussion
Electrochemical cycling.—Capacity-potential profiles of the
graphite electrode from a NCM523//Gr cell are shown in Fig. 2a.
The graphite is lithiated and delithiated during cell charge and
discharge, respectively. At low lithiation rates (<C/5), the inter-
calation progresses in distinctive stages seen as plateaus in the plots;
the Li+
ions fill spaces between the carbon sheets forming distinct
LixC6 phases (x = 0.22, 0.33, 0.5, 1). At higher lithiation rates
(⩾1 C), the plateaus are not distinct as intercalation occurs under far-
from-equilibrium conditions. Multiple mixed and strained phases are
probably formed so that the profile appears continuous, rather than
staged; note that LixC6 phases of various compositions have been
reported in the research literature.25–29
During the C/5 delithiation,
staging plateaus are always observed, regardless of the behavior
during the preceding lithiation cycle (Fig. 2a). We observed this
difference between the lithiation and delithiation behavior during
operando XRD studies; therein, we attributed the blurring of phase
boundaries during lithiation to lattice strain and the formation of
distinct LixC6 phases during delithiation to abrupt separation from
oversaturated solid solutions.18
As indicated earlier, the cells in this study were subjected to
multiple applications of the escalating C-rate protocol. Capacity-
voltage profiles from a representative cell, before and after the
protocol, are shown in Fig. S1. The electrochemical cycling causes a
significant loss in cell capacity. The Li+
ions are lost to the solid
electrolyte interphase (SEI) formed during electrolyte reduction on
the graphite electrode and to the dead lithium that accumulates in the
electrode because of repeated excursions below the Li-plating
potential (Fig. 1b).22,30
Figure 2b compares plots from a lithium-plated graphite elec-
trode (Gr-LP) harvested from the cell in Fig. S1, with plots from an
as-prepared graphite (Gr-AP) electrode. The lithiation profile of the
Gr-AP electrode (at C/100 rate) displays distinctive plateaus around
210, 117 and 83 mV vs Li/Li+
. These plateaus are also very distinct
in the C/10 rate lithiation data (not shown), though they occur at
slightly lower potentials because of polarization arising from
electrode impedance. In contrast, the plateaus are not distinct in
the lithiation profile of the Gr-LP electrode, even at a C/100 rate.
The capacity of this aged-harvested electrode (326 mAh g−1
) is also
smaller than that of the as-prepared electrode (357 mAh g−1
). The C/
10 lithiation data of this Gr-LP electrode resembles the 2 C graphite-
lithiation data in Fig. 2a; the sloped profile, the barely visible staging
plateaus and the lower capacity all suggest changes in the graphite
particles that alter lithium insertion into the material. Interestingly,
the staging plateaus are visible both in the C/100 and C/10
delithiation profiles of the harvested material, which is consistent
with the distinct differences between the lithium insertion and
extraction processes mentioned earlier.
The theoretical capacity of graphite is 372 mAh g−1
but the Gr-
AP electrode yields only 357 mAh g−1
even at very low rates. The
underlying reason for this smaller capacity is the inherent turbos-
tratic stacking disorder in the commercial graphite, which limits Li+
ion intercalation into the material.31,32
Fast-charging appears to
create additional disorder, further decreasing capacity. Moreover, the
increased structure-disorder increases the number of electronically
and geometrically non-equivalent sites for Li-intercalation causing
the sloping lithiation profile of the Gr-LP even at extremely low
rates.33
In contrast, most of the sites in Gr-AP are thermodynami-
cally equivalent for Li+
intercalation, thereby producing the
observed staging behavior at low lithiation rates.
Ensemble phase analysis via powder X-ray diffraction.—We
evaluated the bulk-scale structure and ensemble lattice spacing of the
graphite anode coatings using synchrotron X-ray diffraction.
Diffraction patterns obtained on the Gr-AP and Gr-LP electrodes
are shown in Figs 3a and 3b, respectively. Figure 3a shows that the
as-prepared electrode contains two distinct graphite phases: the 2H
phase (marked as #) and the 3 R phase (marked as *). The 3 R phase
is not observed in the Gr-LP electrode pattern (Fig. 3b); we postulate
that this phase transforms into the more stable 2H form during
repeated Li+
insertion into and extraction from the graphite, which
requires gliding of the graphene planes as mentioned in the
Introduction.
We calculated the graphite interplanar d-spacing from the strong
diffraction peak at ∼1.87 Å–1
, which corresponds to the (002)
reflection for the Graphite-2H phase or the (003) reflection for the
Graphite-3R phase. For both Gr-AP and Gr-LP electrode samples we
obtained d 3.356 Å,
interplanar
〈 〉 ≅ which indicates that the latter
sample is fully delithiated and that the amount of residual Li+
ions, within the graphite of the fully discharged cell, is negligible.
However, diffraction pattern of the Gr-LP sample (Fig. 3b) shows
new peaks at ∼2.70 Å–1
and ∼4.40 Å–1
, which arise from lithium
fluoride (LiF) (marked as ♢). The presence of LiF was confirmed by
selected area electron diffraction (SAED) data on a FIB cross-
section prepared from the top surface of the Gr-LP sample (Fig. S2).
LiF is known to be a component of the graphite SEI and forms
through decomposition reactions of the LiPF6 salt.34,35
There was no
evidence of other known SEI phases in the Gr-LP pattern, which
indicates that these compounds are either fully amorphous or lack
the long-range order needed to coherently scatter the X-ray beam.
SEM imaging and compositional analysis.—Figure 4 reveals the
dramatic change to the graphite anode surface after being subjected
to cycling under the fast-charge, lithium-plating condition. Figure 4a
shows a photograph of the Gr-AP sample (cut to a 14.2 mm
diameter); the EDS data in Figs. 4b and S3 indicate that the coating
contains only C and F, reflecting the graphite, C45 and PVDF
Figure 3. Synchrotron powder diffraction data from the following graphite
electrodes: (a) as-prepared (Gr-AP) and (b) cycled with lithium plating (Gr-
LP). The Bragg reflections are indexed according to JCPDS cards 01–071-
–3739 for Graphite-2H, 01–075–2078 for Graphite-3R, and 01–071–3743 for
LiF. The phases are marked using the following symbols: # for Graphite-2H,
* for Graphite-3R, and ♢ for LiF.
Journal of The Electrochemical Society, 2021 168 100509
6. materials used for electrode preparation. Figure 4c is an SEM image
of the Gr-AP sample surface at 2k × magnification to illustrate that
the electrode is comprised of densely packed, potato-shaped graphite
particles up to 10 μm in size.
SEM and EDS data from the Gr-NP electrode are displayed in
Fig. S4. The graphite particles appear unchanged by the low-rate
cycles; the elemental analyses reveal the presence of C, O, F and P,
which arise from electrolyte decomposition products and residues on
the electrode. By contrast, Fig. 4d shows a photograph of the Gr-LP
sample (cut to 14.2 mm diameter) with an uneven white-coloration
across the surface; the average elemental composition (in wt%) of
the electrode surface (Fig. 4e) is 21% O, 49% F, 27% P and 3% C.
Figure 4f shows the surface morphology of the Gr-LP sample at 2k
× magnification; in this image, there is complete coverage of the
graphite particles by products formed by reactions of the plated
lithium with the electrolyte (also see Fig. S5).
To further determine extent of changes, we examined the
electrodes in cross-section to study morphological and elemental
characteristics throughout their depth (see Figs. 5, S6, S7 and S8).
Details of the coating thickness calculations are provided in Section
4 of the SI and Fig. S9. Figure 5a shows that the Gr-AP sample has
an average coating thickness of 76.6 μm. Figure 5b shows a FIB
cross-section of a typical graphite particle, revealing the presence of
internal pores. The elemental composition across the electrode
thickness was measured via EDS line-scans. For the Gr-AP sample,
the carbon signal, which arises predominantly from the graphite,
measures an average of 97 wt% across the depth of the coating layer
above the copper current collector, while the fluorine signal, which
arises from PVDF binder, measures an average of 3 wt% (Figs. 5c
S6). Cross-sections of the Gr-NP electrode (Fig. S7) reveal an
average coating thickness of 78.1 μm, which is about 2% greater
than that of the Gr-AP electrode. Irreversible increases in graphite
electrode thickness have been noted previously in electrochemical
dilatometry studies; these typically range from 2%–5% after a few
cycles.36–38
EDS scans reveal carbon, oxygen, fluorine and phos-
phorous signals, distributed across the electrode. These elements are
from the electrolyte decomposition products that accumulate in the
electrode.
By contrast, the Gr-LP electrode has an average coating thickness
of 91.3 μm, which does not include the ∼15–20 μm thick layer
resulting from lithium plating on the anode surface (see Fig. 5d).
This coating thickness is 19.2% and 16.9% greater than that of the
Gr-AP and Gr-NP electrodes, respectively. We attribute this
electrode thickness increase to SEI buildup in the electrode pores
and rearrangement of graphite particles during the electrochemical
cycling. The process is exacerbated by Li plating and subsequent
electrolyte reduction, which increases the amount of SEI. This SEI
buildup is also seen on individual graphite particles, on the exterior
surfaces and in the internal pores (Fig. 5e). Moreover, EDS line-
scans show that the elemental composition is non-uniform across the
electrode thickness (Figs. 5f and S8). The topmost portion, which
has no graphite, contains mainly oxygen, fluorine and phosphorus
indicating that the products of lithium plating are mainly inorganic—
for example, LiF and lithium (oxy)fluoro-phosphate compounds.
Below this portion, in the electrode coating, carbon is the dominant
element but we also observe an abundance of fluorine and
phosphorus, possibly (oxy)fluoro-phosphate compounds resulting
from hydrolysis reactions of the electrolyte salt.39,40
STEM-EDS compositional analysis.—Using STEM-EDS, we
further show that the (oxy)fluoro-phosphate compounds only coat
the surface of the graphite particle and do not penetrate the bulk.
Figure 4. Comparison of the anode surface morphology and composition. The as-prepared graphite (Gr-AP) anode surface details are elucidated via: (a)
photograph at 1x magnification, (b) EDS elemental composition, in weight percent, and (c) SEM image at 2000 × magnification. Similarly, the Gr-LP anode
surface details are elucidated via: (d) photograph at 1x magnification, (e) EDS elemental composition in weight percent, and (f) SEM image at 2000 ×
magnification. Scale bars in (a) and (d): 5 mm.
Journal of The Electrochemical Society, 2021 168 100509
7. Figure 6a shows a survey of the Gr-LP particle section (prepared by
FIB) with EDS elemental analysis performed in the marked region,
which is magnified in Fig. 6b.
We reveal compositional heterogeneity by comparing the local
EDS spectra from graphite edges (marked as Area #1 and Area #3)
to the graphite center (marked as Area #2) shown in Fig. 6c(i). The
spectra from Area #1 and Area #3 show signals for O, F, and P in
addition to the signal from C. However, Area #2 only shows C
signature, which indicates a lack of (oxy)fluoro-phosphate com-
pounds in the graphite interior. Figure 6c(ii) shows the spectra
corresponding to the whole area in Fig. 6b. The elemental maps
(Fig. 6d) further confirm the spatial heterogeneity between carbon
and the (oxy)fluoro-phosphates; the C K signal appears only in the
graphite bulk, while the O, F, and P signals appear on the graphite
band edges. Moreover, the O, F, and P signals appear in the same
Figure 5. SEM imaging and elemental mapping of the electrode cross-sections. The as-prepared graphite (Gr-AP) sample details are elucidated via (a) SEM
image of the electrode cross-section, (b) SEM image of an individual particle section, and (c) EDS elemental data acquired across the thickness from bottom of
the current collector to the top of the coating surface—see white arrow in (a). Similarly, the lithium-plated graphite electrode (Gr-LP) sample details are
elucidated via (d) SEM image of the electrode cross-section, (e) SEM image of an individual particle section, and (f) EDS elemental data acquired across the
thickness depth from bottom of the current collector to the top surface—see white arrow in (d). Scale bars: (a), (d) are 25 μm; (b), (e) are 2 μm.
Journal of The Electrochemical Society, 2021 168 100509
8. locations across the EDS maps. Additional EDS maps for different
regions of the Gr-LP electrodes are provided in Figs. S10 and S11.
The above observations indicate that the SEI only accumulates on
the graphite particle edges and does not penetrate the bulk material.
Electrolyte solvent co-intercalation would cause excessive strain
and/or damage to the host graphite. We do not see such damage in
the bulk graphite and, therefore, do not anticipate extensive
electrolyte penetration. We also observe that smaller pores within
the graphite yield weaker electrolyte residue signatures compared to
the larger pores. The electrolyte is known to penetrate the intra-
particle pores during electrochemical cycling.41
Larger pores pro-
vide easier access to the electrolyte; hence, more SEI would be
expected to accumulate in the larger pores than in the smaller pores.
Revealing localized disorder via high-resolution TEM.—High-
resolution TEM (HRTEM) data reveal the nature of the turbostratic
disorder that manifests in graphite particles at the lattice-level
(Fig. 7). Figure 7a, spanning a 50 nm × 50 nm field-of-view, shows
that the Gr-AP sample has straight and uniform graphite lattice
fringes corresponding to the constituent graphene planes. From this
image, we can qualitatively assess the degree of uniformity by
studying Region 1 (Fig. 7b) and Region 2 (Fig. 7c). The lattice-
fringe spacing, measured directly from the images of both regions, is
∼0.33 nm, which is consistent with the interplanar d-spacing of
graphite determined by XRD.
Fast-Fourier Transform (FFT) analysis is useful for quantifying
geometric and periodic patterns in electron microscopy images.42,43
The localized Fast-Fourier Transform (FFT) of the Region 1 and
Region 2 images are shown in Figs. 7d and 7e, respectively;
information to explain features observed in the HRTEM images is
contained in Section 6 and Fig. S12 of the SI. Briefly, the FFT of a
real-space intensity image (with distances x in nm) yields a
representative image in the corresponding spatial frequency domain
(with distances x
1/ in nm–1
).42,43
By applying FFT to the image in
Fig. 7b, the periodic stripe pattern of the graphite lattice (with
measured spacing 0.33 nm
∼ ) is mapped to points in Fig. 7d
corresponding to the frequency of the lattice spacing (i.e.,
1 0.33 nm 1
∼ / − from the center). Moreover, because the intensity
variation of the fringes lies along the direction normal to the fringes
in Fig. 7b (specified as direction 1 on the shown axis), the
corresponding spots in the frequency domain of Fig. 7d lie along
this same direction. The higher frequency spots in Fig. 7d that lie
along the same line (direction 1) correspond to additional harmonics
(i.e., n 1 0.33 nm 1
× ∼ / − where n is an integer) of the real-space
lattice; observation of such harmonics implies that the lattice is
relatively straight and uniform (i.e., ordered) within Region 1. In the
specified direction 2 (normal to direction 1), spots are occasionally
observed within the lattice fringes (Fig. 7b); these spots likely arise
from atomic columns within the graphite and the distance between
them correspond to the spacing between such columns. Similar
observations can be made for the Region 2 image (Fig. 7c) and its
corresponding FFT (Fig. 7e), thereby illustrating spatial uniformity
of the Gr-AP lattice.
Figure 6. STEM-EDS of a graphite particle cross-section from the Gr-LP sample. HAADF-STEM images of (a) graphite particle section and (b) a close-up of
the area where the EDS maps were acquired. (c) EDS spectra represented by the following regions: (i) from selected areas 1 (top-edge of graphite edge), 2 (center
of graphite band), and 3 (bottom-edge of graphite band) as marked in (b); (ii) whole-area EDS spectrum. (d) EDS maps of (i) C, (ii) O, (iii) F, and (iv) P signals.
Scale bars: (a) 2 μm, (b) 100 nm, (d) (i)–(iv) 50 nm.
Journal of The Electrochemical Society, 2021 168 100509
9. By contrast, HRTEM images of the Gr-LP sample (Fig. 7f), show
significant nonuniformity. This nonuniformity is illustrated by
example from the magnified Region 1 (Fig. 7g) and Region 2
(Fig. 7h); localized FFTs of Regions 1 and 2 are shown in Figs. 7i
and 7j, respectively. Region 1, which is taken near the surface of an
internal pore within a graphite particle, is different from both
Regions 1 and 2 of the Gr-AP sample. From Fig. 7g, we find that
the Gr-LP lattice of Region 1 appears wavy; based on Fig. 7f, we
estimate that this waviness extends about 20 nm into the graphite
bulk. The FFT of Region 1 (Fig. 7i) confirms lattice disorder in the
following ways: (i) arcs are found instead of spots along direction 1;
(ii) the high frequency harmonic spot (marked by the white arrow) is
relatively faint compared to those in the Gr-AP sample. Furthermore,
the interplanar d-spacing from Fig. 7g measures up to ∼0.37 nm,
indicating that the lattice in this region does not return to its original
delithiated state. This nanoscopic increase in interplanar spacing is
not captured in the powder diffraction data (Fig. 3) because the latter
technique provides an average from all portions of the sample. On
the other hand, Region 2, which is in the bulk of the Gr-LP sample,
shows straight, uniform lattice fringes (Fig. 7h) similar to those
observed in the Gr-AP sample (Figs. 7b, 7c). The corresponding FFT
of Region 2 (Fig. 7j) has spots along direction 1 and a high-
frequency harmonic, which suggests greater ordering within the
graphite bulk. Taken together, the HRTEM images and FFT results
indicate there is greater disorder in the graphite lattice near the
Figure 7. Direct electron imaging of the graphite lattice via HRTEM. The as-prepared graphite (Gr-AP) electrode lattice details are elucidated via (a) TEM
imaging with highlighted Regions 1 and 2; real-space magnification of (b) Region 1 and (c) Region 2; localized Fast-Fourier Transforms of (d) Region 1 and (e)
Region 2. Correspondingly, the Gr-LP lattice details are elucidated via (f) TEM imaging with highlighted Regions 1 and 2; real-space magnification of (g)
Region 1 and (h) Region 2; and localized Fast-Fourier Transforms of (i) Region 1 and (j) Region 2. Scale bars: (a), (f) are 10 nm; (b), (c), (g), (h) are 2 nm; (d),
(e), (i), (j) are 5 nm–1
.
Journal of The Electrochemical Society, 2021 168 100509
10. surface of its internal pores and that this disorder can extend up to
∼20 nm into the particle bulk.
Quantification of nanoscopic turbostratic disorder via SEND.—
In Fig. 8 and 9, we quantify the nanoscale heterogeneity of the
graphite by measuring the interplanar d-spacing and local lattice
rotation using SEND.44
In this technique, a ∼2 nm probe (at full-
width half-maximum) is rastered across a 150 nm × 150 nm real-
space area generating an electron diffraction pattern for each probe
position. SEND provides position-resolved structural information
regarding turbostratic disorder in the materials. Details of the SEND
data acquisition are briefly described in the experimental section;
data analysis information is provided in Section 7 of the SI, which
includes Fig. S13. In the SEND experiments, we quantify both the
graphite interplanar spacing and the lattice rotation by tracking
changes to the Ginterplanar vector (with respect to the Graphite-2H
phase) for each real-space sample coordinate of the SEND scan. The
quantification is done by determining (1) changes to the length of the
vector G d
1
interplanar interplanar
∣ ∣ = to measure position-to-position
nanoscopic interplanar d-spacing, which is then represented as a
dinterplanar map to highlight local d-spacing changes; (2) changes to
the in-plane orientation θ of each vector G ,
interplanar which is then
represented as a map of θ
∣∇ ∣ to identify locations where rotational
changes in the lattice occur.
Figure 8a(i) contains HAADF-STEM image from a Gr-AP
particle cross-section, with marked Region 1 (magnified in
Fig. 8a(ii)) and Region 2 (magnified in Fig. 8a(iii)) where SEND
data were acquired. First, we discuss the nanoscale structure of
Region 1 in Fig. 8b. The data indicate that the lattice rotation shows
negligible variation ( 0.09 nm 1
∼ ° − ) across the sample (Fig. 8b(i)) and
that the interplanar d-spacing map across Region 1 is relatively
uniform (Fig. 8b(ii)). Figure 8b(iii) is a plot of the overall d-spacing
from the map as a histogram; the data show a distribution of d-
spacings in the sample with a mean of 0.334 nm and a standard
deviation of 0.006 nm. Figure 8c illustrates that Region 2 is
comparable to Region 1 in terms of both lattice rotation
(Fig. 8c(i)) and interplanar spacings (Figs. 8c(ii) and (iii)).
However, we find a slightly elevated value for rotational variation
in the particle bulk of Fig. 8c(i). This observation points to an
important characteristic of graphite, which is that the graphene
planes tend to group as bands of 10–20 nm thickness (Fig. S14).
Within each graphite band, the magnitude of the rotational variation
is negligible; between band-to-band, the in-plane lattice angle can
exhibit sudden jumps. Overall, though, the results for the Gr-AP
sample are consistent with the HRTEM observations, which also
indicated a uniform lattice. Furthermore, SEND data from the Gr-NP
electrode (Fig. S15) are very similar to those from the Gr-AP
electrode, which indicate that the low-rate cycles have negligible
impact on the graphite particle structure.
By contrast, a non-uniform lattice and an increase in lattice
disorder at the particle edges are observed in particles from the Gr-
LP electrode. Figure 9a(i) contains a HAADF-STEM image with
areas marked Region 1 (magnified in Fig. 9a(ii)) and Region 2
(magnified in Fig. 9a(iii)) where SEND data were collected. In
Fig. 9b(i), we show position-to-position changes of the in-plane
rotation angle of Ginterplanar in Region 1, which is near a relatively
thin pore region. The graphite bulk in Region 1 has a uniform lattice
rotation ( 0.14 nm 1
∼ ° − ), while the graphite edge has greater disorder
(with rotational changes 2 nm 1
> ° − ). Figure 9b(ii) shows the corre-
sponding interplanar d-spacing reconstruction map; the d-spacing is
elevated ( 0.37 nm
> ) only within ∼2 nm of the particle edge while
the bulk has d-spacings similar to those in the Gr-AP sample. The d-
spacing distribution (Fig. 9b(iii)) shows a mean around 0.337 nm
and a standard deviation of 0.008 nm, only slightly larger than those
for the Gr-AP sample.
On the other hand, Region 2 (acquired near the edge of a larger
graphite pore) of the Gr-LP sample (Fig. 9c) shows greater lattice
disorder. The average rotation gradient in this region is 0.30 nm,
̃ °/
while the particle edges have values 4 nm
> °/ (Fig. 9c(i)). Moreover,
the frequency of lattice rotation (i.e., the “wavy” nature of the
lattice) occurs up to ∼20 nm into the graphite bulk from the pore
edge. A similar behavior is observed in Fig. 9c(ii), which shows
elevated d-spacings near the pore edge and extending into the
particle bulk. Figure 9c(iii) shows that the mean d-spacing of Region
2 is 0.35 nm, which is larger than that calculated from the X-ray
data. The d-spacing distribution also shows a tail that extends from
∼0.36 nm to 0.40 nm, which indicates that the graphite edges in
Region 2 have sustained greater damage than those in Region 1. This
result also points to the spatial heterogeneity in lattice disorder
within each graphite particle—the edges with greater exposure to the
electrolyte will experience more Li+
ion (de)intercalation reactions
and apparently greater damage, especially during high-rate charging.
Damage localized at the graphite particle edges is not entirely
unexpected.45
Prior studies have pointed out that Li+
ion intercala-
tion into graphite occurs primarily through the edge planes.46,47
At
high charge rates, significant build-up of Li+
ions is expected at the
edges planes; the concentration gradients between the surface and
bulk sites could induce stresses that are significant enough to deform
the graphite lattice near the particle edges.
Mitigating damage at the graphite particle edges is crucial to
prolonging the life of LIB cells subjected to fast charge. One
solution would be to raise the lower cutoff voltage (LCV) for cell
cycling (e.g. from 2.8 to 3.3 V) to prevent complete delithiation of
the graphite. The residual dilute LixC6 phases have higher d-spacings
than the pristine graphite,29
which would facilitate Li+
ion inter-
calation and (partially) mitigate the stresses induced during the
process. Alternative solutions could include the use of graphite with
higher d-spacings in the anode, as has been suggested for both Li+
and Na+
ion cells.48,49
However, such “expanded” graphite materials
typically have lower electronic conductivity, which would limit the
overall rate of intercalation. In addition, these materials have higher
surface areas and a proclivity to trap more lithium in the SEI formed
during electrolyte reduction reactions. Other solutions proposed to
facilitate rapid cycling include the use of functionalized-graphite that
have higher d-spacings at the particle edges,50
graphite with particle
edges aligned perpendicular to the current collector,51
graphite with
carbon coatings that have larger interlamellar spacing,52
and anodes
containing a mix of graphite and hard carbons.7
These efforts, along
with research on cathode and electrolyte materials, electrode
architectures and cycling protocols, are important steps towards
making fast-charging of LIB cells, a commercial reality.
Conclusions
Fast charging of LIB cells can degrade their energy and power
performance characteristics. Here we show representative data from
as-prepared graphite electrodes (Gr-AP) and from electrodes ex-
tracted from (discharged) cells that were previously charged at rates
up to 6 C (Gr-LP). Electrochemical measurements show that the
harvested electrodes have lower capacities than the Gr-AP electrode
and display a sloping lithiation profile, rather than a staged profile,
even at low rates. Analysis of X-ray diffraction data from the Gr-AP
and Gr-LP electrodes yield similar interplanar d-spacings, indicating
that the graphite bulk is not altered by the electrochemical cycling.
Similar conclusions about the graphite particle bulk can be drawn
from the analysis of HREM and HAADF-STEM images and SEND
data. However, these nanoscale data clearly indicate damage at the
graphite edges, which extend up to ∼20 nm into the particle bulk for
the Gr-LP sample. This damage is seen as arcs (rather than spots) in
the FFT data of HREM images and as increased rotations and higher
d-spacings in the SEND data; both datasets suggest increased
turbostratic disorder and buckling of the graphene planes at particle
edges. In addition to changes in graphite-edge structure, the Gr-LP
electrode shows a significant thickness increase from the build-up of
SEI and particle rearrangements that occur during the cycling. This
SEI contains a mix of compounds, including LiF (seen in the XRD
Journal of The Electrochemical Society, 2021 168 100509
11. patterns) and (oxy)fluoro-phosphates suggested by the EDS data.
Larger quantities of this SEI are present adjacent to the larger
internal pores of the graphite, which likely have easier access to the
electrolyte than the smaller pores. Furthermore, the SEI is localized
Figure 8. Quantitative lattice rotation and interplanar d-spacing analysis of the as-prepared graphite (Gr-AP) sample. (a) HAADF-STEM images (i) at low-
magnification, showing Regions 1 and 2 where SEND acquisition was performed; (ii), (iii) magnified images of Regions 1 and 2, respectively. Diffractive image
reconstructions and analysis of (b) Region 1 and (c) Region 2 containing the following: (i) in-plane rotation gradient map, (ii) interplanar spacing map, (iii)
interplanar spacing distribution. Scale bars: (a) (i) is 2 μm; (a) (ii), (a) (iii), (b) (i), (b) (ii), (c) (i), (c) (ii) are 50 nm.
Journal of The Electrochemical Society, 2021 168 100509
12. at the particle edges and does not penetrate the graphite bulk, suggesting that only Li+
ions (no electrolyte components) intercalate
into the particles (effective desolvation of ions).
Figure 9. Quantitative lattice rotation and interplanar d-spacing analysis of the fast-charged graphite (Gr-LP) electrode. (a) HAADF-STEM images (i) at low-
magnification showing Regions 1 and 2 where SEND data were acquired; (ii), (iii) magnified images of Regions 1 and Region 2. Diffractive image
reconstructions and analysis of (b) Region 1 and (c) Region 2 containing the following: (i) in-plane rotation gradient map, (ii) interplanar spacing map, (iii)
interplanar spacing distribution. Scale bars: (a) (i) is 2 μm; (a) (ii), (a) (iii), (b) (i), (b) (ii), (c) (i), (c) (ii) are 50 nm.
Journal of The Electrochemical Society, 2021 168 100509
13. The implication of our study is that even a small number of high-
rate cycles appears to be sufficient to induce significant and
permanent disorder in graphite domains that are closest to the
electrolyte, be it at particle surfaces or the inner pores. Such disorder
could affect the lithiation kinetics, preventing the graphite particles
from accepting charge and favoring the occurrence of Li plating.
Moreover, we show that these structural changes are highly non-
uniform across the various pores within a same particle, which could
either be a cause or consequence of reaction heterogeneities
commonly observed at high rates. Awareness and mitigation of the
structural evolution at the graphite/electrolyte interfaces is crucial to
the development of LIBs that can endure repeated fast-charging and
yet reliably deliver high-performance over the 10 + year lifespan of
electric vehicles.
Acknowledgments
SP acknowledges support from the U.S. Department of Energy
(DOE) Graduate Student Research (SCGSR) program. The SCGSR
program is administered by the Oak Ridge Institute for Science and
Education for DOE under contract number DE‐SC0014664. This
work was carried out in part at the Materials Research Laboratory
Central Research Facilities, University of Illinois. DA and MTFR
acknowledge support from DOE’s Vehicle Technologies Office
(VTO). The electrodes used in this article were fabricated at
Argonne’s Cell Analysis, Modeling and Prototyping (CAMP)
Facility, which is fully supported by the VTO. We are grateful to
our many colleagues, especially Stephen Trask and Andrew Jansen
at Argonne. Use of the Advanced Photon Source (APS) at Argonne
National Laboratory was supported by the U.S. Department of
Energy, Office of Science, Office of Basic Energy Sciences, under
Contract No. DE-AC02–06CH11357. We are grateful to Saul
Lapidus at the APS for help with the high-resolution powder
diffraction experiments. The submitted manuscript has been created
by UChicago Argonne, LLC, Operator of Argonne National
Laboratory (“Argonne”). Argonne, a U.S. Department of Energy
Office of Science laboratory, is operated under Contract No. DE-
AC02–06CH11357. The U.S. Government retains for itself, and
others acting on its behalf, a paid-up nonexclusive, irrevocable
worldwide license in said article to reproduce, prepare derivative
works, distribute copies to the public, and perform publicly and
display publicly, by or on behalf of the Government.
ORCID
Saran Pidaparthy https://orcid.org/0000-0002-0783-3094
Marco-Tulio F. Rodrigues https://orcid.org/0000-0003-0833-6556
Jian-Min Zuo https://orcid.org/0000-0002-5151-3370
Daniel P. Abraham https://orcid.org/0000-0003-0402-9620
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