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            <p>JES is the flagship journal of The Electrochemical Society. Published continuously from 1902 to the present, JES remains one of the most highly-cited journals in electrochemistry and solid-state science and technology.</p>
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Mark Wightman and Christian Amatore</option><option value="/collections/1945-7111_focus_issue_165_15_Y15">Focus Issue on Electrocatalysis – In Honor of Radoslav Adzic</option><option value="/collections/1945-7111_focus_issue_165_4_Y5">Focus Issue on Processes at the Semiconductor–Solution Interface</option><option value="/collections/1945-7111_focus_issue_165_6_Y7">Focus Issue on Proton Exchange Membrane Fuel Cell (PEMFC) Durability</option><option value="/collections/1945-7111_focus_issue_165_8_Y9">Focus Issue on Ubiquitous Sensors and Systems for IoT</option><option value="/collections/1945-7111_focus_issue_164_1_Y1">Focus Issue of Selected Papers from IMLB 2016 with Invited Papers Celebrating 25
      Years of Lithium Ion Batteries</option><option value="/collections/1945-7111_focus_issue_164_10_Y11">Focus Issue on Oxygen Reduction and Evolution Reactions for High Temperature Energy Conversion and Storage</option><option value="/collections/1945-7111_focus_issue_164_3_Y3">Focus Issue on Biological Fuel Cells</option><option value="/collections/1945-7111_focus_issue_164_8_Y9">Focus Issue on Progress in Molten Salts and Ionic Liquids</option><option value="/collections/focus-issue_1945-7111_164_5_Y5">Focus Issue on Biosensors and Micro–Nano Fabricated Electromechanical Systems</option><option value="/collections/1945-7111_focus_issue_163_1_Y1">Focus Issue on Redox Flow Batteries–Reversible Fuel Cells</option><option value="/collections/1945-7111_focus_issue_163_11_Y19">Focus Issue on Electrolysis for Increased Renewable Energy Penetration</option><option value="/collections/1945-7111_focus_issue_163_12_Y21">Focus Issue on Electrochemical Deposition as Surface Controlled Phenomenon</option><option value="/collections/1945-7111_focus_issue_163_4_Y13">Focus Issue Honoring Allen J. Bard</option><option value="/collections/1945-7111_focus_issue_electrochemical_capacitors_fundamentals_to_applications">Electrochemical Capacitors: Fundamentals to Applications</option><option value="/collections/1945-7111_focus_issue_focus_issue_of_selected_presentations_from_IMLB_2014">Focus Issue of Selected Presentations from the International Meeting on Lithium Batteries (IMLB 2014)</option><option value="/collections/1945-7111_focus_issue_microfluidics_MEMS_NEMS_sensors_and_devices">Microfluidics, MEMS/NEMS, Sensors and Devices</option><option value="/collections/1945-7111_focus_issue_162_11_Y9">Focus Issue on Electrophoretic Deposition</option><option value="/collections/1945-7111_focus_issue_162_13_Y13">Focus Issue on Electrochemical Interfaces in Energy Storage Systems</option><option value="/collections/1945-7111_focus_issue_in_recognition_of_adam_heller_and_his_enduring_contributions_to_electrochemistry">In Recognition of Adam Heller and His Enduring Contributions to Electrochemistry</option><option value="/collections/1945-7111_focus_issue_mechano-electro-chemical_coupling_in_energy_related_materials_and_devices">Mechano-Electro-Chemical Coupling in Energy Related Materials and Devices</option><option value="/collections/1945-7111_focus_issue_mathematical_modeling_of_electrochemical_systems_at_multiple_scales">Mathematical Modeling of Electrochemical Systems at Multiple Scales</option><option value="/collections/1945-7111_focus_issue_electrochemical_processing_and_materials_tailoring_for_advanced_energy_technology">Electrochemical Processing and Materials Tailoring for Advanced Energy
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.0411609jes" class="art-list-item-title event_main-link">Calendar Aging of Lithium-Ion Batteries</a><p class="small art-list-item-meta">Peter Keil <em>et al</em> 2016 <em>J. Electrochem. Soc.</em> <b>163</b> A1872 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.0411609jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Calendar Aging of Lithium-Ion Batteries</span></a><a href="/article/10.1149/2.0411609jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Calendar Aging of Lithium-Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Calendar Aging of Lithium-Ion Batteries" data-link-purpose-append-open="Calendar Aging of Lithium-Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>In this study, the calendar aging of lithium-ion batteries is investigated at different temperatures for 16 states of charge (SoCs) from 0 to 100%. Three types of 18650 lithium-ion cells, containing different cathode materials, have been examined. Our study demonstrates that calendar aging does not increase steadily with the SoC. Instead, plateau regions, covering SoC intervals of more than 20%–30% of the cell capacity, are observed wherein the capacity fade is similar. Differential voltage analyses confirm that the capacity fade is mainly caused by a shift in the electrode balancing. Furthermore, our study reveals the high impact of the graphite electrode on calendar aging. Lower anode potentials, which aggravate electrolyte reduction and thus promote solid electrolyte interphase growth, have been identified as the main driver of capacity fade during storage. In the high SoC regime where the graphite anode is lithiated more than 50%, the low anode potential accelerates the loss of cyclable lithium, which in turn distorts the electrode balancing. Aging mechanisms induced by high cell potential, such as electrolyte oxidation or transition-metal dissolution, seem to play only a minor role. To maximize battery life, high storage SoCs corresponding to low anode potential should be avoided.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.0411609jes">https://doi.org/10.1149/2.0411609jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/abae37" class="art-list-item-title event_main-link">Degradation of Commercial Lithium-Ion Cells as a Function of Chemistry and Cycling Conditions</a><p class="small art-list-item-meta">Yuliya Preger <em>et al</em> 2020 <em>J. Electrochem. Soc.</em> <b>167</b> 120532 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/abae37/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Degradation of Commercial Lithium-Ion Cells as a Function of Chemistry and Cycling Conditions</span></a><a href="/article/10.1149/1945-7111/abae37/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Degradation of Commercial Lithium-Ion Cells as a Function of Chemistry and Cycling Conditions</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Degradation of Commercial Lithium-Ion Cells as a Function of Chemistry and Cycling Conditions" data-link-purpose-append-open="Degradation of Commercial Lithium-Ion Cells as a Function of Chemistry and Cycling Conditions">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Energy storage systems with Li-ion batteries are increasingly deployed to maintain a robust and resilient grid and facilitate the integration of renewable energy resources. However, appropriate selection of cells for different applications is difficult due to limited public data comparing the most commonly used off-the-shelf Li-ion chemistries under the same operating conditions. This article details a multi-year cycling study of commercial LiFePO<sub>4</sub> (LFP), LiNi<sub>x</sub>Co<sub>y</sub>Al<sub>1−x−y</sub>O<sub>2</sub> (NCA), and LiNi<sub>x</sub>Mn<sub>y</sub>Co<sub>1−x−y</sub>O<sub>2</sub> (NMC) cells, varying the discharge rate, depth of discharge (DOD), and environment temperature. The capacity and discharge energy retention, as well as the round-trip efficiency, were compared. Even when operated within manufacturer specifications, the range of cycling conditions had a profound effect on cell degradation, with time to reach 80% capacity varying by thousands of hours and cycle counts among cells of each chemistry. The degradation of cells in this study was compared to that of similar cells in previous studies to identify universal trends and to provide a standard deviation for performance. All cycling files have been made publicly available at batteryarchive.org, a recently developed repository for visualization and comparison of battery data, to facilitate future experimental and modeling efforts.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/abae37">https://doi.org/10.1149/1945-7111/abae37</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ad6cbd" class="art-list-item-title event_main-link">The Operation Window of Lithium Iron Phosphate/Graphite Cells Affects their Lifetime</a><p class="small art-list-item-meta">Eniko S. Zsoldos <em>et al</em> 2024 <em>J. Electrochem. Soc.</em> <b>171</b> 080527 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ad6cbd/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Operation Window of Lithium Iron Phosphate/Graphite Cells Affects their Lifetime</span></a><a href="/article/10.1149/1945-7111/ad6cbd/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Operation Window of Lithium Iron Phosphate/Graphite Cells Affects their Lifetime</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Operation Window of Lithium Iron Phosphate/Graphite Cells Affects their Lifetime" data-link-purpose-append-open="The Operation Window of Lithium Iron Phosphate/Graphite Cells Affects their Lifetime">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Lithium iron phosphate (LFP) battery cells are ubiquitous in electric vehicles and stationary energy storage because they are cheap and have a long lifetime. This work compares LFP/graphite pouch cells undergoing charge-discharge cycles over five state of charge (SOC) windows (0%–25%, 0%–60%, 0%–80%, 0%–100%, and 75%–100%). Cycling LFP cells across a lower average SOC results in less capacity fade than cycling across a higher average SOC, regardless of depth of discharge. The primary capacity fade mechanism is lithium inventory loss due to: lithiated graphite reactivity with electrolyte, which increases incrementally with SOC, and lithium alkoxide species causing iron dissolution and deposition on the negative electrode at high SOC which further accelerates lithium inventory loss. Our results show that even low voltage LFP systems (3.65 V) have a tradeoff between average SOC and lifetime. Operating LFP cells at lower average SOC can extend their lifetime substantially in both EV and grid storage applications.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ad6cbd">https://doi.org/10.1149/1945-7111/ad6cbd</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ab9050" class="art-list-item-title event_main-link">Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models</a><p class="small art-list-item-meta">Chang-Hui Chen <em>et al</em> 2020 <em>J. Electrochem. Soc.</em> <b>167</b> 080534 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ab9050/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models</span></a><a href="/article/10.1149/1945-7111/ab9050/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models" data-link-purpose-append-open="Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Presented here, is an extensive 35 parameter experimental data set of a cylindrical 21700 commercial cell (LGM50), for an electrochemical pseudo-two-dimensional (P2D) model. The experimental methodologies for tear-down and subsequent chemical, physical, electrochemical kinetics and thermodynamic analysis, and their accuracy and validity are discussed. Chemical analysis of the LGM50 cell shows that it is comprised of a NMC 811 positive electrode and bi-component Graphite-SiO<sub>x</sub> negative electrode. The thermodynamic open circuit voltages (OCV) and lithium stoichiometry in the electrode are obtained using galvanostatic intermittent titration technique (GITT) in half cell and three-electrode full cell configurations. The activation energy and exchange current coefficient through electrochemical impedance spectroscopy (EIS) measurements. Apparent diffusion coefficients are estimated using the Sand equation on the voltage transient during the current pulse; an expansion factor was applied to the bi-component negative electrode data to reflect the average change in effective surface area during lithiation. The 35 parameters are applied within a P2D model to show the fit to experimental validation LGM50 cell discharge and relaxation voltage profiles at room temperature. The accuracy and validity of the processes and the techniques in the determination of these parameters are discussed, including opportunities for further modelling and data analysis improvements.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ab9050">https://doi.org/10.1149/1945-7111/ab9050</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ad14d0" class="art-list-item-title event_main-link">Lithium-Ion Cells in Automotive Applications: Tesla 4680 Cylindrical Cell Teardown and Characterization</a><p class="small art-list-item-meta">Manuel Ank <em>et al</em> 2023 <em>J. Electrochem. Soc.</em> <b>170</b> 120536 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ad14d0/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Lithium-Ion Cells in Automotive Applications: Tesla 4680 Cylindrical Cell Teardown and Characterization</span></a><a href="/article/10.1149/1945-7111/ad14d0/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Lithium-Ion Cells in Automotive Applications: Tesla 4680 Cylindrical Cell Teardown and Characterization</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Lithium-Ion Cells in Automotive Applications: Tesla 4680 Cylindrical Cell Teardown and Characterization" data-link-purpose-append-open="Lithium-Ion Cells in Automotive Applications: Tesla 4680 Cylindrical Cell Teardown and Characterization">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Battery research depends upon up-to-date information on the cell characteristics found in current electric vehicles, which is exacerbated by the deployment of novel formats and architectures. This necessitates open access to cell characterization data. Therefore, this study examines the architecture and performance of first-generation Tesla 4680 cells in detail, both by electrical characterization and thermal investigations at cell-level and by disassembling one cell down to the material level including a three-electrode analysis. The cell teardown reveals the complex cell architecture with electrode disks of hexagonal symmetry as well as an electrode winding consisting of a double-sided and homogeneously coated cathode and anode, two separators and no mandrel. A solvent-free anode fabrication and coating process can be derived. Energy-dispersive X-ray spectroscopy as well as differential voltage, incremental capacity and three-electrode analysis confirm a NMC811 cathode and a pure graphite anode without silicon. On cell-level, energy densities of 622.4 Wh/L and 232.5 Wh/kg were determined while characteristic state-of-charge dependencies regarding resistance and impedance behavior are revealed using hybrid pulse power characterization and electrochemical impedance spectroscopy. A comparatively high surface temperature of ∼70 °C is observed when charging at 2C without active cooling. All measurement data of this characterization study are provided as open source.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ad14d0">https://doi.org/10.1149/1945-7111/ad14d0</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.0191808jes" class="art-list-item-title event_main-link">Review—Organic-Inorganic Hybrid Functional Materials: An Integrated Platform for Applied Technologies</a><p class="small art-list-item-meta">Sajjad Husain Mir <em>et al</em> 2018 <em>J. Electrochem. Soc.</em> <b>165</b> B3137 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.0191808jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Review—Organic-Inorganic Hybrid Functional Materials: An Integrated Platform for Applied Technologies</span></a><a href="/article/10.1149/2.0191808jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Review—Organic-Inorganic Hybrid Functional Materials: An Integrated Platform for Applied Technologies</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Review—Organic-Inorganic Hybrid Functional Materials: An Integrated Platform for Applied Technologies" data-link-purpose-append-open="Review—Organic-Inorganic Hybrid Functional Materials: An Integrated Platform for Applied Technologies">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Hybrid functional materials, constituting both inorganic and organic components, are considered potential platforms for applications in extremely diverse fields such as optics, micro-electronics, transportation, health, energy, energy storage, diagnosis, housing, environment and the highly relevant area is Internet of Things (IoT). Material properties of hybrid materials can be tuned by modification of the composition on the molecular scale to produce smart materials. Cross-cutting approaches, to synergistically couple molecular engineering and processing allows to tailor complex hybrid systems of various shapes with perfect control over size, composition, functionality, and morphology. The detailed description and discussion of variety of hybrid functional organic-inorganic materials and their contribution in the designing of specific modern technologies is the prime focus of this review.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.0191808jes">https://doi.org/10.1149/2.0191808jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ac6d13" class="art-list-item-title event_main-link">Review—“Knees” in Lithium-Ion Battery Aging Trajectories</a><p class="small art-list-item-meta">Peter M. Attia <em>et al</em> 2022 <em>J. Electrochem. Soc.</em> <b>169</b> 060517 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ac6d13/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Review—“Knees” in Lithium-Ion Battery Aging Trajectories</span></a><a href="/article/10.1149/1945-7111/ac6d13/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Review—“Knees” in Lithium-Ion Battery Aging Trajectories</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Review—“Knees” in Lithium-Ion Battery Aging Trajectories" data-link-purpose-append-open="Review—“Knees” in Lithium-Ion Battery Aging Trajectories">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Lithium-ion batteries can last many years but sometimes exhibit rapid, nonlinear degradation that severely limits battery lifetime. In this work, we review prior work on “knees” in lithium-ion battery aging trajectories. We first review definitions for knees and three classes of “internal state trajectories” (termed snowball, hidden, and threshold trajectories) that can cause a knee. We then discuss six knee “pathways”, including lithium plating, electrode saturation, resistance growth, electrolyte and additive depletion, percolation-limited connectivity, and mechanical deformation—some of which have internal state trajectories with signals that are electrochemically undetectable. We also identify key design and usage sensitivities for knees. Finally, we discuss challenges and opportunities for knee modeling and prediction. Our findings illustrate the complexity and subtlety of lithium-ion battery degradation and can aid both academic and industrial efforts to improve battery lifetime.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ac6d13">https://doi.org/10.1149/1945-7111/ac6d13</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.1837571" class="art-list-item-title event_main-link">Phospho‐olivines as Positive‐Electrode Materials for Rechargeable Lithium Batteries</a><p class="small art-list-item-meta">A. K. Padhi <em>et al</em> 1997 <em>J. Electrochem. Soc.</em> <b>144</b> 1188 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.1837571/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Phospho‐olivines as Positive‐Electrode Materials for Rechargeable Lithium Batteries</span></a><a href="/article/10.1149/1.1837571/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Phospho‐olivines as Positive‐Electrode Materials for Rechargeable Lithium Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Phospho‐olivines as Positive‐Electrode Materials for Rechargeable Lithium Batteries" data-link-purpose-append-open="Phospho‐olivines as Positive‐Electrode Materials for Rechargeable Lithium Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Reversible extraction of lithium from <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn1.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msub><mi>LiFePO</mi><mrow><mn>4</mn></mrow></msub></math></span></span> (triphylite) and insertion of lithium into <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn2.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msub><mi>FePO</mi><mrow><mn>4</mn></mrow></msub></math></span></span> at 3.5 V <i>vs.</i> lithium at 0.05 mA/cm<sup>2</sup> shows this material to be an excellent candidate for the cathode of a low‐power, rechargeable lithium battery that is inexpensive, nontoxic, and environmentally benign. Electrochemical extraction was limited to ∼0.6 Li/formula unit; but even with this restriction the specific capacity is 100 to 110 mAh/g. Complete extraction of lithium was performed chemically; it gave a new phase, <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn3.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msub><mi>FePO</mi><mrow><mn>4</mn></mrow></msub></math></span></span>, isostructural with heterosite, <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn4.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msub><mi>Fe</mi><mrow><mn>0.65</mn></mrow></msub><msub><mi>Mn</mi><mrow><mn>0.35</mn></mrow></msub><msub><mo>PO</mo><mrow><mn>4</mn></mrow></msub></math></span></span>. The <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn5.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msub><mi>FePO</mi><mrow><mn>4</mn></mrow></msub></math></span></span> framework of the ordered olivine <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn6.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msub><mi>LiFePO</mi><mrow><mn>4</mn></mrow></msub></math></span></span> is retained with minor displacive adjustments. Nevertheless the insertion/extraction reaction proceeds via a two‐phase process, and a reversible loss in capacity with increasing current density appears to be associated with a diffusion‐limited transfer of lithium across the two‐phase interface. Electrochemical extraction of lithium from isostructural <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn7.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msub><mi>LiMPO</mi><mrow><mn>4</mn></mrow></msub></math></span></span> (M = Mn, Co, or Ni) with an <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn8.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msub><mi>LiClO</mi><mrow><mn>4</mn></mrow></msub></math></span></span> electrolyte was not possible; but successful extraction of lithium from <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn9.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msub><mi>LiFe</mi><mrow><mn>1</mn><mo>−</mo><mi>x</mi></mrow></msub><msub><mi>Mn</mi><mrow><mi>x</mi></mrow></msub><msub><mo>PO</mo><mrow><mn>4</mn></mrow></msub></math></span></span> was accomplished with maximum oxidation of the <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn10.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msup><mi>Mn</mi><mrow><mn>3</mn><mo>+</mo></mrow></msup><mo>/</mo><msup><mi>Mn</mi><mrow><mn>2</mn><mo>+</mo></mrow></msup></math></span></span> occurring at <i>x</i> = 0.5. The <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn11.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msup><mi>Fe</mi><mrow><mn>3</mn><mo>+</mo></mrow></msup><mo>/</mo><msup><mi>Fe</mi><mrow><mn>2</mn><mo>+</mo></mrow></msup></math></span></span> couple was oxidized first at 3.5 V followed by oxidation of the <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn12.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msup><mi>Mn</mi><mrow><mn>3</mn><mo>+</mo></mrow></msup><mo>/</mo><msup><mi>Mn</mi><mrow><mn>2</mn><mo>+</mo></mrow></msup></math></span></span> couple at 4.1 V <i>vs.</i> lithium. The <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn13.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msup><mi>Fe</mi><mrow><mn>3</mn><mo>+</mo></mrow></msup><mo>‐</mo><mo>O</mo><mo>‐</mo><msup><mi>Mn</mi><mrow><mn>2</mn><mo>+</mo></mrow></msup></math></span></span> interactions appear to destabilize the <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn14.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msup><mi>Mn</mi><mrow><mn>2</mn><mo>+</mo></mrow></msup></math></span></span> level and stabilize the <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn15.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msup><mi>Fe</mi><mrow><mn>3</mn><mo>+</mo></mrow></msup></math></span></span> level so as to make the <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/144/4/1188/revision1/jes_144_4_1188ieqn16.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><msup><mi>Mn</mi><mrow><mn>3</mn><mo>+</mo></mrow></msup><mo>/</mo><msup><mi>Mn</mi><mrow><mn>2</mn><mo>+</mo></mrow></msup></math></span></span> energy accessible.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.1837571">https://doi.org/10.1149/1.1837571</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.1441707jes" class="art-list-item-title event_main-link">Review—SEI: Past, Present and Future</a><p class="small art-list-item-meta">E. Peled and S. Menkin 2017 <em>J. Electrochem. Soc.</em> <b>164</b> A1703 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.1441707jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Review—SEI: Past, Present and Future</span></a><a href="/article/10.1149/2.1441707jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Review—SEI: Past, Present and Future</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Review—SEI: Past, Present and Future" data-link-purpose-append-open="Review—SEI: Past, Present and Future">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>The Solid-Electrolyte-Interphase (SEI) model for non-aqueous alkali-metal batteries constitutes a paradigm change in the understanding of lithium batteries and has thus enabled the development of safer, durable, higher-power and lower-cost lithium batteries for portable and EV applications. Prior to the publication of the SEI model (1979), researchers used the Butler-Volmer equation, in which a direct electron transfer from the electrode to lithium cations in the solution is assumed. The SEI model proved that this is a mistaken concept and that, in practice, the transfer of electrons from the electrode to the solution in a lithium battery, must be prevented, since it will result in fast self-discharge of the active materials and poor battery performance. This model provides [E. Peled, in “Lithium Batteries,” J.P. Gabano (ed), Academic Press, (1983), E. Peled, <i>J. Electrochem. Soc.</i>, <b>126</b>, 2047 (1979).] new equations for: electrode kinetics (i<sub>o</sub> and b), anode corrosion, SEI resistivity and growth rate and irreversible capacity loss of lithium-ion batteries. This model became a cornerstone in the science and technology of lithium batteries. This paper reviews the past, present and the future of SEI batteries.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.1441707jes">https://doi.org/10.1149/2.1441707jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae2958" class="art-list-item-title event_main-link">Comparative Analysis of Silicon-Carbon Composite, Graphite, and Microscale Silicon Anodes for Next-Gen Lithium-Ion Batteries</a><p class="small art-list-item-meta">Jonas L. S. Dickmanns <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 020505 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae2958/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Comparative Analysis of Silicon-Carbon Composite, Graphite, and Microscale Silicon Anodes for Next-Gen Lithium-Ion Batteries</span></a><a href="/article/10.1149/1945-7111/ae2958/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Comparative Analysis of Silicon-Carbon Composite, Graphite, and Microscale Silicon Anodes for Next-Gen Lithium-Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Comparative Analysis of Silicon-Carbon Composite, Graphite, and Microscale Silicon Anodes for Next-Gen Lithium-Ion Batteries" data-link-purpose-append-open="Comparative Analysis of Silicon-Carbon Composite, Graphite, and Microscale Silicon Anodes for Next-Gen Lithium-Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>While silicon can significantly enhance the energy density of lithium-ion battery (LiB) anodes, its volume expansion of +280% in the fully lithiated Li<sub>15</sub>Si<sub>4</sub> state and the resulting poor cycle life have limited its use in commercial applications. This study investigates a novel silicon-carbon (Si/C) composite anode material, composed of a carbon host structure infiltrated by silicon. The Si/C performance characteristics is compared with those of state-of-the-art graphite (Gra) and silicon-dominant (Si) anodes in full-cells with an NCA cathode. Full-cell charge and discharge rate tests show the same rate capability for the Si/C and Si anodes, which outperform the Gra anode. For a capacity retention of 80%, the cycle life of the full-cells with the Si/C anode of ∼650 cycles far exceeds the ∼200 cycles obtained with the Si anode but is still short of the ∼1000 cycles obtained with the graphite anode. The projected stack-level gravimetric/volumetric energy densities assuming commercial separator and current collector properties are ∼7%/∼16% higher for the Si/C compared to the graphite anode, approaching the ∼15%/∼20% energy density gains of the Si anodes. Consequently, this Si/C composite is a promising anode active material for LiBs, offering a combination of high energy density, rate capability, and lifetime.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p>
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<ul><li><p>Synthesis overview of a silicon-carbon composite (Si/C) anode material.</p></li><li><p>Full-cell comparison of graphite, Si-dominant, and Si/C anodes with NCM cathodes.</p></li><li><p>Enhanced fast-charging of silicon-containing anodes without lithium plating.</p></li><li><p>Si/C offers an optimal balance between cycle life and energy/power density.</p></li></ul>
</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae2958">https://doi.org/10.1149/1945-7111/ae2958</a></div></div></li></ul><!--    articleEntryList end--></div></div></div><!-- End Most read tabpanel --><!-- Start Latest tabpanel --><div tabindex="0"
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae98c0" class="art-list-item-title event_main-link">Towards Optimizing Li-ion Battery Fast Charging: A Strategy and a Validation Framework</a><p class="small art-list-item-meta">Mark W. Verbrugge and Daniel R. Baker 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 170515 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae98c0/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Towards Optimizing Li-ion Battery Fast Charging: A Strategy and a Validation Framework</span></a><a href="/article/10.1149/1945-7111/ae98c0/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Towards Optimizing Li-ion Battery Fast Charging: A Strategy and a Validation Framework</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Towards Optimizing Li-ion Battery Fast Charging: A Strategy and a Validation Framework" data-link-purpose-append-open="Towards Optimizing Li-ion Battery Fast Charging: A Strategy and a Validation Framework">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This study focuses on the fast charging of lithium-ion cells with porous graphite electrodes while avoiding lithium plating. We demonstrate that by using a linearized version of the model equations, an optimization problem can be formulated, which bounds the maximum current density and ensures that the open-circuit potential at the graphite surface remains above a critical threshold. Based on these insights, we propose a new charging strategy evaluated using the full cell model, which initiates charging at the maximum allowable constant current (CC) before transitioning to a constant value for the open-circuit potential (CU) at the electrode-electrolyte interface. This CC-CU method is compared to various pulse charging protocols, the results of which are consistent with the proposed strategy providing a good estimate for the optimal charge rate for common use conditions.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae98c0">https://doi.org/10.1149/1945-7111/ae98c0</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9b73" class="art-list-item-title event_main-link">Experimental Study on the Advanced Treatment of Sulfonic Acid Wastewater Using a Dual-Anode Electrochemical Method</a><p class="small art-list-item-meta">Chao Guo <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 173502 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9b73/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Experimental Study on the Advanced Treatment of Sulfonic Acid Wastewater Using a Dual-Anode Electrochemical Method</span></a><a href="/article/10.1149/1945-7111/ae9b73/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Experimental Study on the Advanced Treatment of Sulfonic Acid Wastewater Using a Dual-Anode Electrochemical Method</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Experimental Study on the Advanced Treatment of Sulfonic Acid Wastewater Using a Dual-Anode Electrochemical Method" data-link-purpose-append-open="Experimental Study on the Advanced Treatment of Sulfonic Acid Wastewater Using a Dual-Anode Electrochemical Method">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Sulfonic acid wastewater is highly toxic, corrosive and difficult to biodegrade, posing serious threats to the ecological environment and human health. In this study, a synergistic electrochemical oxidation–electrocoagulation system comprising Ti/PbO<sub>2</sub> and Fe dual anodes coupled with a stainless steel cathode was established. Operating parameters were optimized using single-factor experiments and the Box–Behnken response surface method, while treatment efficacy and mechanisms were evaluated by electrochemical characterization, single- and dual-anode comparisons, radical quenching, cyclic testing and spectroscopic analysis. Under 60 min electrolysis, 49 mA·cm<sup>−2</sup>, pH 3 and 2 cm plate spacing, the predicted COD removal was 35.92%, while the measured COD and TOC removals were 35.70% and 17.90%, respectively. The dual-anode system outperformed the Ti/PbO<sub>2</sub> and Fe single-anode systems, confirming synergism between anodic oxidation and electrocoagulation. Quenching reduced COD removal from 35.43% to 12.57%, identifying ·OH-mediated oxidation as a key mechanism. After 10 cycles, COD removal declined slightly from 35.8% to 33.7%, with minor Pb<sup>2+</sup> leaching. UV–Vis and FT-IR indicated changes in aromatic conjugated structures, chromophores and sulphonic acid groups. Further mass-spectrometric verification of intermediates and pathways is required.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlight</h2><p>1.Ti/PbO<sub>2</sub>-Fe dual-anode coupled oxidation and electroflocculation technology.</p><p>2.The response surface method determined the optimal conditions to be: a current density of 49 mA·cm<sup>−2</sup>, a pH of 3, an electrode spacing of 2 cm, and a reaction time of 60 min.</p><p>3.The removal efficiencies for chemical oxygen demand (COD) and total organic carbon (TOC) reached 35.70%–17.90%, respectively.</p><p>4.The treatment performance of the dual-anode system outperformed the sum of the effects of the single-anode systems.</p><p>5.The hydroxyl radical-dominated electrocatalytic-electrocoagulation synergistic mechanism maintained stable COD removal performance</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9b73">https://doi.org/10.1149/1945-7111/ae9b73</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9ef7" class="art-list-item-title event_main-link">Optimal Yttrium Doping Window in RuO<sub>2</sub> for Enhanced Activity and Durability in Three-Electrode Acidic OER</a><p class="small art-list-item-meta">Yang Ying <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 176501 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9ef7/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Optimal Yttrium Doping Window in RuO2 for Enhanced Activity and Durability in Three-Electrode Acidic OER</span></a><a href="/article/10.1149/1945-7111/ae9ef7/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Optimal Yttrium Doping Window in RuO2 for Enhanced Activity and Durability in Three-Electrode Acidic OER</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Optimal Yttrium Doping Window in RuO2 for Enhanced Activity and Durability in Three-Electrode Acidic OER" data-link-purpose-append-open="Optimal Yttrium Doping Window in RuO2 for Enhanced Activity and Durability in Three-Electrode Acidic OER">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Ruthenium dioxide (RuO<sub>2</sub>) is a highly active catalyst for the acidic oxygen evolution reaction (OER), but its anodic dissolution limits long-term operation. Here, we synthesized a series of Y<i><sub>x</sub></i>Ru<sub>1−<i>x</i></sub>O<sub>2</sub> catalysts and identified Y–RuO<sub>2</sub>–2 as the best-performing composition among the samples tested in a three-electrode cell containing 0.1 M HClO<sub>4</sub>. Y–RuO<sub>2</sub>–2 requires an overpotential of 206 mV to reach 10 mA cm<sup>−2</sup> and remains operational during a 345 600 s (96 h) chronopotentiometry test. In a separate experiment terminated after 100 000 s, post-test XRD, SEM/EDS, and XPS measurements show retention of the rutile framework, no obvious micron-scale Y segregation within the analyzed regions, and a predominantly Ru<sup>4+</sup> surface state. ICP-MS analysis of the electrolyte after 100 000 s gives a dissolved-Ru concentration of 55 μg l<sup>−1</sup>, lower than those measured for commercial RuO<sub>2</sub> and hydrothermally prepared undoped RuO<sub>2</sub> under the same protocol. EIS and DFT-PDOS results provide qualitative, indirect evidence of electronic-structure and charge-transfer changes associated with moderate Y incorporation. These results establish an experimentally observed composition-performance relationship in three-electrode acidic OER screening, while operando spectroscopy and MEA testing remain necessary for direct mechanistic and device-level validation.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>Aliovalent doping enables acid-stable OER via functionalized lattice design.</p></li><li><p>Overpotential drops to 206 mV @10 mA·cm<sup>−2</sup> with negligible decay for 96 h.</p></li><li><p>Strategy breaks activity-stability trade-off for RuO<sub>2</sub>.</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9ef7">https://doi.org/10.1149/1945-7111/ae9ef7</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/aea028" class="art-list-item-title event_main-link">Effects of an Induced Temperature Gradient on the Performance and Degradation of LFP/AG Cylindrical Cells</a><p class="small art-list-item-meta">Kate Leslie <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 170513 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/aea028/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Effects of an Induced Temperature Gradient on the Performance and Degradation of LFP/AG Cylindrical Cells</span></a><a href="/article/10.1149/1945-7111/aea028/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Effects of an Induced Temperature Gradient on the Performance and Degradation of LFP/AG Cylindrical Cells</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Effects of an Induced Temperature Gradient on the Performance and Degradation of LFP/AG Cylindrical Cells" data-link-purpose-append-open="Effects of an Induced Temperature Gradient on the Performance and Degradation of LFP/AG Cylindrical Cells">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Thermal management of Li-ion cells within battery packs for stationary energy storage and electric vehicles is critical to ensure longevity. Cells within packs are often heated or cooled using a thermal plate underneath the pack, which could lead to non-uniform temperature in the cells. To test the effects of temperature gradients on LFP/graphite cylindrical cells, a specialized cell holder was designed to apply a constant temperature to the top of a cell and a different constant temperature to the bottom. Temperatures of 30 °C–40 °C, 25 °C–45 °C, and 15 °C–55 °C were applied to the bottom and tops of the cells, respectively, and verified using an infrared camera. Cells were cycled at a variety of rates for approximately six months, and the capacity loss was compared between the different conditions. For most conditions there was no difference in the capacity fade based on temperature gradient and performance closely matched that of cells tested at a constant temperature of 35 °C. Thermal modelling of the jelly roll suggests that the temperature gradient does not penetrate deeply into the jelly roll due to the excellent axial thermal conductivity and this can explain the independence of capacity loss on the magnitude of the applied temperature gradient.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/aea028">https://doi.org/10.1149/1945-7111/aea028</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/aea05a" class="art-list-item-title event_main-link">TL-PINN: Transfer Learning-Enhanced Physics-Informed Neural Network for Lithium-Ion Battery State of Charge Estimation</a><p class="small art-list-item-meta">Zhihong Wang <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 170512 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/aea05a/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;TL-PINN: Transfer Learning-Enhanced Physics-Informed Neural Network for Lithium-Ion Battery State of Charge Estimation</span></a><a href="/article/10.1149/1945-7111/aea05a/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;TL-PINN: Transfer Learning-Enhanced Physics-Informed Neural Network for Lithium-Ion Battery State of Charge Estimation</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="TL-PINN: Transfer Learning-Enhanced Physics-Informed Neural Network for Lithium-Ion Battery State of Charge Estimation" data-link-purpose-append-open="TL-PINN: Transfer Learning-Enhanced Physics-Informed Neural Network for Lithium-Ion Battery State of Charge Estimation">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Accurate state-of-charge (SOC) estimation is essential for the safe and efficient operation of battery management systems (BMS). To address the limited accuracy and poor reliability of conventional methods under complex operating conditions, a transfer learning-enhanced physics-informed neural network (TL-PINN) is proposed for SOC estimation. The proposed framework embeds the underlying dynamics of the equivalent circuit into the neural network through differential equation constraints. By jointly optimizing data reconstruction and physical constraints, electrochemical knowledge is explicitly incorporated into the network, enabling improved estimation accuracy and robustness under complex scenarios. Furthermore, maximum mean discrepancy (MMD)-based adaptation and fine-tuning strategies are introduced to facilitate efficient reuse of source-domain knowledge and enhance cross-domain generalization. Experiments conducted on both single-cell and real-world vehicle datasets demonstrate that the base PINN model achieves the best overall performance, with a root mean square error (RMSE) of 0.835%. In cross-temperature transfer scenarios, the RMSE remains below 3.0% across all target temperatures after fine-tuning. Moreover, after transferring the pretrained single-cell model to real-world vehicle operating data, the proposed method still achieves an average RMSE of 4.21%. These results demonstrate the superior adaptability and robustness of the proposed TL-PINN, highlighting its potential for reliable battery state monitoring in electric vehicles.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/aea05a">https://doi.org/10.1149/1945-7111/aea05a</a></div></div></li></ul><!--    articleEntryList end--></div></div></div><!-- End Latest tabpanel --><!-- Express Letters tabpanel --><!-- Express Letters tabpanel --><!-- Start Review tabpanel --><div tabindex="0"
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9646" class="art-list-item-title event_main-link">Recent Advances in Electrochemical Sensors for Aflatoxin B1 Detection</a><p class="small art-list-item-meta">Amed Gallegos-Tabanico <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 167504 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9646/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Recent Advances in Electrochemical Sensors for Aflatoxin B1 Detection</span></a><a href="/article/10.1149/1945-7111/ae9646/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Recent Advances in Electrochemical Sensors for Aflatoxin B1 Detection</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Recent Advances in Electrochemical Sensors for Aflatoxin B1 Detection" data-link-purpose-append-open="Recent Advances in Electrochemical Sensors for Aflatoxin B1 Detection">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Aflatoxin B1 (AFB1), the most toxic and carcinogenic toxin produced by Aspergillus flavus and Aspergillus parasiticus, poses a major risk to food safety and public health due to its frequent occurrence in cereals and derived products. Conventional detection methods, including High-Performance Liquid Chromatography (HPLC) and Enzyme-Linked Immunosorbent Assay (ELISA), provide high sensitivity but are costly, time-consuming, and unsuitable for on-site use. Currently, no effective method exists to reduce aflatoxin levels in food and feed, thus early detection remains the only viable strategy for managing contamination. This review highlights advances in electrochemical sensors as promising alternatives, emphasizing the role of nanostructured materials, electrode surface modifications, and molecular recognition strategies such as aptamers, molecularly imprinted polymers, and antibodies. Challenges like matrix effects, sensor stability, and reproducibility are discussed, alongside future perspectives toward portable, reliable, and cost-effective detection platforms.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9646">https://doi.org/10.1149/1945-7111/ae9646</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9647" class="art-list-item-title event_main-link">Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications</a><p class="small art-list-item-meta">Zeda Zhou and Yixuan Bian 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 167503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9647/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications</span></a><a href="/article/10.1149/1945-7111/ae9647/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications" data-link-purpose-append-open="Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Cortisol, a steroid hormone, is critical in regulating the stress response, metabolic homeostasis, and immune balance in the human body. Since cortisol is widely distributed in body fluids, the use of easily accessible fluids, such as sweat, makes continuous health assessment possible. Wearable sensors support the non-invasive and <i>in situ</i> collection of biomarkers, while electrochemical sensing methods have been widely used for the analysis of biomarkers due to their low cost, easy operation, high sensitivity, and fast response. The development and application of wearable electrochemical sensors provide essential support for non-invasive, real-time, and continuous monitoring of cortisol. This review systematically covers the recent progress in wearable electrochemical sensors, focusing particularly on sensing strategies of different recognition elements and critically evaluating their performance and limitations in complex biological fluids. Additionally, this review introduces the innovative applications of graphene, MXene, metal nanoparticles, and other functional materials in wearable electrochemical sensors, systematically comparing the sensing abilities of each material. Subsequently, in view of the challenges encountered in practical applications, this work discusses microfluidic integration strategies, multilayer interference-resistant interface designs, and machine learning-based data calibration methods. Finally, future prospects for interdisciplinary approaches in advancing precision medicine and real-time health monitoring are reviewed.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9647">https://doi.org/10.1149/1945-7111/ae9647</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae9406" class="art-list-item-title event_main-link">From Task-Specific AI to Battery Foundation Models</a><p class="small art-list-item-meta">Jingyuan Zhao <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 150520 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9406/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;From Task-Specific AI to Battery Foundation Models</span></a><a href="/article/10.1149/1945-7111/ae9406/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;From Task-Specific AI to Battery Foundation Models</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="From Task-Specific AI to Battery Foundation Models" data-link-purpose-append-open="From Task-Specific AI to Battery Foundation Models">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Artificial intelligence (AI) is influencing battery research and life-cycle management, spanning materials discovery, electrode and cell design, manufacturing optimization, diagnostics, safety monitoring, recycling, and certification. These advances are enabled by growing battery datasets and learning methods that extract patterns from complex electrochemical systems. Yet most current models remain task-specific and are trained on fragmented datasets, limiting transferability across chemistries, cell formats, operating conditions, and life-cycle stages. Battery foundation models (BFMs) offer a promising but emerging paradigm for battery intelligence. They may be formulated as large, pre-trained, and adaptable architectures that integrate multimodal battery data with physics-informed priors to represent electrochemical structures, states, and dynamics. Unlike direct analogues of general large language models, BFMs should be understood as physics-aware foundation models designed for scientific reasoning under multiscale physical constraints, heterogeneous and incomplete data, and stringent safety and reliability requirements. By combining self-supervised learning with mechanistic electrochemical models, BFMs may learn more interpretable and transferable representations across materials, formats, and duty cycles. If sufficiently validated, such representations could support materials discovery, manufacturing, diagnostics, recycling, and certification. This Review discusses challenges in data fragmentation, validation, interpretability, and computational sustainability, and outlines a roadmap toward responsible BFMs and integrated battery-domain ecosystems across the lifecycle.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights:</h2><p><ul><li><p>Trace the shift from general LLMs toward physics-aware foundation models for battery science.</p></li><li><p>Integrate multimodal data with physics-informed priors to enable robust and transferable models.</p></li><li><p>Discuss lifecycle-wide applications from materials discovery to recycling and certification.</p></li><li><p>Frame challenges in data fragmentation, interpretability, and computational sustainability.</p></li><li><p>Outline a roadmap toward lifecycle-responsible BFMs and integrated domain ecosystems.</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9406">https://doi.org/10.1149/1945-7111/ae9406</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae888c" class="art-list-item-title event_main-link">Isothermal Microcalorimetry for Battery Characterization</a><p class="small art-list-item-meta">David J. Arnot <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 150515 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae888c/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Isothermal Microcalorimetry for Battery Characterization</span></a><a href="/article/10.1149/1945-7111/ae888c/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Isothermal Microcalorimetry for Battery Characterization</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Isothermal Microcalorimetry for Battery Characterization" data-link-purpose-append-open="Isothermal Microcalorimetry for Battery Characterization">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>As battery function has improved over the past decades, so too has our ability to interrogate the underlying electrochemical processes. Thermal energy generation is a key aspect of batteries affecting electrochemical function, safety, and lifespan. The heat generated by a battery is related to thermodynamics, kinetics, structural changes, and side reactions; measurements of heat production can therefore provide insight into any of these subjects. Isothermal microcalorimetry (IMC) can quantify heat flow within functioning systems with microwatt (or better) accuracy and precision. The ability to simultaneously measure heat production and electrochemical properties allows for fundamental scientific investigations as well as practical measurements on laboratory scale and commercial cells with different form factors. Herein, we review the use of isothermal microcalorimetry for probing battery thermal effects associated with the (dis)charge reaction, phase changes, and parasitic reactions. This work serves as an introduction for unfamiliar readers and summarizes the research that has been done over the years. We begin with a brief history of IMC as it relates to battery research, followed by an overview of the applicable theory, and highlight extensive examples from the literature. Opportunities for future research directions involving application and advances for the use of IMC are also presented.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>Battery energy content is released as either usable work or unwanted heat</p></li><li><p>Isothermal microcalorimetry measures thermal energy exchange with <i>μ</i>W accuracy and precision</p></li><li><p>Battery thermal processes can be a signature of degradation processes</p></li><li><p>Thermodynamic properties can be derived from calorimetric measurements</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae888c">https://doi.org/10.1149/1945-7111/ae888c</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae8eb9" class="art-list-item-title event_main-link">The Use of Adsorptive Stripping Voltammetry for the Determination of Ti(IV): Advantages, Limitations, Applications—A Review</a><p class="small art-list-item-meta">Edyta Sobczak and Malgorzata Grabarczyk 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 156503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae8eb9/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Use of Adsorptive Stripping Voltammetry for the Determination of Ti(IV): Advantages, Limitations, Applications—A Review</span></a><a href="/article/10.1149/1945-7111/ae8eb9/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Use of Adsorptive Stripping Voltammetry for the Determination of Ti(IV): Advantages, Limitations, Applications—A Review</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Use of Adsorptive Stripping Voltammetry for the Determination of Ti(IV): Advantages, Limitations, Applications—A Review" data-link-purpose-append-open="The Use of Adsorptive Stripping Voltammetry for the Determination of Ti(IV): Advantages, Limitations, Applications—A Review">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This review discusses methods of determining the presence of titanium using adsorptive stripping voltammetry (AdSV) and catalytic adsorptive voltammetry (CAdSV). The work centers on the key factors that influence the sensitivity and selectivity of the proposed analytical procedures. Particular attention was paid to the role of the complexing agents used and the presence of oxidizing agents. The influence of the type of working electrode and the most commonly used electrode modifiers was also considered. The possibility of determining titanium and other elements simultaneously during a single voltammetric measurement was also discussed. The following sections describe the potential for interference from components of the inorganic and organic matrices. The review also provides examples of how the described voltammetric procedures can be used to determine titanium in real samples with diverse matrices. The most important analytical parameters of the methods described are presented in tabular form to allow comparison of their usefulness for analysis.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae8eb9">https://doi.org/10.1149/1945-7111/ae8eb9</a></div></div></li></ul><!--    articleEntryList end--></div></div></div><!-- End Review tabpanel --><!-- Start Featured tabpanel --><!-- End Featured tabpanel --><!-- Start Editor's chocie tabpanel --><div tabindex="0"
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae60a9" class="art-list-item-title event_main-link">Editors’ Choice—Understanding the Role of Multivalency in Chloride-Based Electrolytes for Efficient Iron Electrosynthesis</a><p class="small art-list-item-meta">William Lvovich <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 082502 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae60a9/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Understanding the Role of Multivalency in Chloride-Based Electrolytes for Efficient Iron Electrosynthesis</span></a><a href="/article/10.1149/1945-7111/ae60a9/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Understanding the Role of Multivalency in Chloride-Based Electrolytes for Efficient Iron Electrosynthesis</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Editors’ Choice—Understanding the Role of Multivalency in Chloride-Based Electrolytes for Efficient Iron Electrosynthesis" data-link-purpose-append-open="Editors’ Choice—Understanding the Role of Multivalency in Chloride-Based Electrolytes for Efficient Iron Electrosynthesis">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This study investigates aqueous electrolytes for efficient iron electrodeposition directly from Fe<sup>3+</sup> at ambient temperature. Concentrated lithium chloride (LiCl) based electrolytes were found to stabilize the Fe<sup>3+</sup> in the electrolyte, suppress parasitic hydrogen evolution and suppress redox shuttling of intermediate Fe<sup>2+</sup>, thus promoting efficient iron electrodeposition. These attributes collectively enabled high Coulombic efficiencies (&gt;75%) at high current densities (&gt;200 mA cm<sup>−2</sup>). Furthermore, detailed investigation revealed that increasing the LiCl concentration increased the electrolyte viscosity and decreased the Fe<sup>2+</sup> out-diffusion rate while also suppressing the activity of water. Sufficiently high LiCl concentrations (&gt;7 M) thus provide a window of current densities in which elevated Coulombic efficiencies can be achieved. Overall, this paper develops an understanding of the effects of electrolyte composition on the competition between Fe electrodeposition, hydrogen co-evolution, and intermediate Fe<sup>2+</sup> out-diffusion for efficient Fe metal electrosynthesis.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae60a9">https://doi.org/10.1149/1945-7111/ae60a9</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae17eb" class="art-list-item-title event_main-link">Editors’ Choice—Modeling of Multistage Redox-Mediated Electrodialysis for Volatile Fatty Acids Fractionation</a><p class="small art-list-item-meta">Riccardo Candeago <em>et al</em> 2025 <em>J. Electrochem. Soc.</em> <b>172</b> 113503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae17eb/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Modeling of Multistage Redox-Mediated Electrodialysis for Volatile Fatty Acids Fractionation</span></a><a href="/article/10.1149/1945-7111/ae17eb/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Modeling of Multistage Redox-Mediated Electrodialysis for Volatile Fatty Acids Fractionation</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Editors’ Choice—Modeling of Multistage Redox-Mediated Electrodialysis for Volatile Fatty Acids Fractionation" data-link-purpose-append-open="Editors’ Choice—Modeling of Multistage Redox-Mediated Electrodialysis for Volatile Fatty Acids Fractionation">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Production of volatile fatty acids (VFAs) from biomass fermentation is a promising pathway for sustainable chemical production. A central challenge is cost-effective recovery and fractionation of VFAs from fermentation broths. Redox-mediated electrodialysis (redox-ED) can be an energy efficient technique for VFA separation, replacing water splitting with redox-reactions. However, the low selectivity between VFAs of different lengths (separation factors &lt;3) obtained using commercially-available anion-exchange membranes limits the final product purity for industrial use. Cascaded operation can overcome these material limitations and increase product purity, yet multistage redox-ED can be complex and has not been extensively explored for selective ion separations. Here, we developed a physics-based model of redox-ED using finite elements to simulate the separation of a ternary carboxylic acid feed (propionic, butyric, and hexanoic) and evaluated five different multistage architectures including series, parallel, co-current, and counter-current setups. The single-stage, two-dimensional steady-state model captured the effect of the flow-field, concentration, and potential gradients, yielding reasonable agreement with experimental data. We then investigated the tradeoff between number of stages, product purity, and productivity, and assessed the impact of membrane selectivity. In sum, cascaded redox-ED with reflux simultaneously improved product purity and productivity, while series or equivalent single-stage architectures presented a tradeoff between VFA purity and productivity.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae17eb">https://doi.org/10.1149/1945-7111/ae17eb</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/adc553" class="art-list-item-title event_main-link">Editors’ Choice—Rapid Deactivation Convolutes Electrochemical CO<sub>2</sub> Reduction Selectivity Measurements on Gold Rotating Ring Disk Electrodes</a><p class="small art-list-item-meta">Maria Kelly <em>et al</em> 2025 <em>J. Electrochem. Soc.</em> <b>172</b> 046503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/adc553/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Rapid Deactivation Convolutes Electrochemical CO2 Reduction Selectivity Measurements on Gold Rotating Ring Disk Electrodes</span></a><a href="/article/10.1149/1945-7111/adc553/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Rapid Deactivation Convolutes Electrochemical CO2 Reduction Selectivity Measurements on Gold Rotating Ring Disk Electrodes</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Editors’ Choice—Rapid Deactivation Convolutes Electrochemical CO2 Reduction Selectivity Measurements on Gold Rotating Ring Disk Electrodes" data-link-purpose-append-open="Editors’ Choice—Rapid Deactivation Convolutes Electrochemical CO2 Reduction Selectivity Measurements on Gold Rotating Ring Disk Electrodes">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Voltammetric measurements of electrochemical CO<sub>2</sub> reduction reaction (CO<sub>2</sub>RR) selectivity on rotating ring disk electrodes (RRDE) are a rapid and sensitive method for quantifying an electrocatalyst’s selectivity, i.e. faradaic efficiency (FE). This method has been applied to polycrystalline Au electrocatalysts where a Au disk electrode catalyzes both the CO<sub>2</sub>RR and hydrogen evolution reaction while the concentric Au ring electrode selectively senses CO by oxidizing CO back to CO<sub>2</sub>. Such measurements enabled fundamental mechanistic studies but suffer from poor inter-laboratory reproducibility. This work identifies causes of variability in RRDE selectivity measurements by comparing protocols with different electrochemical methods, reagent purities, and glassware cleaning procedures. We observed FE<sub>CO</sub> decrease by 56% during 5 min chronoamperometry measurements, a phenomenon that is not readily apparent in voltammetric scans due to their dynamic nature. Electroplating of electrolyte impurities onto the disk and ring surfaces were identified as a major contributor to Au deactivation. Additionally, the oxygen reduction reaction may lead to higher disk currents in inadequately purged electrolytes, causing an apparent underestimation of FE<sub>CO</sub> at low overpotentials. Lastly, we propose operational bounds for CO<sub>2</sub>RR selectivity measurements on Au using the RRDE method and provide suggestions on steps for improving the accuracy of this technique.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/adc553">https://doi.org/10.1149/1945-7111/adc553</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/adbd7d" class="art-list-item-title event_main-link">Editors’ Choice—Molten Salt Electrolysis in Chloride Melts for Energy-Efficient Iron Metal Production</a><p class="small art-list-item-meta">Anar Badalbayli <em>et al</em> 2025 <em>J. Electrochem. Soc.</em> <b>172</b> 032508 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/adbd7d/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Molten Salt Electrolysis in Chloride Melts for Energy-Efficient Iron Metal Production</span></a><a href="/article/10.1149/1945-7111/adbd7d/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Molten Salt Electrolysis in Chloride Melts for Energy-Efficient Iron Metal Production</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Editors’ Choice—Molten Salt Electrolysis in Chloride Melts for Energy-Efficient Iron Metal Production" data-link-purpose-append-open="Editors’ Choice—Molten Salt Electrolysis in Chloride Melts for Energy-Efficient Iron Metal Production">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This study explores chloride molten salt electrolysis (CMSE) as a promising route for energy-efficient iron metal (Fe) production. Moderate temperature (500 °C) LiCl-KCl molten salts offer excellent thermodynamic stability, high ionic conductivity and diffusivity, and high solubility for FeCl<sub>3</sub>, thereby enabling efficient Fe metal extraction at high electrowinning rates. Here, we demonstrate the two essential steps for converting taconite ore into Fe metal. First, Fe<sub>2</sub>O<sub>3</sub> from taconite pellets was selectively leached in HCl yielding a high-purity FeCl<sub>3</sub> aqueous solution, while the gangue components settled at the bottom. Then, anhydrous FeCl<sub>3</sub> was electrolyzed in a LiCl-KCl eutectic molten salt at 500 °C at high current density (1 A cm<sup>−2</sup>) and at high Coulombic efficiency (&gt;85%). Analysis of the electrowon Fe deposits revealed dendritic structures with purity of &gt;99 wt%, which could be further improved to nearly 100 wt% through arc re-melting. CMSE offers low specific energy consumption (3.7 kWhr kg<sup>−1</sup>), competitive with H<sub>2</sub>-DRI and other electrolytic approaches being pursued globally. Our findings underscore the potential of CMSE as an energy-efficient route for electrosynthesis of Fe metal.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/adbd7d">https://doi.org/10.1149/1945-7111/adbd7d</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/adaf5b" class="art-list-item-title event_main-link">Editors’ Choice—Investigation of the Dynamic Evolution of the Cathode-Electrolyte Interphase Using Scanning Electrochemical Microscopy</a><p class="small art-list-item-meta">Guoxin Li <em>et al</em> 2025 <em>J. Electrochem. Soc.</em> <b>172</b> 026501 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/adaf5b/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Investigation of the Dynamic Evolution of the Cathode-Electrolyte Interphase Using Scanning Electrochemical Microscopy</span></a><a href="/article/10.1149/1945-7111/adaf5b/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Investigation of the Dynamic Evolution of the Cathode-Electrolyte Interphase Using Scanning Electrochemical Microscopy</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Editors’ Choice—Investigation of the Dynamic Evolution of the Cathode-Electrolyte Interphase Using Scanning Electrochemical Microscopy" data-link-purpose-append-open="Editors’ Choice—Investigation of the Dynamic Evolution of the Cathode-Electrolyte Interphase Using Scanning Electrochemical Microscopy">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Cathode-electrolyte interphase (CEI) is critical for inhibiting the cathode degradation to maintain cell life. However, the evolution of the CEI is still unclear due to its complex and slow dynamic process. Here we used scanning electrochemical microscopy (SECM) for in situ investigation of CEI formation process on LiFePO<sub>4</sub> cathode. Feedback images and probe scan curves showed a heterogeneous passivation that was gently generated on the LiFePO<sub>4</sub> particles during both charging and discharging. Besides, a LiFePO<sub>4</sub> composited electrode was also used to investigate the CEI formation to simulate the condition of real battery system. The composited cathode does not show obvious CEI formation within first two cycles. The SECM results between the pristine LiFePO<sub>4</sub> particles and the composited LiFePO<sub>4</sub> indicated the dynamic accumulation of CEI, which is influenced by the ability to charge transfer kinetics of cathode materials. This approach provided a feasible consideration for the connections between the dynamic evolution of the CEI and changes in charge transfer capability of cathode during cycling.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>In-situ investigation of cathode-electrolyte interphase formation.</p></li><li><p>The evolution of native active material and composite slurry were compared.</p></li><li><p>The electrochemical activity change upon cathode cycling are analysed in situ.</p></li><li><p>The influence of the charge transfer capability upon CEI generation is revealed.</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/adaf5b">https://doi.org/10.1149/1945-7111/adaf5b</a></div></div></li></ul><!--    articleEntryList end--></div></div></div><!-- End Editor's chocie tabpanel --><!-- Start AM tabpanel --><div tabindex="0"
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                         style="display: none;"><!--    accepted manuscript listing start--><p id="jnl-issue-disp-links" class="cf"><button data-reveal-label-alt="Close all abstracts" class="reveal-all-trigger mr-2 small"
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               data-link-purpose-append-open="in this tab">Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!-- Start AM list content --><ul class="art-list" id="wd-jnl-issue-art-list"><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/aea1c0" class="art-list-item-title event_main-link">Data-Driven Advances in Electrochemical Energy and Sensing: Artificial Intelligence Approaches from Concept to Application</a><p class="small art-list-item-meta">Ghosh et al&nbsp;</p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/aea1c0/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View accepted manuscript<span class="offscreen-hidden">,&nbsp;Data-Driven Advances in Electrochemical Energy and Sensing: Artificial Intelligence Approaches from Concept to Application</span></a><a href="/article/10.1149/1945-7111/aea1c0/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Data-Driven Advances in Electrochemical Energy and Sensing: Artificial Intelligence Approaches from Concept to Application</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Data-Driven Advances in Electrochemical Energy and Sensing: Artificial Intelligence Approaches from Concept to Application" data-link-purpose-append-open="Data-Driven Advances in Electrochemical Energy and Sensing: Artificial Intelligence Approaches from Concept to Application">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small">
						<p>The intersection of machine learning (ML) and electrochemical research is catalyzing transformative advancements in energy storage and conversion technologies. This review critically examines the role of ML and deep learning (DL) in optimizing electrochemical systems, focusing on batteries, supercapacitors, fuel cells, and sensors. ML-driven approaches facilitate accelerated material discovery, precise property predictions, and enhanced device performance monitoring, surpassing conventional trial-and-error methodologies. Integrating computational materials science, including density functional theory (DFT) and molecular dynamics (MD), with ML enables predictive modelling of electrochemical processes at an unprecedented scale. However, challenges such as data heterogeneity, model interpretability, and computational cost continue to limit widespread adoption. This review identifies key strategies to overcome these barriers, including establishing standardized data repositories, developing hybrid physics-informed ML models, and implementing explainable AI (XAI) for enhanced model transparency. By addressing these challenges, ML has the potential to drive the next wave of breakthroughs in electrochemical energy storage and conversion, accelerating the transition toward a sustainable and energy-secure future.</p>
					</div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/aea1c0">https://doi.org/10.1149/1945-7111/aea1c0</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/aea1c1" class="art-list-item-title event_main-link">Physics-Based Parameterisation of a High-Power Silicon–Graphite Lithium-Ion Battery: Electrochemical Model of the Molicel P45B Cell</a><p class="small art-list-item-meta">Dickinson et al&nbsp;</p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/aea1c1/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View accepted manuscript<span class="offscreen-hidden">,&nbsp;Physics-Based Parameterisation of a High-Power Silicon–Graphite Lithium-Ion Battery: Electrochemical Model of the Molicel P45B Cell</span></a><a href="/article/10.1149/1945-7111/aea1c1/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Physics-Based Parameterisation of a High-Power Silicon–Graphite Lithium-Ion Battery: Electrochemical Model of the Molicel P45B Cell</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Physics-Based Parameterisation of a High-Power Silicon–Graphite Lithium-Ion Battery: Electrochemical Model of the Molicel P45B Cell" data-link-purpose-append-open="Physics-Based Parameterisation of a High-Power Silicon–Graphite Lithium-Ion Battery: Electrochemical Model of the Molicel P45B Cell">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small">
						<p>A comprehensive, teardown-led parameterisation is developed for an electrochemical model of the Molicel P45B, a 4.5 Ah high-power lithium-ion cell with 21700 cylindrical form factor. Parameters are supplied in BPX JSON format, supporting Single Particle Model (SPM) and Doyle-Fuller-Newman (DFN) “Newman-style” models. In continuation of the authors’ previous dissemination of an equivalent circuit model (ECM) of the same cell, detailed insights into the cell’s internal design are presented and compared to prior studies; this includes cell overall design and bill-of-materials, electrode masses and dimensions, and active material morphology and chemistry. The negative electrode is a graphite–SiOx blend and, by contrast to legacy parameterisation work, is described in the model using separately parameterised graphite and Si additive components which contribute in parallel to electrode charge capacity and current. Further, the Si-containing additive is described by an empirical, electrode-specific hysteresis model. Critical reported parameters utilise tuning for best predictive description of full cell voltage measurements, with comparison to values obtained from electrochemical measurements on harvested electrode samples from teardown. The parameterisation is validated holistically using application-relevant pulse and continuous-current data, across the full operating envelope of temperature, state-of-charge, and operating current.</p>
					</div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/aea1c1">https://doi.org/10.1149/1945-7111/aea1c1</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/aea1c2" class="art-list-item-title event_main-link">Thermo-Electrochemical Analysis of Cylindrical Cell Format Effects on Extreme Fast Charging of Li-Ion Batteries</a><p class="small art-list-item-meta">Yasrebi et al&nbsp;</p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/aea1c2/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View accepted manuscript<span class="offscreen-hidden">,&nbsp;Thermo-Electrochemical Analysis of Cylindrical Cell Format Effects on Extreme Fast Charging of Li-Ion Batteries</span></a><a href="/article/10.1149/1945-7111/aea1c2/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Thermo-Electrochemical Analysis of Cylindrical Cell Format Effects on Extreme Fast Charging of Li-Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Thermo-Electrochemical Analysis of Cylindrical Cell Format Effects on Extreme Fast Charging of Li-Ion Batteries" data-link-purpose-append-open="Thermo-Electrochemical Analysis of Cylindrical Cell Format Effects on Extreme Fast Charging of Li-Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small">
						<p>Extreme fast charging (XFC) of lithium-ion batteries is essential for reducing electric vehicle charging time. However, the influence of cylindrical cell format on thermo-electrochemical behavior under XFC remains insufficiently understood. This study employs a validated coupled airflow–electrochemical–thermal model to systematically investigate the charging performance of 18650, 21700, 26650, and 46120 cells at charge rates of 3C–6C. The analysis evaluates heat generation, temperature distribution, charging characteristics, lithium deposition potential, and lithiation behavior. Results indicate that the average volumetric heat generation rate is weakly affected by cell format, while cell format significantly influences thermal behavior, with larger cells exhibiting substantially higher peak temperatures and internal temperature gradients. These trends are primarily attributed to differences in convective surface-to-volume ratio, heat accumulation, and temperature-dependent changes in overall cell resistance. At 3C charge rate, change of format from 18650 to 46120 raises peak temperature by ~10°C and increases the maximum internal temperature difference by a factor of 4.65. Larger formats also achieve higher state-of-charge levels during the constant-current charging stage and exhibit reduced susceptibility to lithium plating. The findings highlight the critical role of cell geometry in determining XFC performance and provide practical guidance for designing next-generation high-energy battery systems and effective thermal management strategies.</p>
					</div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/aea1c2">https://doi.org/10.1149/1945-7111/aea1c2</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/aea1c3" class="art-list-item-title event_main-link">Modification and Application of Circular Electrode with Rotatory Flow Field for Vanadium Redox Flow Batteries</a><p class="small art-list-item-meta">Guo et al&nbsp;</p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/aea1c3/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View accepted manuscript<span class="offscreen-hidden">,&nbsp;Modification and Application of Circular Electrode with Rotatory Flow Field for Vanadium Redox Flow Batteries</span></a><a href="/article/10.1149/1945-7111/aea1c3/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Modification and Application of Circular Electrode with Rotatory Flow Field for Vanadium Redox Flow Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Modification and Application of Circular Electrode with Rotatory Flow Field for Vanadium Redox Flow Batteries" data-link-purpose-append-open="Modification and Application of Circular Electrode with Rotatory Flow Field for Vanadium Redox Flow Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small">
						<p>Vanadium redox flow batteries (VRFBs) are increasingly recognized as promising candidates for large-scale energy storage, owing to their intrinsic safety, cost-effectiveness, and adaptable design. However, inadequate mass transfer and the resulting performance limitations are the main barriers to large-scale deployment and broader commercialization. In this work, a circular electrode coupled with a rotatory flow field is proposed. The main novelty of the proposed configuration lies in the coordinated design of the electrode geometry and flow-field architecture, which aims to simultaneously improve reactant distribution within the porous electrode and reduce the hydraulic penalty associated with electrolyte circulation. Numerical simulations were conducted to evaluate charge/discharge voltages, overpotential, uniformity factor, and polarization behavior for different designs. Compared with the parallel flow field, the proposed configuration improves the V²⁺ concentration uniformity factor by up to 18.27% and increases the discharge voltage by 2.24% at an applied current density of 40 mA/cm² and an inlet flow rate of 4 mL/s. Moreover, the rotatory configuration exhibits a substantially lower pressure drop than the serpentine flow field while maintaining superior electrochemical performance. These results demonstrate that the proposed circular-electrode/rotatory-flow-field coupling provides an effective strategy for simultaneously enhancing mass transport and limiting hydraulic losses in VRFBs.</p>
					</div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/aea1c3">https://doi.org/10.1149/1945-7111/aea1c3</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/aea1c4" class="art-list-item-title event_main-link">By-Product to Product: A Unified Intercalative Soft Carbon for High-Power Lithium-Ion-Based Dual Carbon Batteries</a><p class="small art-list-item-meta">Bhowmik et al&nbsp;</p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/aea1c4/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View accepted manuscript<span class="offscreen-hidden">,&nbsp;By-Product to Product: A Unified Intercalative Soft Carbon for High-Power Lithium-Ion-Based Dual Carbon Batteries</span></a><a href="/article/10.1149/1945-7111/aea1c4/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;By-Product to Product: A Unified Intercalative Soft Carbon for High-Power Lithium-Ion-Based Dual Carbon Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="By-Product to Product: A Unified Intercalative Soft Carbon for High-Power Lithium-Ion-Based Dual Carbon Batteries" data-link-purpose-append-open="By-Product to Product: A Unified Intercalative Soft Carbon for High-Power Lithium-Ion-Based Dual Carbon Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small">
						<p>The pursuit of cost-effective energy storage systems with high power and long cycle life has driven increasing interest in carbon-based dual-ion technologies. Herein, we present a by-product-to-product strategy that transforms petroleum pitch—an abundant industrial by-product—into a high-value soft-carbon framework, enabling a dual-function intercalative system in which a single precursor-derived soft carbon serves as both cathode and anode in lithium-ion-based dual-carbon batteries. As-prepared soft carbon delivers 153 mAh g-1 at a high current density of 2 A g-1 at the anode, enabled by enlarged near-surface domains that facilitate fast, reversible ion storage. Similarly, as a cathode, it delivers 55 mAh g-1 at 2 A g-1, exceeding that of a conventional graphite cathode, owing to abundant active sites and short diffusion pathways, supporting fast charging and enhanced structural stability. The dual-role intercalative behavior establishes a balanced system with a high energy density of ~114 Wh kg⁻¹ even at a high-power density of ~3665 W kg⁻¹ and a durability of 2000 cycles. This work demonstrates pitch-derived soft carbon as a unified bipolar electrode framework, advancing the design of next-generation lithium-ion batteries with high power and long life.</p>
					</div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/aea1c4">https://doi.org/10.1149/1945-7111/aea1c4</a></div></div></li></ul><!-- End AM list content --><p><a href="/journal/1945-7111/acceptedmanuscripts/1">More Accepted manuscripts</a></p><!--    accepted manuscript listing end--></div></div></div><!-- End AM tabpanel --><!-- Start Trending tabpanel --><div tabindex="0"
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae98c0" class="art-list-item-title event_main-link">Towards Optimizing Li-ion Battery Fast Charging: A Strategy and a Validation Framework</a><p class="small art-list-item-meta">Mark W. Verbrugge and Daniel R. Baker 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 170515 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae98c0/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Towards Optimizing Li-ion Battery Fast Charging: A Strategy and a Validation Framework</span></a><a href="/article/10.1149/1945-7111/ae98c0/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Towards Optimizing Li-ion Battery Fast Charging: A Strategy and a Validation Framework</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Towards Optimizing Li-ion Battery Fast Charging: A Strategy and a Validation Framework" data-link-purpose-append-open="Towards Optimizing Li-ion Battery Fast Charging: A Strategy and a Validation Framework">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This study focuses on the fast charging of lithium-ion cells with porous graphite electrodes while avoiding lithium plating. We demonstrate that by using a linearized version of the model equations, an optimization problem can be formulated, which bounds the maximum current density and ensures that the open-circuit potential at the graphite surface remains above a critical threshold. Based on these insights, we propose a new charging strategy evaluated using the full cell model, which initiates charging at the maximum allowable constant current (CC) before transitioning to a constant value for the open-circuit potential (CU) at the electrode-electrolyte interface. This CC-CU method is compared to various pulse charging protocols, the results of which are consistent with the proposed strategy providing a good estimate for the optimal charge rate for common use conditions.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae98c0">https://doi.org/10.1149/1945-7111/ae98c0</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/aea028" class="art-list-item-title event_main-link">Effects of an Induced Temperature Gradient on the Performance and Degradation of LFP/AG Cylindrical Cells</a><p class="small art-list-item-meta">Kate Leslie <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 170513 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/aea028/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Effects of an Induced Temperature Gradient on the Performance and Degradation of LFP/AG Cylindrical Cells</span></a><a href="/article/10.1149/1945-7111/aea028/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Effects of an Induced Temperature Gradient on the Performance and Degradation of LFP/AG Cylindrical Cells</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Effects of an Induced Temperature Gradient on the Performance and Degradation of LFP/AG Cylindrical Cells" data-link-purpose-append-open="Effects of an Induced Temperature Gradient on the Performance and Degradation of LFP/AG Cylindrical Cells">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Thermal management of Li-ion cells within battery packs for stationary energy storage and electric vehicles is critical to ensure longevity. Cells within packs are often heated or cooled using a thermal plate underneath the pack, which could lead to non-uniform temperature in the cells. To test the effects of temperature gradients on LFP/graphite cylindrical cells, a specialized cell holder was designed to apply a constant temperature to the top of a cell and a different constant temperature to the bottom. Temperatures of 30 °C–40 °C, 25 °C–45 °C, and 15 °C–55 °C were applied to the bottom and tops of the cells, respectively, and verified using an infrared camera. Cells were cycled at a variety of rates for approximately six months, and the capacity loss was compared between the different conditions. For most conditions there was no difference in the capacity fade based on temperature gradient and performance closely matched that of cells tested at a constant temperature of 35 °C. Thermal modelling of the jelly roll suggests that the temperature gradient does not penetrate deeply into the jelly roll due to the excellent axial thermal conductivity and this can explain the independence of capacity loss on the magnitude of the applied temperature gradient.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/aea028">https://doi.org/10.1149/1945-7111/aea028</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae94f0" class="art-list-item-title event_main-link">Comparative Benchmarking of a Next-Generation Automotive 4695 Cylindrical Lithium-Ion Cell Against Tesla’s 4680</a><p class="small art-list-item-meta">Denis Düzgün <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 170510 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae94f0/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Comparative Benchmarking of a Next-Generation Automotive 4695 Cylindrical Lithium-Ion Cell Against Tesla’s 4680</span></a><a href="/article/10.1149/1945-7111/ae94f0/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Comparative Benchmarking of a Next-Generation Automotive 4695 Cylindrical Lithium-Ion Cell Against Tesla’s 4680</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Comparative Benchmarking of a Next-Generation Automotive 4695 Cylindrical Lithium-Ion Cell Against Tesla’s 4680" data-link-purpose-append-open="Comparative Benchmarking of a Next-Generation Automotive 4695 Cylindrical Lithium-Ion Cell Against Tesla’s 4680">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Growing demand for high-energy lithium-ion batteries in electric vehicles has accelerated the adoption of large-format 46xx cylindrical cells as a route to higher energy density and improved pack-level efficiency. Tesla’s 4680 cell established an early benchmark. Since then, the 46xx landscape has expanded, with developments reported by manufacturers such as EVE Energy, BAK Battery, Gotion, Lishen and Panasonic. However, independent like-for-like datasets on cell performance, design and materials remain limited. Here, we examine a recently introduced state-of-the-art 4695 cylindrical lithium-ion cell using cell-level electrical characterization, thermal analysis and teardown. The results are compared with previously published data on Tesla’s 4680 cell. The 4695 cell exhibits an advanced internal design with complex current-collector disks and a mandrel-free jelly roll composed of double-sided, uniformly coated electrodes separated by two separator layers. Post-mortem analysis indicates a nickel-rich NCMA cathode and a graphite anode containing ∼3 wt.% silicon. Compared with the 4680 reference cell, the 4695 cell shows approximately 50% lower direct-current resistance and achieves 744 Wh L<sup>−1</sup> and 276 Wh kg<sup>−1</sup>, corresponding to energy densities about 15% higher. GC-MS indicates EC, EMC and DMC as the main electrolyte solvents, while additional detected compounds suggest EP, FEC and PC.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae94f0">https://doi.org/10.1149/1945-7111/ae94f0</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae9990" class="art-list-item-title event_main-link">Optimised Pulse-Fitting for Robust Time-Domain Impedance Analysis of Automotive Lithium-Ion Cells under Application-Specific Pulse Conditions</a><p class="small art-list-item-meta">Rico Klink <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 170509 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9990/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Optimised Pulse-Fitting for Robust Time-Domain Impedance Analysis of Automotive Lithium-Ion Cells under Application-Specific Pulse Conditions</span></a><a href="/article/10.1149/1945-7111/ae9990/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Optimised Pulse-Fitting for Robust Time-Domain Impedance Analysis of Automotive Lithium-Ion Cells under Application-Specific Pulse Conditions</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Optimised Pulse-Fitting for Robust Time-Domain Impedance Analysis of Automotive Lithium-Ion Cells under Application-Specific Pulse Conditions" data-link-purpose-append-open="Optimised Pulse-Fitting for Robust Time-Domain Impedance Analysis of Automotive Lithium-Ion Cells under Application-Specific Pulse Conditions">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>A pulse-fitting methodology for time-domain analysis of lithium-ion battery impedance is presented and systematically extended to address automotive-relevant measurement constraints under controlled test conditions, including non-ideal current profiles, limited stabilization times, measurement noise, low sampling frequencies, and SOC-dependent OCV contributions. Since no universally applicable test pulse exists for large-format automotive lithium-ion cells, pulse-based diagnostics require evaluation methods that remain robust under application-specific excitation conditions. In this work, a pulse-fitting methodology for time-domain analysis of lithium-ion battery impedance is systematically extended. The approach models the voltage response to current pulses using a physically motivated RC network, enabling the extraction of diffusion-related time constants without relying on frequency-domain techniques. Key enhancements include numerical convolution for non-ideal current profiles, incorporation of a dynamic open-circuit voltage, Tikhonov regularisation, and weighting and scaling strategies to improve robustness against noise and low sampling frequencies. Furthermore, a quadratic programming solver is introduced to increase stability for ill-conditioned problems, and an extrapolation method is proposed to account for insufficient voltage stabilization times. The methodology is validated using both synthetic and experimental pulse data, demonstrating reliable access to low-frequency impedance characteristics. The results highlight the potential of the approach for advanced state estimation and model development.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9990">https://doi.org/10.1149/1945-7111/ae9990</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae9c72" class="art-list-item-title event_main-link">The Impact of Cobalt Substitution in Lithiated Spinel/Layered Li<sub>2</sub>(MnNi)<sub>1−<i>δ/2</i></sub>Co<i><sub>δ</sub></i>O<sub>4</sub> (0 ⩽ <i>δ</i> ⩽ 0.667) Cathodes for Li-Ion Batteries</a><p class="small art-list-item-meta">Subhadip Mallick <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 170508 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9c72/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Impact of Cobalt Substitution in Lithiated Spinel/Layered Li2(MnNi)1−δ/2CoδO4 (0 ⩽ δ ⩽ 0.667) Cathodes for Li-Ion Batteries</span></a><a href="/article/10.1149/1945-7111/ae9c72/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Impact of Cobalt Substitution in Lithiated Spinel/Layered Li2(MnNi)1−δ/2CoδO4 (0 ⩽ δ ⩽ 0.667) Cathodes for Li-Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Impact of Cobalt Substitution in Lithiated Spinel/Layered Li2(MnNi)1−δ/2CoδO4 (0 ⩽ δ ⩽ 0.667) Cathodes for Li-Ion Batteries" data-link-purpose-append-open="The Impact of Cobalt Substitution in Lithiated Spinel/Layered Li2(MnNi)1−δ/2CoδO4 (0 ⩽ δ ⩽ 0.667) Cathodes for Li-Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>In 2020, the discovery of the lithiated spinel Li<sub>2</sub>MnNiO<sub>4</sub> opened the door to the design of a new class of cathode materials for the lithium-ion battery industry. This compound is typically prepared in air at 400 °C and co-exists with a disordered layered structure of the same composition (LiMn<sub>0.5</sub>Ni<sub>0.5</sub>O<sub>2</sub>), delivering most of its capacity (∼200 mAh g<sup>−1</sup>) between 4.8 and 3.0 V with essentially no redox on the manganese ions. This communication reports the effects of cobalt substitution on the structural and electrochemical properties of lithiated-spinel/layered Li<sub>2</sub>(MnNi)<sub>1−<i>δ/2</i></sub>Co<i><sub>δ</sub></i>O<sub>4</sub> composite electrodes over the compositional range 0 ⩽ <i>δ</i> ⩽ 0.667.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9c72">https://doi.org/10.1149/1945-7111/ae9c72</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae9df5" class="art-list-item-title event_main-link">Understanding the Limits of Voltage-Based Parametrization of DFN Models</a><p class="small art-list-item-meta">Yibo Wen and Daniel Schröder 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 170506 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9df5/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Understanding the Limits of Voltage-Based Parametrization of DFN Models</span></a><a href="/article/10.1149/1945-7111/ae9df5/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Understanding the Limits of Voltage-Based Parametrization of DFN Models</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Understanding the Limits of Voltage-Based Parametrization of DFN Models" data-link-purpose-append-open="Understanding the Limits of Voltage-Based Parametrization of DFN Models">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Voltage data are widely used for the parametrization of mathematical models for batteries, e.g. for the Doyle–Fuller–Newman (DFN) model. However, the information content and the resulting practical identifiability of the model parameters is currently insufficiently understood. We gain deeper understanding by using a combined framework of global sensitivity analysis and a Jacobian-based method. Balancing the open circuit potential of the electrodes was first used to establish a thermodynamically consistent baseline for the lithium-ion battery model. Then, multi-start fitting showed that low-C-rate voltage-based parametrization remains ambiguous, with distinct parameter sets yielding similarly good voltage fits. Sobol analysis of the full parameter set further revealed that the sensitivity of the voltage-based objective is strongly condition-dependent, with different C-rate conditions and state-of-charge windows emphasizing different subsets of parameters. Jacobian singular value analysis showed that the parameter-to-voltage mapping is strongly anisotropic and effectively low-rank, meaning that the parameters are only weakly linked to the original data. Our results show that voltage-based DFN parametrization is governed by a reduced and excitation-dependent information structure. Practical parametrization should therefore be understood as the identification of a physically consistent and predicatively useful parameter subspace rather than the unique conservation of all information from voltage data alone.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9df5">https://doi.org/10.1149/1945-7111/ae9df5</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/aea1c1" class="art-list-item-title event_main-link">Physics-Based Parameterisation of a High-Power Silicon–Graphite Lithium-Ion Battery: Electrochemical Model of the Molicel P45B Cell</a><p class="small art-list-item-meta">Edmund J.F. Dickinson <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b></b>  </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/aea1c1/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Physics-Based Parameterisation of a High-Power Silicon–Graphite Lithium-Ion Battery: Electrochemical Model of the Molicel P45B Cell</span></a><a href="/article/10.1149/1945-7111/aea1c1/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Physics-Based Parameterisation of a High-Power Silicon–Graphite Lithium-Ion Battery: Electrochemical Model of the Molicel P45B Cell</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Physics-Based Parameterisation of a High-Power Silicon–Graphite Lithium-Ion Battery: Electrochemical Model of the Molicel P45B Cell" data-link-purpose-append-open="Physics-Based Parameterisation of a High-Power Silicon–Graphite Lithium-Ion Battery: Electrochemical Model of the Molicel P45B Cell">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>A comprehensive, teardown-led parameterisation is developed for an electrochemical model of the Molicel P45B, a 4.5 Ah high-power lithium-ion cell with 21700 cylindrical form factor. Parameters are supplied in BPX JSON format, supporting Single Particle Model (SPM) and Doyle-Fuller-Newman (DFN) “Newman-style” models. In continuation of the authors’ previous dissemination of an equivalent circuit model (ECM) of the same cell, detailed insights into the cell’s internal design are presented and compared to prior studies; this includes cell overall design and bill-of-materials, electrode masses and dimensions, and active material morphology and chemistry. The negative electrode is a graphite–SiOx blend and, by contrast to legacy parameterisation work, is described in the model using separately parameterised graphite and Si additive components which contribute in parallel to electrode charge capacity and current. Further, the Si-containing additive is described by an empirical, electrode-specific hysteresis model. Critical reported parameters utilise tuning for best predictive description of full cell voltage measurements, with comparison to values obtained from electrochemical measurements on harvested electrode samples from teardown. The parameterisation is validated holistically using application-relevant pulse and continuous-current data, across the full operating envelope of temperature, state-of-charge, and operating current.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/aea1c1">https://doi.org/10.1149/1945-7111/aea1c1</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae9409" class="art-list-item-title event_main-link">Analysis of the Stabilizing Effect of Ca on the Durability of Sodium Ni–Fe–Mn Layered Oxides</a><p class="small art-list-item-meta">Rebecca Wilhelm <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 160520 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9409/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Analysis of the Stabilizing Effect of Ca on the Durability of Sodium Ni–Fe–Mn Layered Oxides</span></a><a href="/article/10.1149/1945-7111/ae9409/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Analysis of the Stabilizing Effect of Ca on the Durability of Sodium Ni–Fe–Mn Layered Oxides</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Analysis of the Stabilizing Effect of Ca on the Durability of Sodium Ni–Fe–Mn Layered Oxides" data-link-purpose-append-open="Analysis of the Stabilizing Effect of Ca on the Durability of Sodium Ni–Fe–Mn Layered Oxides">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Sodium-ion batteries are emerging as a viable alternative to lithium-ion batteries, particularly for cost-sensitive applications. A key component for such batteries is a durable cathode active material based on abundant and cost-effective resources. NaNi<sub>1/3</sub>Fe<sub>1/3</sub>Mn<sub>1/3</sub>O<sub>2</sub> has shown promise due to its excellent cycling stability and relatively high energy density in cells with hard carbon anodes. The addition of Ca to NaNi<sub>1/3</sub>Fe<sub>1/3</sub>Mn<sub>1/3</sub>O<sub>2</sub> has been shown to improve processability by reducing its sensitivity to moisture. Here, we investigate the stabilizing role of calcium in NaNi<sub>1/3</sub>Fe<sub>1/3</sub>Mn<sub>1/3</sub>O<sub>2</sub>. Specifically, we identify the location of calcium within cathode active material particles using X-ray photoelectron spectroscopy, examine gas evolution during operation with online electrochemical mass spectrometry, and evaluate the influence of calcium on cycling stability, material degradation, and internal resistance evolution in full-cells with a Na reference electrode at two different upper cutoff voltages, 3.9 V and 4.1 V. The stability enhancements are most pronounced at 3.9 V, leading to reduced capacity fading over 1000 cycles and suppressed cathode impedance build-up. Our findings demonstrate that reactive sodium metal—even when used only as reference electrode with a small surface area—can skew full-cell testing due to detrimental side reactions involving sodium alkoxides formed on the sodium metal surface.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9409">https://doi.org/10.1149/1945-7111/ae9409</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae9991" class="art-list-item-title event_main-link">A Novel Multi-Channel Online Electrochemical Mass Spectrometer for Battery Gas Analysis Applied to Electrolyte Additive Screening</a><p class="small art-list-item-meta">Michael MacDonald <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 170501 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9991/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;A Novel Multi-Channel Online Electrochemical Mass Spectrometer for Battery Gas Analysis Applied to Electrolyte Additive Screening</span></a><a href="/article/10.1149/1945-7111/ae9991/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;A Novel Multi-Channel Online Electrochemical Mass Spectrometer for Battery Gas Analysis Applied to Electrolyte Additive Screening</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="A Novel Multi-Channel Online Electrochemical Mass Spectrometer for Battery Gas Analysis Applied to Electrolyte Additive Screening" data-link-purpose-append-open="A Novel Multi-Channel Online Electrochemical Mass Spectrometer for Battery Gas Analysis Applied to Electrolyte Additive Screening">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>A novel multi-channel Online Electrochemical Mass Spectrometer was built to quantify gases in up to six battery cells for the study of interfacial gas generating reactions in alkali-ion cells. It measures an integral signal of the total evolved/consumed gases by sampling each cell once per hour using an automated switching sequence of computer-controlled valves optimized to remove residual gases from the central gas line connecting the six cells without affecting the vacuum chamber containing the quadrupole mass analyzer. It is demonstrated that the new multi-OEMS system enables reproducible gassing studies on machine-made double-sided graphite electrodes since the evolved gas volume easily exceeds the electrode pore volume, so that sluggish gas diffusion around the solid current collector can be avoided. Multi-OEMS can be used for rapid electrolyte additive screening as demonstrated for common CO<sub>2</sub> forming additives like VC and FEC, C<sub>2</sub>H<sub>4</sub> forming additives like DTD, and novel additives like EC-bisDTD, a polycyclic compound combining EC and DTD, that can suppress gas generation. The multi-sampling approach accelerates systematic gassing experiments and still resolves interfacial gas generating reactions at relevant timescales for alkali-ion cells.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9991">https://doi.org/10.1149/1945-7111/ae9991</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/aea0bb" class="art-list-item-title event_main-link">Electrolyte Design Enables Improved Capacity Retention of LiFePO4 Cells with Both Graphite and Silicon-Carbon Composite Anodes</a><p class="small art-list-item-meta">Thitiphum Sangsanit <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b></b>  </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/aea0bb/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Electrolyte Design Enables Improved Capacity Retention of LiFePO4 Cells with Both Graphite and Silicon-Carbon Composite Anodes</span></a><a href="/article/10.1149/1945-7111/aea0bb/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Electrolyte Design Enables Improved Capacity Retention of LiFePO4 Cells with Both Graphite and Silicon-Carbon Composite Anodes</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Electrolyte Design Enables Improved Capacity Retention of LiFePO4 Cells with Both Graphite and Silicon-Carbon Composite Anodes" data-link-purpose-append-open="Electrolyte Design Enables Improved Capacity Retention of LiFePO4 Cells with Both Graphite and Silicon-Carbon Composite Anodes">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>LiFePO4 (LFP) cells show lower gravimetric and volumetric energy density than other types of Li-ion cells. To improve this, a Si-containing anode is employed in LFP cells. However, LFP cells with Si-C composites in the anode show more rapid capacity loss than cells with only graphite in the anode.  Lithium alkoxides produced a poorly passivated negative electrode surfaces in carbonate electrolytes travel to the positive electrode and cause Fe dissolution.  This Fe moves to the negative and compromises the SEI leading to Li inventory loss and capacity fade.  It is more difficult to passivate Si-C effectively in typical electrolytes due to its large volume changes.  To solve this issue, we use an electrolyte, based on the solvents sulfolane and toluene, where alkoxide production is impossible and which eliminates Fe dissolution from LFP.  LFP/Si-C cells with sulfolane:toluene electrolytes show excellent capacity retention, much better than cells with traditional carbonate electrolytes.  Alkoxide-suppressing additives were also explored in this work, and 10% FEC in an EC-free electrolyte also showed promising results. This will open the way to employ a Si-C–containing anode in LFP cells to achieve higher gravimetric and volumetric energy density without sacrificing lifetime.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/aea0bb">https://doi.org/10.1149/1945-7111/aea0bb</a></div></div></li></ul><!--    articleEntryList end--><p><a href="/nsearch?currentPage=1&amp;terms=&amp;nextPage=2&amp;previousPage=-1&amp;searchDatePeriod=anytime&amp;journals=1945-7111&amp;accessType=open-access&amp;orderBy=newest&amp;pageLength=20">More Open Access articles</a></p></div></div></div><!-- End Open Access tabpanel --><!-- Start Spotlights tabpanel --><!-- End Spotlights tabpanel --><!-- MostCited tabpanel --><div tabindex="0"
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.2358294" class="art-list-item-title event_main-link">Comment on “Trends in the Exchange Current for Hydrogen Evolution” [<i>J. Electrochem. Soc.</i>, 152, J23 (2005)]</a><p class="small art-list-item-meta">Wolfgang Schmickler and Sergio Trasatti 2006 <em>J. Electrochem. Soc.</em> <b>153</b> L31 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.2358294/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Comment on “Trends in the Exchange Current for Hydrogen Evolution” [J. Electrochem. Soc., 152, J23 (2005)]</span></a><a href="/article/10.1149/1.2358294/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Comment on “Trends in the Exchange Current for Hydrogen Evolution” [J. Electrochem. Soc., 152, J23 (2005)]</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Comment on “Trends in the Exchange Current for Hydrogen Evolution” [J. Electrochem. Soc., 152, J23 (2005)]" data-link-purpose-append-open="Comment on “Trends in the Exchange Current for Hydrogen Evolution” [J. Electrochem. Soc., 152, J23 (2005)]">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>We compare the adsorption energies calculated by Nørskov  et al. with data derived from experimental values; except for Ni and Co, which absorb hydrogen strongly, there is a linear relation. We discuss the model proposed by these authors in the light of extensive previous work and of experimental data and find it overly simplistic.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.2358294">https://doi.org/10.1149/1.2358294</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.1856988" class="art-list-item-title event_main-link">Trends in the Exchange Current for Hydrogen Evolution</a><p class="small art-list-item-meta">J. K. Nørskov <em>et al</em> 2005 <em>J. Electrochem. Soc.</em> <b>152</b> J23 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.1856988/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Trends in the Exchange Current for Hydrogen Evolution</span></a><a href="/article/10.1149/1.1856988/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Trends in the Exchange Current for Hydrogen Evolution</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Trends in the Exchange Current for Hydrogen Evolution" data-link-purpose-append-open="Trends in the Exchange Current for Hydrogen Evolution">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>A density functional theory database of hydrogen chemisorption energies on close packed surfaces of a number of transition and noble metals is presented. The bond energies are used to understand the trends in the exchange current for hydrogen evolution. A volcano curve is obtained when measured exchange currents are plotted as a function of the calculated hydrogen adsorption energies and a simple kinetic model is developed to understand the origin of the volcano. The volcano curve is also consistent with Pt being the most efficient electrocatalyst for hydrogen evolution. © 2005 The Electrochemical Society. All rights reserved.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.1856988">https://doi.org/10.1149/1.1856988</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.1441707jes" class="art-list-item-title event_main-link">Review—SEI: Past, Present and Future</a><p class="small art-list-item-meta">E. Peled and S. Menkin 2017 <em>J. Electrochem. Soc.</em> <b>164</b> A1703 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.1441707jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Review—SEI: Past, Present and Future</span></a><a href="/article/10.1149/2.1441707jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Review—SEI: Past, Present and Future</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Review—SEI: Past, Present and Future" data-link-purpose-append-open="Review—SEI: Past, Present and Future">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>The Solid-Electrolyte-Interphase (SEI) model for non-aqueous alkali-metal batteries constitutes a paradigm change in the understanding of lithium batteries and has thus enabled the development of safer, durable, higher-power and lower-cost lithium batteries for portable and EV applications. Prior to the publication of the SEI model (1979), researchers used the Butler-Volmer equation, in which a direct electron transfer from the electrode to lithium cations in the solution is assumed. The SEI model proved that this is a mistaken concept and that, in practice, the transfer of electrons from the electrode to the solution in a lithium battery, must be prevented, since it will result in fast self-discharge of the active materials and poor battery performance. This model provides [E. Peled, in “Lithium Batteries,” J.P. Gabano (ed), Academic Press, (1983), E. Peled, <i>J. Electrochem. Soc.</i>, <b>126</b>, 2047 (1979).] new equations for: electrode kinetics (i<sub>o</sub> and b), anode corrosion, SEI resistivity and growth rate and irreversible capacity loss of lithium-ion batteries. This model became a cornerstone in the science and technology of lithium batteries. This paper reviews the past, present and the future of SEI batteries.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.1441707jes">https://doi.org/10.1149/2.1441707jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.0021707jes" class="art-list-item-title event_main-link">Oxygen Release and Its Effect on the Cycling Stability of LiNi<sub>x</sub>Mn<sub>y</sub>Co<sub>z</sub>O<sub>2</sub> (NMC) Cathode Materials for Li-Ion Batteries</a><p class="small art-list-item-meta">Roland Jung <em>et al</em> 2017 <em>J. Electrochem. Soc.</em> <b>164</b> A1361 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.0021707jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Oxygen Release and Its Effect on the Cycling Stability of LiNixMnyCozO2 (NMC) Cathode Materials for Li-Ion Batteries</span></a><a href="/article/10.1149/2.0021707jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Oxygen Release and Its Effect on the Cycling Stability of LiNixMnyCozO2 (NMC) Cathode Materials for Li-Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Oxygen Release and Its Effect on the Cycling Stability of LiNixMnyCozO2 (NMC) Cathode Materials for Li-Ion Batteries" data-link-purpose-append-open="Oxygen Release and Its Effect on the Cycling Stability of LiNixMnyCozO2 (NMC) Cathode Materials for Li-Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Layered LiNi<sub>x</sub>Mn<sub>y</sub>Co<sub>z</sub>O<sub>2</sub> (NMC) is a widely used class of cathode materials with LiNi<sub>1/3</sub>Mn<sub>1/3</sub>Co<sub>1/3</sub>O<sub>2</sub> (NMC111) being the most common representative. However, Ni-rich NMCs are more and more in the focus of current research due to their higher specific capacity and energy. In this work we will compare LiNi<sub>1/3</sub>Mn<sub>1/3</sub>Co<sub>1/3</sub>O<sub>2</sub> (NMC111), LiNi<sub>0.6</sub>Mn<sub>0.2</sub>Co<sub>0.2</sub>O<sub>2</sub> (NMC622), and LiNi<sub>0.8</sub>Mn<sub>0.1</sub>Co<sub>0.1</sub>O<sub>2</sub> (NMC811) with respect to their cycling stability in NMC-graphite full-cells at different end-of-charge potentials. It will be shown that stable cycling is possible up to 4.4 V for NMC111 and NMC622 and only up to 4.0 V for NMC811. At higher potentials, significant capacity fading was observed, which was traced back to an increase in the polarization of the NMC electrode, contrary to the nearly constant polarization of the graphite electrode. Furthermore, we show that the increase in the polarization occurs when the NMC materials are cycled up to a high-voltage feature in the dq/dV plot, which occurs at ∼4.7 V vs. Li/Li<sup>+</sup> for NMC111 and NMC622 and at ∼4.3 V vs. Li/Li<sup>+</sup> for NMC811. For the latter material, this feature corresponds to the H2 → H3 phase transition. Contrary to the common understanding that the electrochemical oxidation of carbonate electrolytes causes the CO<sub>2</sub> and CO evolution at potentials above 4.7 V vs. Li/Li<sup>+</sup>, we believe that the observed CO<sub>2</sub> and CO are mainly due to the chemical reaction of reactive lattice oxygen with the electrolyte. This hypothesis is based on gas analysis using On-line Electrochemical Mass Spectrometry (OEMS), by which we prove that all three materials release oxygen from the particle surface and that the oxygen evolution coincides with the onset of CO<sub>2</sub> and CO evolution. Interestingly, the onsets of oxygen evolution for the different NMCs correlate well with the high-voltage redox feature at ∼4.7 V vs. Li/Li<sup>+</sup> for NMC111 and NMC622 as well as at ∼4.3 V vs. Li/Li<sup>+</sup> for NMC811. To support this hypothesis, we show that no CO<sub>2</sub> or CO is evolved for the LiNi<sub>0.43</sub>Mn<sub>1.57</sub>O<sub>4</sub> (LNMO) spinel up to 5 V vs. Li/Li<sup>+</sup>, consistent with the absence of oxygen release. Lastly, we demonstrate by the use of <sup>13</sup>C labeled conductive carbon that it is the electrolyte rather than the conductive carbon which is oxidized by the released lattice oxygen. Taking these findings into consideration, a mechanism is proposed for the reaction of released lattice oxygen with ethylene carbonate yielding CO<sub>2</sub>, CO, and H<sub>2</sub>O.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.0021707jes">https://doi.org/10.1149/2.0021707jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.1393348" class="art-list-item-title event_main-link">High Capacity Anode Materials for Rechargeable Sodium‐Ion Batteries</a><p class="small art-list-item-meta">D. A. Stevens and J. R. Dahn 2000 <em>J. Electrochem. Soc.</em> <b>147</b> 1271 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.1393348/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;High Capacity Anode Materials for Rechargeable Sodium‐Ion Batteries</span></a><a href="/article/10.1149/1.1393348/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;High Capacity Anode Materials for Rechargeable Sodium‐Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="High Capacity Anode Materials for Rechargeable Sodium‐Ion Batteries" data-link-purpose-append-open="High Capacity Anode Materials for Rechargeable Sodium‐Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Electrochemical techniques have been used to study the reversible insertion of sodium into hard‐carbon host structures at room temperature. In this paper we compare these results with those for lithium insertion in the same materials and demonstrate the presence of similar alkali metal insertion mechanisms in both cases. Despite the gravimetric capacities being lower for sodium than lithium insertion, we have achieved a reversible sodium capacity of 300 mAh/g, close to that for lithium insertion in graphitic carbon anode materials. Such materials may therefore be useful as anodes in rechargeable sodium‐ion batteries. © 2000 The Electrochemical Society. All rights reserved.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.1393348">https://doi.org/10.1149/1.1393348</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.3515880" class="art-list-item-title event_main-link">A Critical Review of Thermal Issues in Lithium-Ion Batteries</a><p class="small art-list-item-meta">Todd M. Bandhauer <em>et al</em> 2011 <em>J. Electrochem. Soc.</em> <b>158</b> R1 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.3515880/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;A Critical Review of Thermal Issues in Lithium-Ion Batteries</span></a><a href="/article/10.1149/1.3515880/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;A Critical Review of Thermal Issues in Lithium-Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="A Critical Review of Thermal Issues in Lithium-Ion Batteries" data-link-purpose-append-open="A Critical Review of Thermal Issues in Lithium-Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Lithium-ion batteries are well-suited for fully electric and hybrid electric vehicles due to their high specific energy and energy density relative to other rechargeable cell chemistries. However, these batteries have not been widely deployed commercially in these vehicles yet due to safety, cost, and poor low temperature performance, which are all challenges related to battery thermal management. In this paper, a critical review of the available literature on the major thermal issues for lithium-ion batteries is presented. Specific attention is paid to the effects of temperature and thermal management on capacity/power fade, thermal runaway, and pack electrical imbalance and to the performance of lithium-ion cells at cold temperatures. Furthermore, insights gained from previous experimental and modeling investigations are elucidated. These include the need for more accurate heat generation measurements, improved modeling of the heat generation rate, and clarity in the relative magnitudes of the various thermal effects observed at high charge and discharge rates seen in electric vehicle applications. From an analysis of the literature, the requirements for lithium-ion thermal management systems for optimal performance in these applications are suggested, and it is clear that no existing thermal management strategy or technology meets all these requirements.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.3515880">https://doi.org/10.1149/1.3515880</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.1850854" class="art-list-item-title event_main-link">The Impact of Elastic Deformation on Deposition Kinetics at Lithium/Polymer Interfaces</a><p class="small art-list-item-meta">Charles Monroe and John Newman 2005 <em>J. Electrochem. Soc.</em> <b>152</b> A396 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.1850854/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Impact of Elastic Deformation on Deposition Kinetics at Lithium/Polymer Interfaces</span></a><a href="/article/10.1149/1.1850854/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Impact of Elastic Deformation on Deposition Kinetics at Lithium/Polymer Interfaces</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Impact of Elastic Deformation on Deposition Kinetics at Lithium/Polymer Interfaces" data-link-purpose-append-open="The Impact of Elastic Deformation on Deposition Kinetics at Lithium/Polymer Interfaces">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Past theories of electrode stability assume that the surface tension resists the amplification of surface roughness at cathodes and show that instability at lithium/liquid interfaces cannot be prevented by surface forces alone [Electrochim. Acta, <b>40</b>, 599 (1995)]. This work treats interfacial stability in lithium/polymer systems where the electrolyte is solid. Linear elasticity theory is employed to compute the additional effect of bulk mechanical forces on electrode stability. The lithium and polymer are treated as Hookean elastic materials, characterized by their shear moduli and Poisson’s ratios. Two-dimensional displacement distributions that satisfy force balances across a periodically deforming interface are derived; these allow computation of the stress and surface-tension forces. The incorporation of elastic effects into a kinetic model demonstrates regimes of electrolyte mechanical properties where amplification of surface roughness can be inhibited. For a polymer material with Poisson’s ratio similar to poly(ethylene oxide), interfacial roughening is mechanically suppressed when the separator shear modulus is about twice that of lithium. © 2005 The Electrochemical Society. All rights reserved.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.1850854">https://doi.org/10.1149/1.1850854</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.1379565" class="art-list-item-title event_main-link">The Mechanisms of Lithium and Sodium Insertion in Carbon Materials</a><p class="small art-list-item-meta">D. A. Stevens and J. R. Dahn 2001 <em>J. Electrochem. Soc.</em> <b>148</b> A803 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.1379565/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Mechanisms of Lithium and Sodium Insertion in Carbon Materials</span></a><a href="/article/10.1149/1.1379565/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Mechanisms of Lithium and Sodium Insertion in Carbon Materials</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Mechanisms of Lithium and Sodium Insertion in Carbon Materials" data-link-purpose-append-open="The Mechanisms of Lithium and Sodium Insertion in Carbon Materials">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>In this paper, we compare the interactions of lithium and sodium with a range of carbon materials in electrochemical cells. Through wide angle <i>in situ</i> X-ray scattering studies, we demonstrate that both lithium and sodium can be inserted into the interlayer space in disordered carbon materials. This insertion process is accompanied by an increase in the interlayer spacing in these materials. Small-angle <i>in situ</i> scattering studies are presented to clearly show the insertion of lithium and sodium into nanopores within disordered hard carbons. We also show that very little, if any, sodium can be inserted into graphitic materials in contrast to the large capacity seen for lithium insertion. © 2001 The Electrochemical Society. All rights reserved.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.1379565">https://doi.org/10.1149/1.1379565</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.3483106" class="art-list-item-title event_main-link">Hydrogen Oxidation and Evolution Reaction Kinetics on Platinum: Acid vs Alkaline Electrolytes</a><p class="small art-list-item-meta">Wenchao Sheng <em>et al</em> 2010 <em>J. Electrochem. Soc.</em> <b>157</b> B1529 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.3483106/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Hydrogen Oxidation and Evolution Reaction Kinetics on Platinum: Acid vs Alkaline Electrolytes</span></a><a href="/article/10.1149/1.3483106/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Hydrogen Oxidation and Evolution Reaction Kinetics on Platinum: Acid vs Alkaline Electrolytes</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Hydrogen Oxidation and Evolution Reaction Kinetics on Platinum: Acid vs Alkaline Electrolytes" data-link-purpose-append-open="Hydrogen Oxidation and Evolution Reaction Kinetics on Platinum: Acid vs Alkaline Electrolytes">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>The kinetics of the hydrogen oxidation reaction (HOR) and hydrogen evolution reaction (HER) on polycrystalline platinum [Pt(pc)] and high surface area carbon-supported platinum nanoparticles (Pt/C) were studied in 0.1 M KOH using rotating disk electrode (RDE) measurements. After corrections of noncompensated solution resistance from ac impedance spectroscopy and of hydrogen mass transport in the HOR branch, the kinetic current densities were fitted to the Butler–Volmer equation using a transfer coefficient of <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/157/11/B1529/revision1/jes_157_11_B1529ieqn1.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><mrow><mi>α</mi><mo>=</mo><mn>0.5</mn></mrow></math></span></span>, from which HOR/HER exchange current densities on Pt(pc) and Pt/C were obtained, and the HOR/HER mechanisms in alkaline solution were discussed. Unlike the HOR/HER rates on Pt electrodes in alkaline solution, the HOR/HER rates on a Pt electrode in 0.1 M <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/157/11/B1529/revision1/jes_157_11_B1529ieqn2.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><mrow><msub><mrow><mtext>HClO</mtext></mrow><mrow><mn>4</mn></mrow></msub></mrow></math></span></span> were limited entirely by hydrogen diffusion, which renders the quantification of the HOR/HER kinetics impossible by conventional RDE measurements. The simulation of the hydrogen anode performance based on the specific exchange current densities of the HOR/HER at <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/157/11/B1529/revision1/jes_157_11_B1529ieqn3.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><mrow><mn>80</mn><mo>°</mo><mi>C</mi></mrow></math></span></span> illustrates that in addition to the oxygen reduction reaction cell voltage loss on the cathode, the slow HOR kinetics are projected to cause significant anode potential losses in alkaline fuel cells for low platinum loadings (<span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/157/11/B1529/revision1/jes_157_11_B1529ieqn4.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><mrow><mo></mo><mn>130</mn><mspace></mspace><mtext>mV</mtext></mrow></math></span></span> at <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/157/11/B1529/revision1/jes_157_11_B1529ieqn5.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><mrow><mn>0.05</mn><mspace></mspace><msub><mrow><mtext>mg</mtext></mrow><mrow><mtext>Pt</mtext></mrow></msub><mo>/</mo><msubsup><mrow><mtext>cm</mtext></mrow><mrow><mtext>anode</mtext></mrow><mrow><mn>2</mn></mrow></msubsup></mrow></math></span></span> and <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="mml"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/157/11/B1529/revision1/jes_157_11_B1529ieqn6.jpg" style="max-width: 100%;" alt="Equation or symbol description not available" align="top" role="math"></img></span><math xmlns="http://www.w3.org/1998/Math/MathML"><mrow><mn>1.5</mn><mspace></mspace><mi>A</mi><mo>/</mo><msubsup><mrow><mtext>cm</mtext></mrow><mrow><mtext>anode</mtext></mrow><mrow><mn>2</mn></mrow></msubsup></mrow></math></span></span>), contrary to what is reported for proton exchange membrane fuel cells.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.3483106">https://doi.org/10.1149/1.3483106</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/abd60e" class="art-list-item-title event_main-link">Review—Localized High-Concentration Electrolytes for Lithium Batteries</a><p class="small art-list-item-meta">Xia Cao <em>et al</em> 2021 <em>J. Electrochem. Soc.</em> <b>168</b> 010522 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/abd60e/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Review—Localized High-Concentration Electrolytes for Lithium Batteries</span></a><a href="/article/10.1149/1945-7111/abd60e/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Review—Localized High-Concentration Electrolytes for Lithium Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Review—Localized High-Concentration Electrolytes for Lithium Batteries" data-link-purpose-append-open="Review—Localized High-Concentration Electrolytes for Lithium Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>The conventional LiPF<sub>6</sub>/carbonate-based electrolytes have been widely used in graphite (Gr)-based lithium (Li) ion batteries (LIBs) for more than 30 years because a stable solid electrolyte interphase (SEI) layer forms on the graphite surface and enables its long-term cycling stability. However, few of these electrolytes are stable under the more stringent conditions needed with a Li metal anode (LMA) and other anodes, such as silicon (Si), which exhibit large volume changes during charge/discharge processes. Many different approaches have been developed lately to stabilize Li metal batteries (LMBs) and Si-based LIBs. From this aspect, localized high-concentration electrolytes (LHCEs) have unique advantages: not only are they stable in a wide electrochemical window, they can also form stable SEI layers on LMA and Si anode surfaces to enable their long-term cycling stability. The ultrathin SEI layer formed on a Gr anode can also improve the safety and high-rate operation of conventional LIBs. In this paper, we give a brief summary of our recent work on LHCEs, including their design principle and applications in both LMBs and LIBs. A perspective on the future development of LHCEs is also discussed.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/abd60e">https://doi.org/10.1149/1945-7111/abd60e</a></div></div></li></ul><!--    articleEntryList end--></div></div></div><!-- End Featured tabpanel --></div><!-- End Article listing tabs --><!--  Start of google banners in the middle.  --><section aria-label="Main column advert"><div class="ad-iframe-wrap"><div id='div-gpt-ad-1562594774007-0' style='width: 728px; height: 90px; display: block;'><script>
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