| sample_id,doi,problem_statement,hypothesis,problem_core,problem_type_broad,problem_type_fine,battery_system,component,failure_mode_or_limitation,intervention_or_solution,mechanism_or_rationale,target_property,claimed_outcome,evidence_strength,novelty_axis,keywords,keywords_compact,num_reasoning_steps,reasoning_process |
| 0,10.1021/acsmaterialsau.4c00136,,,The fundamental bottleneck is the absence of a clear mechanistic link between polyoxotungstate heteroatom chemistry and their temperature-dependent redox thermodynamics.,Mechanistic Understanding,redox entropy tuning by heteroatom substitution,unknown,redox-active polyoxotungstate molecular electrolyte species,insufficient understanding of how heteroatom substitution affects redox thermodynamics and temperature-dependent electrochemical behavior,,,redox entropy and redox potential thermodynamics,,moderate,new mechanistic insight,polyoxotungstate | heteroatom substitution | redox entropy | variable-temperature open-circuit potential | VT-OCP | variable-temperature cyclic voltammetry | cyclic voltammetry | E1/2 | dielectric continuum function | solvation effects | charge-state dependence | nonaqueous electrolyte | acetonitrile | molecular redox thermodynamics | electronic structure tuning,polyoxotungstate | redox entropy | heteroatom substitution | VT-OCP | VT-CV | solvation | E1/2,6, |
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| 1,10.1016/j.chempr.2021.09.012,,,,Multi-factor System Tradeoff,digitalization sustainability tradeoff,unknown,chemical R&D and manufacturing data/infrastructure ecosystem,,,,system-level sustainability and transparency of digitalized chemical manufacturing,,moderate,system-level digital sustainability framework,digitalization of chemistry | chemical manufacturing | value-chain transparency | raw data access | blockchain | traceability | AI and machine learning | robotic laboratories | high-performance computing | smart devices and sensors | circular design | life cycle assessment | e-waste | reskilling and upskilling | sustainable chemicals,digital chemistry | transparency | blockchain traceability | AI-enabled R&D | robotic labs | circular electronics | life cycle assessment,6,"[Begin Step 1] The passage starts from the premise that digitalization can improve chemistry by expanding access to raw data, enabling collaboration, and helping identify manufacturing bottlenecks. [End Step 1] |
| [Begin Step 2] It then identifies a first bottleneck: insufficient transparency and traceability across the chemical value chain, especially for compounds and restricted materials, which limits oversight and broad data-enabled innovation. [End Step 2] |
| [Begin Step 3] A second bottleneck is organizational rather than purely technical: digitalized R&D and manufacturing require new skills in data handling, AI/ML, and robotic infrastructure, so workforce capability becomes a limiting factor for adoption. [End Step 3] |
| [Begin Step 4] A third bottleneck is environmental: more sensors, smart devices, processors, and batteries increase resource extraction and e-waste, creating a risk that digitalization itself imposes significant environmental costs. [End Step 4] |
| [Begin Step 5] The proposed solution is therefore a combined system-level intervention consisting of transparent data access, secure exchange and traceability using tools such as blockchain, workforce reskilling/upskilling, and circular life cycle-based infrastructure design. [End Step 5] |
| [Begin Step 6] The causal logic is that transparency exposes bottlenecks, skilled personnel can use AI and robotics productively, and circular management of hardware reduces resource and waste impacts; together these changes allow digitalization to improve chemical innovation and sustainability without its infrastructure burden cancelling the intended benefits. [End Step 6]" |
| 2,10.1149/2.0381701jes,"Practical lithium-sulfur batteries are limited by low sulfur loading in the cathode, which suppresses areal capacity and prevents realization of high cell-level energy density despite sulfur's high theoretical specific capacity. Conventional cathode architectures using planar current collectors provide insufficient pore volume and transport pathways for heavily loaded sulfur electrodes, so achieving >200 Wh/kg at pouch-cell level becomes difficult.","Applying a 3D mass-producible aluminum foam current collector together with a high-solids S/KB slurry using CMC+SBR binder to a lithium-sulfur cathode addresses low sulfur loading and limited areal capacity because the porous foam and better-dispersed binder enable dense composite filling with large cathode pore volume and effective ionic/electronic pathways, thereby improving sulfur loading and areal capacity and making >200 Wh/kg cell-level energy density plausible.",The fundamental bottleneck is packing enough electrochemically utilizable sulfur into a practical Li-S cathode to achieve high areal capacity and meaningful pouch-cell energy density.,Performance Optimization,low sulfur loading and insufficient areal capacity,lithium-sulfur battery,cathode current collector and sulfur cathode architecture,low sulfur loading in the cathode leading to low sulfur-loading ratio and insufficient areal capacity for practical energy density,"Use of a 3D structured aluminum foam current collector filled with a sulfur/Ketjenblack composite slurry, especially a high-solids CMC+SBR-bound slurry, to build a high-loading sulfur cathode in a pouch cell.","The 3D aluminum foam provides a thick porous scaffold that can host substantially more S/KB composite than a planar foil while maintaining conductive pathways and internal pore volume for ion transport. The CMC+SBR binder enables a higher-solids slurry than PVdF, so more active material is deposited per filling step and the foam is more effectively loaded, increasing sulfur loading. The resulting large pore volume and 3D architecture support more effective sulfur utilization at high loading and can kinetically retard dissolved polysulfide migration by trapping species within the cathode structure.",sulfur loading and areal capacity,unprecedentedly high areal capacity in a single-layer pouch-type Li-S cell and plausible achievement of >200 Wh/kg estimated energy density,strong,scalable 3D current-collector design,lithium-sulfur battery | aluminum foam current collector | 3D structured cathode | high sulfur loading | areal capacity | sulfur/Ketjenblack composite | CMC+SBR binder | high-solids slurry | pouch-type full cell | polysulfide trapping | glyme-based electrolyte | mass-producible metal foam | pore volume | cell-level energy density | sulfur utilization,Li-S battery | Al foam | high sulfur loading | areal capacity | CMC+SBR | 3D cathode | polysulfides | energy density,7,"[Begin Step 1] Lithium-sulfur batteries have intrinsically high theoretical energy density, but practical deployment is constrained because cathodes usually contain too little sulfur per unit area to translate sulfur's gravimetric capacity into cell-level energy density. [End Step 1] |
| [Begin Step 2] Prior sulfur cathodes commonly have areal sulfur loadings below about 2 mg cm−2, and low sulfur-loading ratio in the total cathode mass can make the resulting battery energy density lower than that of conventional lithium-ion batteries. [End Step 2] |
| [Begin Step 3] A key design requirement is therefore a cathode architecture that can accommodate much more sulfur without losing electronic connectivity and ion-accessible space. [End Step 3] |
| [Begin Step 4] The authors select industrially available 3D aluminum foam as the current collector/support so the porous framework can be filled with sulfur/carbon composite throughout its volume rather than only coated on a flat surface. [End Step 4] |
| [Begin Step 5] They further use a CMC+SBR binder because it permits a higher-solids slurry than PVdF, allowing more composite to be introduced per filling step and yielding substantially higher sulfur loading in the foam. [End Step 5] |
| [Begin Step 6] The combination of high loading, conductive carbon, and relatively large cathode pore volume is inferred to preserve sulfur utilization and support ion/electron transport even at thick electrode loading; the 3D structure may also kinetically retard polysulfide migration by repeatedly trapping dissolved species within the cathode region. [End Step 6] |
| [Begin Step 7] Consequently, the Al-foam/CMC+SBR cathode achieves very high areal capacity in a pouch cell, and when that areal capacity is translated to a multilayer pouch-battery model with specified E/S assumptions, the projected gravimetric energy density exceeds 200 Wh kg−1. [End Step 7]" |
| 3,10.1039/d3ra05684h,"Disordered rocksalt cathodes for lithium-ion batteries offer high theoretical capacity and improved sustainability, but their practical capacity remains limited by poor Li+ transport, low electronic conductivity, and rapid capacity fading. In Mn/Ti-based DRX cathodes, these coupled limitations restrict rate capability and cycling stability, hindering commercial viability.","Applying combined O-to-F substitution, particle-size reduction, and carbon surface coating to Mn/Ti-based disordered rocksalt cathodes addresses poor realizable capacity and cycling instability because fluorination increases Li-rich 0-TM percolation environments and suppresses oxygen loss, while smaller particles shorten Li+ diffusion lengths and carbon coating lowers charge-transfer resistance, thereby improving Li+ transport, conductivity, reversible capacity, rate capability, and cycling stability.","The fundamental bottleneck is that Mn/Ti-based DRX cathodes cannot realize their high theoretical capacity because sluggish Li+ percolation, poor electronic transport, and oxygen-redox-induced instability limit reversible electrochemistry.",Multi-factor System Tradeoff,poor Li+ percolation and oxygen-loss-driven capacity fading,lithium-ion battery,DRX cathode,"restricted short- and long-range Li+ diffusion, low electrical conductivity, and irreversible oxygen loss causing poor capacity retention","Combined fluorination of the oxygen sublattice in Li1.3Mn0.4Ti0.3O1.7F0.3, post-synthesis particle-size reduction by ball milling, and carbon coating on particle surfaces","Fluorine substitution increases local Li enrichment around F− and raises the population of Li-rich 0-TM tetrahedral clusters, which improves short-range Li+ percolation in the DRX lattice. Ball-milling reduces particle size and thus shortens long-range Li+ diffusion pathways, while carbon coating improves electronic transport by lowering charge-transfer resistance. Fluorination also shifts charge compensation toward transition-metal redox and away from lattice oxygen, reducing irreversible oxygen loss and improving reversibility and structural stability.","Li+ diffusion/percolation kinetics, charge-transfer resistance, and oxygen-redox reversibility","higher realizable discharge capacity, improved rate capability, and better cycling stability with suppressed irreversible oxygen loss",strong,synergistic co-design,disordered rocksalt cathode | Li-ion battery | Li1.3Mn0.4Ti0.3O1.7F0.3 | fluorine substitution | carbon coating | particle size reduction | 0-TM clusters | Li+ percolation | o-t-o diffusion | oxygen redox | oxygen loss suppression | charge-transfer resistance | rate capability | cycling stability | Mn/Ti-based cathode,DRX cathode | F substitution | carbon coating | Li+ percolation | oxygen loss | rate capability | cycling stability,7,"[Begin Step 1] DRX cathodes have high theoretical capacity because both transition-metal and oxygen redox can contribute, but their practical value is limited when transport and stability are insufficient for reversible cycling. [End Step 1] |
| [Begin Step 2] In Mn/Ti-based DRX materials, the text identifies three coupled bottlenecks: restricted Li+ diffusion in both short and long ranges, limited electrical conductivity, and oxygen-redox-driven oxygen loss that accelerates capacity fade. [End Step 2] |
| [Begin Step 3] Large as-synthesized particles worsen long-range Li+ transport because DRX Li diffusivity is intrinsically lower than in conventional layered cathodes, so reducing particle size should shorten diffusion length and improve access to active material. [End Step 3] |
| [Begin Step 4] Because efficient Li+ transport in DRX relies on interconnected Li-rich 0-TM channels, substituting O with more electronegative F is proposed to increase Li content around F− and create more 0-TM clusters, thereby enhancing short-range Li+ percolation. [End Step 4] |
| [Begin Step 5] Surface carbon coating is introduced to address the electronic bottleneck by improving electronic conductivity and lowering interfacial charge-transfer resistance during electrochemical cycling. [End Step 5] |
| [Begin Step 6] Fluorination also changes charge-compensation behavior so that more redox occurs on transition metals rather than lattice oxygen, which suppresses irreversible oxygen loss and improves reversibility and cycling stability. [End Step 6] |
| [Begin Step 7] Therefore, combining fluorination, particle downsizing, and carbon coating should simultaneously improve ionic transport, electronic transport, and oxygen-redox stability, yielding higher discharge capacity, stronger rate performance, and better capacity retention in DRX cathodes. [End Step 7]" |
| 4,10.1021/acsomega.2c02715,"Estimating evaporative VOC emissions from gasoline vehicles is limited by earlier diurnal breathing loss and refueling loss models that rely on nonphysical fitted parameters, simplified single-component fuel assumptions, and output only total evaporation rather than chemical composition. This limits transferability across environmental conditions and weakens emission inventories needed to assess ozone and secondary organic aerosol formation.","Applying thermodynamics-based multicomponent evaporation models to gasoline-vehicle diurnal breathing loss breakthrough and refueling loss addresses the poor physicality and compositional blindness of prior semi-empirical models because explicit treatment of gas expansion, liquid-to-vapor phase change, and component vapor pressures links fuel composition and temperature to emission flux and speciation, thereby improving estimation of total evaporative VOC emissions and VOC composition for inventory assessment.","The paper seeks to overcome the lack of physically grounded, composition-resolved models for gasoline-vehicle evaporative emissions under real environmental conditions.",Mechanistic Understanding,semi-empirical evaporative emission modeling,unknown,gasoline fuel tank headspace and canister breakthrough/refueling emission pathway,nonphysical regression-based and single-component assumptions causing poor universality and inability to predict VOC composition,"thermodynamics-based estimation models for DBLb and RFL using the ideal gas law, Raoult's law, Antoine/Clausius-Clapeyron vapor-pressure relations, fuel composition data, environmental temperature inputs, and a mixing parameter for DBLb","The revised DBLb model adds both headspace gas expansion and direct liquid-to-vapor phase-change contributions, rather than treating emissions as expansion of pre-existing vapor only, which corrects systematic underestimation. By resolving gasoline as a multicomponent mixture through Raoult's law and component vapor pressures, the model converts fuel composition and temperature into both total emitted moles and VOC speciation. For DBLb, a mixing coefficient accounts for incomplete short-timescale convection in the tank headspace, while for RFL the displaced vapor volume during refueling is linked directly to emitted vapor through thermodynamics.",accuracy and universality of total evaporative emission and VOC composition estimation,improved replication of DBLb and RFL experiments and more credible national/future VOC emission inventory estimates,strong,new physically grounded emission model,evaporative emissions | volatile organic compounds | diurnal breathing loss | canister breakthrough emission | refueling loss | thermodynamic model | Raoult's law | ideal gas equation | Antoine equation | gasoline composition | VOC speciation | environmental temperature dependence | multicomponent vapor pressure | emission inventory | zero-emission vehicle scenario,DBLb | RFL | VOC emissions | thermodynamic modeling | Raoult's law | gasoline vapor speciation | emission inventory,6,"[Begin Step 1] Evaporative VOC emissions from gasoline vehicles materially affect ozone and secondary organic aerosol formation, so accurate estimates of major processes such as DBL breakthrough and RFL are needed for air-quality assessment and policy. [End Step 1] |
| [Begin Step 2] Prior DBL and RFL models are limited because they treat gasoline as an averaged single component, use fitted nonphysical parameters, and only predict total evaporation, making them difficult to generalize to new fuels and temperatures and unable to provide VOC composition. [End Step 2] |
| [Begin Step 3] A more physical model should represent gasoline as a multicomponent mixture whose evaporation depends on component vapor pressures and temperature, and should separately account for the actual thermodynamic drivers of emission in each process. [End Step 3] |
| [Begin Step 4] For DBLb, the authors therefore include both gas-phase thermal expansion and additional vapor generation from liquid-gas phase change, then estimate component partial pressures with Raoult's law and vapor-pressure equations; a mixing factor is introduced because short-timescale headspace mixing is incomplete. [End Step 4] |
| [Begin Step 5] For RFL, the mechanism is simpler: vapor occupying the tank headspace is displaced during liquid refueling, so the emitted amount can be tied to refueling volume and component vapor partial pressures, allowing both total emission and VOC composition to be calculated. [End Step 5] |
| [Begin Step 6] Because these thermodynamic models are physically grounded and composition-resolved, they are expected to reproduce experiments more reliably than earlier semi-empirical formulations and to support improved national and future evaporative emission inventories under ZEV-transition scenarios. [End Step 6]" |
| 5,10.1021/jacsau.3c00035,"High-voltage lithium-metal batteries are limited by unstable electrolyte interfacial chemistry at both electrodes: conventional solvent reactions on Li metal cause low Coulombic efficiency, dendrite growth, and poor cycling, while solvent oxidation and corrosion at highly delithiated cathodes degrade high-voltage stability. Existing concentrated electrolytes that rely mainly on anion-derived interphases can still suffer from inadequate protection and sluggish ion transport, which undermines fast charging and long-cycle operation.","Applying a monofluoro-ether solvent (FDEE) in an anion-enriched concentrated/localized high-concentration electrolyte addresses interphase instability in high-voltage lithium-metal batteries because strong Li+···F-CH2 interactions restructure the solvation sheath, promote solvent-dominant LiF-rich interphase formation, and reduce excessive Li+-anion coordination, thereby improving interfacial conductivity, Li plating reversibility, and high-voltage cathode stability.",The fundamental bottleneck is that conventional anion-dominant concentrated-electrolyte chemistry cannot simultaneously provide sufficiently protective and ion-conductive interphases for both Li-metal anodes and ultrahigh-voltage cathodes.,Interface Stability,solid-electrolyte/interphase instability at high voltage,high-voltage lithium-metal battery,both electrodes and their electrode/electrolyte interphases,"insufficiently protective and poorly conductive anion-derived interphases causing solvent oxidation, side reactions, dendrite-prone Li deposition, and polarization",monofluoro-ether solvent design using FDEE in concentrated/localized high-concentration ether electrolyte,"The highly polar -CH2F group in FDEE forms strong Li+···F-CH2 interactions, which increase Li+-solvent binding, alter the solvation structure toward less intimate Li+-anion coordination, and improve ionic transport. This solvation change shifts interfacial reactivity from predominantly anion-derived chemistry to solvent-dominant FDEE decomposition, producing thin, LiF-enriched, and more conductive interphases on both the high-voltage cathode and Li-metal anode. The resulting interphases better suppress parasitic oxidation/reduction and facilitate charge transfer and Li+ conduction, which stabilizes both electrodes under high voltage and high rate.",interphase composition and ionic/charge-transfer conductivity,"suppressed interfacial side reactions and dendrite-free Li cycling, enabling higher Li Coulombic efficiency, fast-charging capability, and markedly improved cycling stability of 4.7 V-class Li-metal cells",strong,new solvent-dominant interphase design,lithium-metal battery | high-voltage cathode | NMC811 | localized high-concentration electrolyte | monofluoro ether | FDEE | solvation structure | Li+···F-CH2 interaction | solvent-dominant interfacial chemistry | LiF-rich interphase | cathode electrolyte interphase | solid-electrolyte interphase | ionic conductivity | Li Coulombic efficiency | fast charging,FDEE | Li-metal battery | solvent-dominant chemistry | LiF-rich interphase | high-voltage NMC811 | fast charging | solvation engineering,6,"[Begin Step 1] High-voltage Li-metal batteries suffer from side reactions at both electrodes: Li metal reacts with solvent to lower Coulombic efficiency and promote dendrites, while high-voltage cathodes catalyze solvent oxidation and corrosion, causing rapid performance decay. [End Step 1] |
| [Begin Step 2] Concentrated and localized high-concentration electrolytes attempt to solve this by enriching anions in the Li+ solvation sheath so that anion-derived inorganic interphases form, but the text states these interphases remain inadequate for ultrahigh-voltage cathodes and high-rate Li deposition and can also impede ion transport through strong Li+-anion coordination. [End Step 2] |
| [Begin Step 3] The design criterion is therefore to retain high oxidative stability while changing the solvation structure so that interfacial reactions produce more effective, conductive protection rather than relying solely on salt-anion decomposition. [End Step 3] |
| [Begin Step 4] Introducing the monofluoro-ether FDEE provides a highly polar -CH2F group that interacts strongly with Li+, as supported in the text by Raman, NMR, DFT, and MD analyses showing stronger Li+-solvent binding and reduced aggregate anion coordination relative to DEE and ClDEE. [End Step 4] |
| [Begin Step 5] Because FDEE participates directly in interfacial reactions, it promotes solvent-dominant formation of LiF-rich interphases on both cathode and anode; these interphases are thinner, more uniform, and more conductive, which lowers impedance, improves Li+ transport, and suppresses further parasitic decomposition and dendritic Li growth. [End Step 5] |
| [Begin Step 6] If both electrodes are protected by such conductive LiF-enriched interphases, the cell should exhibit higher Li reversibility, stable cycling at 4.6-4.7 V, and better fast-charging/high-rate operation, which the paper reports through CE, symmetric-cell, impedance, and full-cell cycling results. [End Step 6]" |
| 6,10.1016/j.heliyon.2024.e36811,"Large quantities of apple pomace generated by the fruit-processing industry remain an underutilized waste stream after biorefinery, while lead-contaminated wastewater from industrial sources requires low-cost remediation at concentrations relevant to real effluents. A key limitation is whether depleted apple waste, without chemical pretreatment, still retains sufficient surface functionality and adsorption capacity to remove Pb(II) effectively enough to support circular valorization.","Applying minimally treated and biorefined/depleted apple pomace as a biosorbent for Pb(II)-contaminated water addresses low-cost waste valorization and lead removal because residual hydroxyl-, carbonyl-, aromatic-, and carboxyl-derived surface groups together with porous structure enable Pb(II) attraction/chelation and surface adsorption, thereby improving lead uptake capacity and wastewater remediation performance.","The paper seeks to overcome the uncertainty that low-cost, non-pretreated, biorefinery-depleted apple pomace may not adsorb Pb(II) effectively enough for practical wastewater remediation.",Performance Optimization,low-cost Pb(II) biosorption from wastewater,unknown,biosorbent surface,insufficient Pb(II) adsorption capacity of untreated or biorefinery-depleted agri-food waste at realistic wastewater concentrations,"Use raw apple pomace (RA) and especially selectively extracted/depleted apple pomace (EA) from a biorefinery process, without additional physical or chemical pretreatment, as Pb(II) biosorbents.","The apple-waste sorbents retain oxygen-containing and aromatic surface functionalities, and at pH around 5 these groups become more deprotonated, increasing negative surface charge and affinity for cationic Pb2+. FTIR changes after adsorption suggest involvement of O-H, C=O, and C=C groups, consistent with a combined adsorption mechanism involving electrostatic attraction and Pb(II) chelation/coordination. The porous, hierarchical morphology of the extracted material is proposed to provide accessible binding sites and support Pb distribution on the surface.",Pb(II) adsorption capacity and removal efficiency,"Effective lead removal from water using low-cost apple-waste-derived biosorbents, with biorefinery-depleted pomace retaining adsorption performance comparable to raw pomace and supporting circular waste valorization.",strong,biorefinery waste-to-biosorbent valorization,apple pomace | biorefinery-depleted biomass | biosorbent | lead removal | Pb(II) adsorption | wastewater remediation | circular economy | FTIR functional groups | SEM hierarchical porosity | chelation | electrostatic attraction | pH-dependent adsorption | Freundlich isotherm | pseudo-second-order kinetics | maximum adsorption capacity,apple pomace | Pb(II) adsorption | biosorbent | biorefinery residue | chelation | pH effect | Freundlich isotherm,6, |
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| 7,10.1016/j.joule.2024.01.006,,,The fundamental bottleneck is achieving sustained passive evaporative cooling of PV panels without the sorbent layer itself becoming a thermal and chemical liability.,Multi-factor System Tradeoff,thermal resistance versus evaporative cooling balance,unknown,PV module back sheet / sorbent cooling module,,,,PV operating temperature / net cooling capacity under passive conditions,,moderate,system-level passive cooling co-design,photovoltaic thermal management | sorbent-based evaporative cooling | SBEC-PV | passive cooling | back-sheet temperature | latent heat of evaporation | nighttime moisture adsorption | daytime desorption | thermal resistance | adsorbent packaging | CaCl2 hydrogel sorbent | MOF adsorbents | deliquescence and salt loss | PV efficiency temperature coefficient | retrofit scalability,SBEC-PV | passive PV cooling | thermal resistance | moisture adsorption-desorption | adsorbent stability | packaging reliability | PV efficiency,6, |
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| 8,10.1016/j.xcrp.2023.101665,,,,Mechanistic Understanding,insufficient in situ spatially resolved speciation of Cu during CO2R,unknown,Cu electrocatalyst particles at the catalyst/electrolyte interface,limited spatial resolution of in situ STXM and uncertainty in active-state Cu oxidation state and morphology under CO2R,,,spatial resolution and quantitative in situ Cu oxidation-state/morphology mapping fidelity,direct identification of metallic Cu as the steady-state active catalyst below -0.2 VRHE and visualization of continued dendritic restructuring under CO2R conditions with improved image quality and reduced radiation dose,strong,new in situ spectro-ptychography platform,electrochemical CO2 reduction | copper electrocatalyst | soft X-ray spectro-ptychography | in situ spectromicroscopy | scanning transmission X-ray microscopy | Cu L3 edge | oxidation-state mapping | Cu(0)/Cu(I)/Cu(II) speciation | microfluidic electrochemical reactor | controlled electrolyte flow | morphological restructuring | dendrite growth | active catalyst state | radiation dose reduction | structure-property-performance relationship,CO2R | Cu catalyst | spectro-ptychography | in situ Cu speciation | morphology evolution | dendrite growth | Cu L-edge,6, |
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| 9,10.1088/2515-7655/abfb4a,,,,Mechanistic Understanding,insufficient operando health/degradation diagnostics,,whole cell/device,,use of acoustic emission (AE) and ultrasonic testing (UT) as non-invasive in situ/operando diagnostic tools,,,,moderate,new diagnostic insight,acoustic emission | ultrasonic testing | operando diagnostics | non-destructive evaluation | time-of-flight | acoustic impedance mismatch | state of health monitoring | degradation detection | gas evolution | particle cracking | two-phase flow | water management | electrode delamination | electrochemical power devices | failure prevention,AE | UT | operando monitoring | time-of-flight | SoH diagnostics | degradation detection | two-phase flow,6,"[Begin Step 1] Electrochemical devices are increasingly important for energy storage and conversion, but wider deployment depends on better performance, durability, safety, and state monitoring during operation. [End Step 1] |
| [Begin Step 2] Existing diagnostic methods provide valuable information but are not always sufficiently simple, low-cost, non-invasive, or practical for routine in situ and operando monitoring across real devices and use cases. [End Step 2] |
| [Begin Step 3] Internal degradation and process changes in these devices involve physical and mechanical consequences such as cracking, deformation, gas evolution, interface formation, water accumulation, and density or thickness changes. [End Step 3] |
| [Begin Step 4] Because such changes generate acoustic emissions or alter acoustic wave propagation, AE can capture spontaneous stress-release events while UT can probe evolving internal structures through amplitude and time-of-flight changes. [End Step 4] |
| [Begin Step 5] Correlating these acoustic signatures with electrochemical and structural phenomena enables identification of degradation modes, transport states, and health indicators in batteries, fuel cells, and electrolysers without destructive teardown. [End Step 5] |
| [Begin Step 6] Therefore, the paper advances the view that AE and UT are promising non-invasive diagnostic tools that can improve operando health monitoring, failure detection, and lifecycle decision support for electrochemical power devices. [End Step 6]" |
| 10,10.1016/j.isci.2023.107725,"Electrical cochlear implants are limited by broad current spread in the conductive cochlear fluid, which causes strong channel interactions and reduces the number of perceptually independent stimulation channels to well below the number of physical electrodes. This low spectral resolution constrains speech understanding in noisy environments and degrades music perception, creating a major unmet need in hearing restoration.","Applying optogenetic optical cochlear implantation with many spatially confined emitters and adapted optical sound-coding strategies to spiral ganglion neuron stimulation addresses the channel-interaction bottleneck of electrical cochlear implants because confined light delivery reduces spread of excitation and permits more independent and potentially parallel stimulation channels, thereby improving spectral resolution and expected speech intelligibility.",The paper seeks to overcome the limited spectral resolution of electrical cochlear implants caused by broad electrical current spread and resulting channel interaction in the cochlea.,Transport Limitation,broad spread of excitation / channel interaction,optical cochlear implant,intracochlear stimulation array and spiral ganglion neuron interface,Wide electrical current spread in scala tympani causes overlapping neural activation and too few perceptually independent channels.,Replace or augment electrical stimulation with optogenetic optical cochlear implants using spatially confined optical emitters (μLED- or waveguide-based) together with optical sound-coding strategies that exploit increased channel count and parallel stimulation.,"Optical stimulation can be spatially confined much more tightly than electrical current in the conductive cochlear fluid, so each emitter activates a smaller fraction of spiral ganglion neurons and reduces overlap between neighboring channels. This narrower spread of excitation increases the number of non-overlapping functional channels and enables coding strategies with more spectral bands and parallel stimulation. Ultrafast channelrhodopsins further make optical stimulation temporally viable, while adapted pulse timing and longer pulses in parallel operation accommodate their kinetic and energy constraints.",spectral selectivity and number of perceptually independent stimulation channels,"Higher spectral resolution with expected improvement in speech intelligibility, especially in complex listening environments, and potentially better music perception than electrical cochlear implants.",moderate,new stimulation modality and coding co-design,optical cochlear implant | electrical cochlear implant | optogenetic stimulation | spiral ganglion neurons | spread of excitation | spectral selectivity | channel interaction | parallel stimulation | sound coding strategy | channelrhodopsin kinetics | f-Chrimson | waveguide emitters | μLED array | speech intelligibility | fractional articulation index,optical cochlear implant | optogenetics | spread of excitation | spectral selectivity | parallel stimulation | μLED/waveguide | channelrhodopsins,7, |
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| 11,10.1016/j.polymer.2023.126064,,,The paper seeks to overcome the lack of proton exchange membranes that retain high proton conductivity together with adequate thermal and mechanical stability above 100 °C under low-humidity or dry conditions.,Transport Limitation,dehydration-induced proton conductivity loss,PEM fuel cell,proton exchange membrane electrolyte,drastic conductivity drop under anhydrous intermediate/high-temperature operation due to membrane dehydration and unstable additive-based proton conduction,,,anhydrous proton conductivity of the membrane,,strong,new protic polymer composition with anion-tuned membrane design,proton exchange membrane | PEM fuel cell | intermediate-temperature PEM | protic poly(ionic liquid) | poly(diallylmethylammonium) | cyclopolymerization | photopolymerization | counter-anion effect | mesylate anion | triflate anion | TFSI anion | anhydrous proton conductivity | thermal stability | humidity uptake | neutron scattering,PEMFC membrane | protic poly(ionic liquid) | poly(diallylmethylammonium) | anion tuning | anhydrous proton conduction | photocrosslinked membrane | intermediate-temperature PEM,7,"[Begin Step 1] Intermediate- and high-temperature PEM fuel cells are attractive because they offer improved heat/water management and reaction kinetics, but they require membranes that conduct protons effectively above 100 °C at low relative humidity. [End Step 1] |
| [Begin Step 2] Standard PFSA membranes lose conductivity when dehydrated, and many alternative high-temperature PEMs also suffer from poor mechanical/thermal properties or depend on free acids/additives that can evaporate or degrade. [End Step 2] |
| [Begin Step 3] Protic ionic liquids are known to display relatively high proton conductivity and thermal/electrochemical stability under anhydrous conditions, suggesting that incorporating their chemistry into a polymer backbone could create intrinsically proton-conducting membranes. [End Step 3] |
| [Begin Step 4] The authors therefore synthesize polymerizable protic diallylmethylammonium salts and convert them into poly(diallylmethylammonium X−) membranes, using cyclopolymerization and, for selected systems, photo-crosslinking to obtain self-standing films. [End Step 4] |
| [Begin Step 5] By changing the counter-anion, the membrane's ionicity, charge delocalization, hydrophilicity, mobility, and interionic interactions are altered; this tunes proton transport as well as mechanical and thermal behavior, with MsO−, Tf−, and TFSI− emerging as favorable balances. [End Step 5] |
| [Begin Step 6] Because the proton-donating ammonium functionality is built into the polymer, the membranes can sustain proton transport without external acids or liquid additives, while crosslinking stabilizes the structure and adjusts humidity uptake and handleability. [End Step 6] |
| [Begin Step 7] Consequently, the optimized protic membranes are expected to maintain high dry conductivity at intermediate temperatures and to function as promising PEMFC electrolytes, which is supported by conductivity, thermal, mechanical, humidity, CV, and neutron-scattering data reported in the text. [End Step 7]" |
| 12,10.1016/j.rinma.2024.100654,"Conventional aerospace materials face a persistent tradeoff between low weight and high mechanical, thermal, and electrical performance, limiting efficiency, durability, and multifunctionality in aircraft and spacecraft. The review argues that existing metals and polymer composites can be too heavy, insufficiently conductive, or inadequate for heat management and EMI shielding, which matters because these constraints affect fuel consumption, structural integrity, and system safety.","Applying carbon nanotubes as reinforcement, conductive networks, or functional coatings in aerospace composite systems addresses the weight–performance limitation because CNTs provide high aspect ratio, intrinsic mechanical strength, and efficient electrical/thermal transport pathways, thereby improving lightweight structural performance and multifunctional properties such as conductivity, thermal management, and shielding.","The paper targets the inability of conventional aerospace materials to simultaneously achieve lightweight design and high multifunctional mechanical, thermal, and electrical performance.",Multi-factor System Tradeoff,weight–strength–conductivity tradeoff,unknown,aerospace structural composites and coatings,insufficient multifunctional performance of lightweight conventional materials,"integration of carbon nanotubes into composite matrices, fiber surfaces, films, and coatings as multiscale reinforcement and conductive/thermal networks","CNTs introduce nanoscale high-aspect-ratio percolating networks that can carry load, bridge interfaces, and provide rapid electron and heat transport within otherwise less conductive polymer or composite systems. Their intrinsic strength-to-weight ratio and transport properties enable simultaneous reinforcement and multifunctional response, so embedding or grafting CNTs can raise stiffness, conductivity, thermal dissipation, and shielding effectiveness without the mass penalty of traditional metallic solutions.",specific mechanical strength and multifunctional electrical/thermal conductivity,"lighter aerospace materials with improved structural performance, thermal management, EMI shielding, and overall system efficiency",moderate,integrated multifunctional material perspective,carbon nanotubes | single-walled carbon nanotubes | multi-walled carbon nanotubes | aerospace composites | multiscale reinforcement | electrical conductivity | thermal conductivity | electromagnetic interference shielding | lightweight structural components | interfacial bonding | nano-stitching | functional coatings | damage monitoring | polymer matrix composites | thermal management,CNT | aerospace composites | multiscale reinforcement | electrical conductivity | thermal management | EMI shielding | lightweight structures,6, |
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| 13,10.1016/j.cortex.2016.04.016,,,The paper seeks to overcome the inability of conventional aphasia analyses to disentangle overlapping behavioral deficits and lesion-severity effects sufficiently to reveal unique neurocognitive dimensions and their neural correlates.,Mechanistic Understanding,confounded lesion–symptom mapping of multidimensional aphasia deficits,unknown,behavioral-neuroanatomical mapping framework in chronic post-stroke aphasia,,,,specificity and interpretability of brain–behavior factor mapping,,strong,new data-driven lesion-mapping framework,post-stroke aphasia | principal component analysis | rotated PCA | varimax rotation | voxel-based correlational methodology | lesion-symptom mapping | lesion volume covariate | speech quanta | semantic variety | phonological factor | anterior temporal lobe | superior insula | frontal aslant tract | behavioral collinearity | multidimensional deficit structure,post-stroke aphasia | PCA-VBCM | lesion-symptom mapping | speech quanta | phonology | semantics | lesion volume,7,"[Begin Step 1] Chronic post-stroke aphasia is behaviorally heterogeneous, with speech fluency, phonological, semantic, and executive impairments varying continuously across patients rather than falling into clean diagnostic categories. [End Step 1] |
| [Begin Step 2] Standard group averaging can wash out meaningful dissociations, while single-case approaches cannot provide a unified model or quantify severity–performance relationships across patients. [End Step 2] |
| [Begin Step 3] Raw speech and language measures are highly inter-correlated, and lesion location is also related to lesion size after MCA stroke, so simple lesion–behavior correlations risk reflecting shared severity rather than unique cognitive components. [End Step 3] |
| [Begin Step 4] A suitable solution is to decompose the behavioral dataset with rotated PCA so that latent, orthogonal factors represent statistically reliable and interpretable dimensions of impairment rather than overlapping test scores. [End Step 4] |
| [Begin Step 5] These orthogonal factor scores can then be entered into VBCM, and lesion volume can be added as a covariate, allowing variance due to anatomical severity to be separated from variance tied to specific behavioral dimensions. [End Step 5] |
| [Begin Step 6] Under this framework, speech variety merges with semantic ability, while speech quanta remains a distinct factor, and the omnibus model yields separable phonological, semantic, executive, and speech quanta dimensions with different lesion correlates. [End Step 6] |
| [Begin Step 7] Therefore, PCA-VBCM is proposed and demonstrated as a data-driven way to recover unique neural correlates and preserve individual differences within a coherent multidimensional model of aphasia, overcoming the confounds that limit conventional analyses. [End Step 7]" |
| 14,10.1038/srep07349,"Conventional supercapacitors face a tradeoff in which EDLC systems provide high power and long cycle life but low energy density, while pseudocapacitive systems offer higher capacitance but suffer from limited power capability and shorter cycling stability. This limitation is especially important in aqueous supercapacitor devices, where improving both capacitance and operating voltage window is necessary to raise energy density without sacrificing rate performance and durability.","Applying a rationally hybridized 3D sponge-supported rGO/metal-hydroxide electrode architecture and pairing it with an rGO negative electrode in an aqueous supercapacitor addresses the low-energy-density and power/lifetime tradeoff because the conductive porous rGO-sponge framework improves interfacial contact and electrolyte accessibility while Ni(OH)2 or Co(OH)2 adds fast redox storage, thereby increasing capacitance, extending the operating voltage window, and improving device-level energy and rate performance.",The paper seeks to overcome the intrinsic tradeoff between low-energy-density EDLC supercapacitors and higher-capacitance but poorer-rate/shorter-life pseudocapacitive systems.,Multi-factor System Tradeoff,low energy density with limited power-capability/cycle-life balance,aqueous hybrid supercapacitor,hybrid electrodes and full device electrodes,"low energy density in EDLCs together with limited power capability, poorer interfacial utilization, and shorter cycle life in pseudocapacitive electrodes","Binder-free hybrid electrodes consisting of Ni(OH)2 or Co(OH)2 nanostructures chemically bath deposited onto rGO-coated 3D macroporous sponge, combined in a hybrid device with SP@rGO as the negative electrode and SP@rGO@Ni or SP@rGO@Co as the positive electrode.","The rGO-coated sponge forms a conductive 3D macroporous scaffold that improves electrical pathways, interfacial contact, and electrolyte penetration throughout the electrode. Deposited Ni(OH)2 or Co(OH)2 nanosheets/nanoflakes introduce pseudocapacitive redox storage while the rGO contributes EDLC storage, so the hybrid electrode stores charge through dual mechanisms and more effectively utilizes both outer and inner surfaces. The porous architecture and nanochannels shorten ion diffusion paths and act as ion-buffering reservoirs, while the rGO support helps maintain electrical/mechanical integrity during cycling, enabling high-rate operation, extended voltage window in the hybrid full cell, and improved energy density.",specific capacitance and operating voltage window,enhanced energy density and power capability with good rate performance and improved cycling stability in aqueous hybrid supercapacitor devices,strong,synergistic co-design,aqueous hybrid supercapacitor | reduced graphene oxide | Ni(OH)2 nanosheets | Co(OH)2 nanoflakes | 3D macroporous sponge | chemical bath deposition | binder-free electrode | dual charge-storage mechanism | EDLC-pseudocapacitive hybridization | electrolyte accessibility | ion diffusion resistance | extended operating voltage window | specific capacitance | energy density | cycling stability,hybrid supercapacitor | rGO sponge | Ni(OH)2 | Co(OH)2 | dual charge storage | voltage window | energy density | cycling stability,7,"[Begin Step 1] The background problem is that EDLC supercapacitors deliver high power and long life but insufficient energy density, whereas pseudocapacitive electrodes provide higher capacitance yet often lose power capability and cycle life. [End Step 1] |
| [Begin Step 2] A key bottleneck is ineffective integration of carbon and pseudocapacitive materials; simple mixing gives poor interfacial contact and underutilization of active material, limiting charge transfer and rate performance. [End Step 2] |
| [Begin Step 3] A design criterion therefore emerges: the electrode should simultaneously provide conductive pathways, high accessible surface area, open ion-transport channels, and intimate contact between EDLC and redox-active components. [End Step 3] |
| [Begin Step 4] The authors implement this by coating a 3D macroporous sponge with rGO to create a conductive scaffold, then directly growing Ni(OH)2 or Co(OH)2 nanostructures on that scaffold via chemical bath deposition to form binder-free hybrid electrodes. [End Step 4] |
| [Begin Step 5] This architecture is proposed to work because the sponge/rGO network improves electrolyte penetration and electron transport, while the metal hydroxide nanosheets/nanoflakes provide redox charge storage and the rGO contributes electrostatic storage, yielding synergistic dual charge-storage behavior. [End Step 5] |
| [Begin Step 6] The mesoporous/nanochannel-rich structure reduces ion diffusion resistance and increases electroactive surface utilization, and the rGO support helps preserve electrical contact and mechanical integrity against volume changes during cycling. [End Step 6] |
| [Begin Step 7] When these hybrid positive electrodes are paired with an SP@rGO negative electrode, the device can operate over a wider aqueous voltage window, so the combined increase in capacitance and cell voltage leads to higher energy density while retaining high rate capability and good cycling stability. [End Step 7]" |
| 15,10.1021/acsami.0c13092,"Protonic ceramic solid oxide electrochemical devices are limited by poorly understood and often resistive or reactive solid–solid interfaces, including electrolyte grain boundaries, heterointerfaces, and electrode–electrolyte contacts. These interfaces govern proton transport, cation interdiffusion, and interfacial phase formation, so insufficient interfacial control hampers conductivity, durability, and overall device performance.","Applying interface-focused engineering and advanced interface-resolved characterization/modeling to protonic ceramic devices addresses interfacial resistivity and chemical reactivity because atomic-scale knowledge of grain-boundary charge, defect segregation, transport pathways, and cation interdiffusion can guide the design of heterointerfaces, electrodes, and processing routes that stabilize interfaces and improve proton transport, thereby improving conductivity, compatibility, and device performance.","The fundamental bottleneck is that solid–solid interfaces in protonic ceramic devices impose transport barriers and interfacial degradation, yet remain insufficiently understood to be rationally engineered.",Mechanistic Understanding,solid–solid interfacial resistivity and cation interdiffusion,protonic ceramic solid oxide electrochemical device,"solid–solid interfaces across electrolyte grain boundaries, heterointerfaces, and electrode/electrolyte contacts","grain-boundary proton blocking, cation interdiffusion, and growth of reactive interface phases that degrade transport and stability","advanced local interface characterization combined with ab initio/computational modeling and targeted interface engineering of grain boundaries, heterointerfaces, and composite electrodes","The review argues that interfacial structure, composition, defect segregation, and space-charge formation control local proton concentration, oxygen-vacancy distribution, and transport barriers at solid–solid contacts. By resolving these features experimentally and computationally, one can design grain boundaries and heterointerfaces that reduce carrier depletion, create preferential low-resistance proton pathways, and suppress cation interdiffusion or parasitic interphase growth, which should translate into improved conductivity and device durability.",interfacial proton transport and chemical/interface stability,improved protonic ceramic device performance and durability through rational interface design,moderate,new mechanistic interface-focused design framework,protonic ceramic devices | H-SOC | solid–solid interfaces | grain boundary resistivity | space charge layer | proton transport | cation interdiffusion | heterointerface engineering | electrode–electrolyte reactivity | triple-conducting cathodes | ab initio modeling | STEM-EELS | atom probe tomography | in situ/operando characterization | interface phase formation,protonic ceramics | grain boundaries | interface engineering | proton transport | cation interdiffusion | space charge | operando characterization,6,"[Begin Step 1] Proton-conducting solid oxide devices are promising for intermediate-temperature fuel cell and electrolysis applications, but their performance still lags because multiple internal solid–solid interfaces strongly influence transport and stability. [End Step 1] |
| [Begin Step 2] In electrolytes, grain boundaries commonly carry positive core charge and associated space-charge layers that deplete mobile protonic defects and other carriers, creating substantial grain-boundary resistivity. [End Step 2] |
| [Begin Step 3] At electrode–electrolyte and composite-electrode interfaces, cation interdiffusion and interfacial reactions can produce secondary phases, pore formation, or altered defect chemistry, which further degrade conductivity and durability. [End Step 3] |
| [Begin Step 4] Because these limitations originate from atomic-scale interfacial structure and chemistry, bulk characterization or overall device performance metrics alone are insufficient to identify the controlling mechanisms. [End Step 4] |
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