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1 and Li(+) leads to LiOH precipitation at the cathode.
2 by enhancing reductant concentrations at the cathode.
3 re copper current collector from a LiFePO(4) cathode.
4 ared with an additional CP-drug layer on the cathode.
5 orming that of the benchmark Pt/C+RuO(2) air-cathode.
6  (003) plane in a single-crystalline Ni-rich cathode.
7 us carbon nanofibers thin film (Se@NPCFs) as cathode.
8 ron transfer from a low-cost stainless steel cathode.
9 ut from undesirably low water content in the cathode.
10 high-mass-loaded LiNi(0.8)Co(0.1)Mn(0.1)O(2) cathode.
11 ed and undamaged cells was observed over the cathode.
12  mass loading (12 mg cm(-2) ) LiCoO(2) (LCO) cathode.
13  capacities as a sodium-ion or potassium-ion cathode.
14 ting Li-metal and the LLZTO layer contacting cathode.
15 rly for the oxygen reduction reaction at the cathode.
16 he generation and use of hydrogen gas at the cathode.
17 le electrochemical activity were used as the cathode.
18 ages of degradation of electrolytes near the cathode.
19 ue to the production of hydroxyl ions at the cathode.
20 tric operation) at the anode and H(2) at the cathode.
21 y the reduction of oxygen or peroxide at the cathode.
22 Coulombic efficiencies of both the anode and cathode.
23 ccessfully demonstrated by employing dry air cathode.
24 density of batteries with intercalation-type cathodes.
25 le interface compatibility with sulfur-based cathodes.
26 an boost the capacity of lithium-ion battery cathodes.
27  and LiNi(0.8) Mn(0.1) Co(0.1) O(2) (NMC811) cathodes.
28 ectively addressing the drawbacks of Li(2) S cathodes.
29 s an efficient catalytic additive for sulfur cathodes.
30 ical behaviors in single-crystalline Ni-rich cathodes.
31 tions, such as amorphization than Na-layered cathodes.
32 nd volumetric capacity comparable to sulphur cathodes.
33 ment of novel high-energy and high-stability cathodes.
34 are fundamental to oxygen-reducing microbial cathodes.
35 y upon lithium removal and uptake in the NFA cathodes.
36  highlighting their promise as high capacity cathodes.
37 nsition metal antisite defects in Li-layered cathodes.
38 odes were also comparable to those with Pt/C cathodes.
39 ith redox couples for air-stable Na(x)TmO(2) cathodes.
40 h demonstrated in Li metal anode and thick S cathode (4.5 mg cm(-2) ) with a low electrolyte/sulfur r
41 ned carbon nanofiber (CNF)/SR layer-by-layer cathode, a flexible dendrite-free alkali-ion battery is
42       Furthermore, using the catalyst as the cathode, a spontaneous Galvanic Zn-CO(2) cell and a sola
43 e and 3D-printed GA decorated with MnO(2) as cathode achieves a remarkable energy density of 0.65 mWh
44  using S-rGO with polyoxometalate (POM) as a cathode-active material for a rechargeable battery.
45  only slightly trails NMCAM and a commercial cathode after 1000 deep cycles.
46      However, understanding of the nature of cathode-air interfacial reactions remain elusive.
47        It is classically well perceived that cathode-air interfacial reactions, often instantaneous a
48                In conventional intercalation cathodes, alkali metal ions can move in and out of a lay
49 ycling stability over pristine Se or DPTS as cathode alone.
50                               The N-C-CoO(x) cathode also showed good stability over 100 hours of ope
51                                   The hybrid cathode also shows a high Coulombic efficiency of over 9
52 n system was built utilizing V(2)O(5) as the cathode and 1 M Mg(ClO(4))(2) electrolyte within acetoni
53 s of a graphene oxide/platinum nanoparticles cathode and a polyaniline anode in Fe(2+)/Fe(3+) redox e
54 t 85% faradaic efficiency with a Muntz brass cathode and an Inconel anode.
55 sures singular intercalation of Na into both cathode and anode electrodes during cycling, which is of
56 s a high energy density of 210 Wh kg(-1) (of cathode and anode mass) and a low capacity decay rate of
57                                          The cathode and anode simultaneously generate the correspond
58                                          The cathode and anode were separated by a porous solid elect
59 h energy density of 212 Wh/kg (based on both cathode and anode) and maitain 95.3% of the capacity ove
60 , thick, 3D-structured electrodes (V(2) O(5) cathode and Li metal anode) are realized through a combi
61 ns regarding the electrochemistry of S-based cathode and of K metal anode, as well as the holistic as
62 the performance fade issue of single-crystal cathode and provides new insights for improved design of
63 rgy-dependent path length difference between cathode and sample.
64        The use of graphite felt for both the cathode and the anode was key to ensuring chemoselectivi
65 ectrolyte, the corrosion problem between the cathode and the solid electrolyte is overcome.
66 ery, using the protected anode, a 4 V Li-ion cathode, and a commercial carbonate electrolyte, shows c
67 resses transition metal dissolution from the cathode, and ensures singular intercalation of Na into b
68 raises the cation-insertion potential in the cathode, and it depresses the anion-insertion potential
69 lcohol-potassium hydroxide gel as the anode, cathode, and solid-state electrolyte, respectively.
70 h both lithium metal anodes and high voltage cathodes, and can be regulated by manipulating the solva
71 g various anionic intercalation mechanism of cathodes, and the reactions at the anodes including inte
72 ergy-density batteries with a LiCoO(2) (LCO) cathode are of significant importance to the energy-stor
73 working mechanism of the K-ion storage in Se cathode are reported using both experimental and computa
74                                              Cathodes are discussed next, focusing on the role of sul
75 g, but also adds extraneous volume since SOA cathodes are fully lithiated.
76  theoretical analyses reveal that Li-layered cathodes are more resistant to radiation-induced structu
77 t be addressed if high-voltage intercalating cathodes are to be used in such batteries.
78 and nitrite oxidation, which results in high cathode areal capacities (~12 mAh cm(-2)).
79                                          Air cathode Assisted Iron Electrocoagulation (ACAIE) overcom
80 at operate with an alkaline anode and acidic cathode at 500 mA.cm(-2) with a total electrolysis volta
81 Li@MCMB-F) anode with a commercial LiFePO(4) cathode at the positive/negative (P/N) capacity ratio of
82                                              Cathodes based on layered LiMO(2) are the limiting compo
83                                              Cathodes based on MOF-1992 and carbon black (CB) display
84              The dominant populations in the cathode biofilms were shaped by the cathode materials.
85 s the rich battery chemistry of Li-insertion cathodes but also broadens the understanding of alkali m
86 ge hysteresis can be avoided in oxygen-redox cathodes by forming materials with a ribbon superstructu
87 og Na(1.88) Mn[Fe(CN)(6) ](0.97) .1.35H(2) O cathode can be coupled to construct a full ANIB, deliver
88     Here we show that the charging rate of a cathode can be dramatically increased via interaction wi
89                                      The LCO cathode can deliver a high specific capacity of ~190 mAh
90                               As a promising cathode candidate, imide compounds have attracted extens
91 ay for modification of high-capacity Li-rich cathode candidates.
92 d transition metal dissolution dominates the cathode capacity fading.
93 d that these materials can be applied as the cathode catalyst for Li-O(2) battery operations with a r
94                           A highly efficient cathode catalyst for rechargeable Li-CO(2) batteries is
95                               The N-C-CoO(x) cathode catalyst was also paired with a very low loading
96    Loaded with a cobalt phthalocyanine-based cathode catalyst, the hybrid electrode achieves a CO Far
97 esults demonstrate that facet engineering of cathode catalysts could be a new way to tune the formati
98 roach to the development of highly efficient cathode catalysts for metal-CO(2) batteries and beyond.
99 ed remarkable progress in exploring PGM-free cathode catalysts for the oxygen reduction reaction (ORR
100 ies of {111} or {100} facets were adopted as cathode catalysts in Li-O(2) batteries with a tetra(ethy
101 cycle life due to the lack of earth-abundant cathode catalysts that can drive both oxygen reduction a
102 iscussion of different design strategies for cathode catalysts to enhance conversion efficiency and s
103 ponses (relatively stronger DeltaBR) whereas cathode caudad caused an efferent pattern (stronger Delt
104                                              Cathode cephalad polarity caused an afferent pattern of
105 cing clean catholyte into an initially empty cathode chamber through the process of electro-osmostic
106 h Li ions contributing stable cycling as the cathode charge carrier, the K ion working as charge carr
107 les sorbed onto appropriately functionalized cathodes charged to low cell potentials (-0.58 V vs Ag/A
108 e electrolytes and the diversified anode and cathode chemistries therein.
109 he incompatibility between the anode and the cathode chemistry limits the used of Mg as an anode.
110 htening to look back at the evolution of the cathode chemistry that made the modern lithium-ion techn
111 mising role as a high-capacity Li-containing cathode, circumventing use of metallic lithium in constr
112                         We show further that cathode coatings composed of cation selective membranes
113 y of dominant species in the Mo(2)N and Pt/C cathode communities belonged to Stenotrophomonas nitriti
114 cular anode was subsequently combined with a cathode consisting of a polymeric cobalt phthalocyanine
115  stage of research, the potential that these cathodes could have as viable candidates in next-generat
116 e as-prepared selenium-carbon (Se@Co(SA)-HC) cathodes deliver a high discharge capacity, a superior r
117 e LiNi(0.6) Co(0.2) Mn(0.2) O(2) (NCM(622) ) cathodes deliver ultrahigh energy density of 1500 Wh L(-
118 sive LiNi(0.8) Mn(0.1) Co(0.1) O(2) (NMC811) cathode, delivering a discharge capacity of 190.4 mAh g(
119                                   The sulfur cathode delivers a high reversible capacity of 891 mAh g
120 lithium-ion devices constructed using 1 as a cathode demonstrate reasonable capacity retention over 5
121  Full cells with LiNi(1/3)Mn(1/3)Co(1/3)O(2) cathodes demonstrate >92% capacity retention over 500 cy
122                            Here we propose a cathode design concept to achieve good Li-S pouch cell p
123    In a model LiNi(1/3) Mn(1/3) Co(1/3) O(2) cathode, dislocation-mediated ion diffusion is kinetical
124 ulfonate, EMIM-Tf, effectively separates the cathode display from the biosensing anode, protecting it
125  the Prussian Blue colour change because the cathode does not operate below 0 V vs Ag/AgCl at any tim
126 llumination of a voltage-biased plasmonic Ag cathode during CO(2) reduction results in a suppression
127 rption of oxygen intermediates on the carbon cathode during discharge.
128          The deficient sodium in the P2-type cathode easily induces the bad structural stability at d
129              Furthermore, when employed as a cathode electrocatalyst for zinc-air batteries, PcCu-O(8
130 o dendrite-free Li deposition and reversible cathode electrochemistry.
131 catalyst and for the building of fluoridized cathode-electrolyte interphases, protecting both the ele
132 st potential of the pH gradient layer at the cathode/electrolyte interface.
133 e (LiNi(0.8) Co(0.1) Mn(0.1) O(2) , NCM 811) cathodes exhibit 99.6-99.9% Coulombic efficiencies, high
134 t with a 3D-printed Li anode and a LiFePO(4) cathode exhibits a high capacity of 80 mA h g(-1) at a c
135                                   The hybrid cathode exhibits superior cycling stability over pristin
136 luorinated organic lean electrolyte, the C/S cathode experiences a solid-state lithiation/delithiatio
137  and anion in a transition metal oxide based cathode for a Li-ion battery, has garnered much attentio
138  manganese(II, III) oxide (Mn(3) O(4) ) as a cathode for aqueous dual-ion batteries.
139 nal channels can serve as a freestanding air cathode for flexible solid-state Zn-air batteries withou
140 (2) (NMC) layered compounds are the dominant cathode for lithium ion batteries.
141 alt (LirNMC) layered material is a promising cathode for lithium-ion batteries thanks to its large en
142 ithium (Li) metal anode and the high-voltage cathode for long-life, high-energy-density rechargeable
143 al design of three major categories of oxide cathodes for lithium-ion batteries, and a personal persp
144  oxides and their use as high-energy-density cathodes for lithium-ion batteries.
145        In the search for high energy density cathodes for next-generation lithium-ion batteries, the
146 itical to realizing high-performance P2-type cathodes for sodium-ion batteries.
147 ger Li(+) compared to a cell with a pristine cathode, for example, from ~1 to 1.84 for a charging vol
148 i-ion de-intercalation, rather than a direct cathode-gas chemical reaction.
149 oying iron ions catalyst based gas diffusion cathodes, (GDCs).
150                                          The cathode generated a stoichiometric amount of syngas with
151  tests demonstrated that the Mo(2)N nanobelt cathodes had similar catalytic activities for H(2) evolu
152                   Single-crystalline Ni-rich cathode has a great potential to address the challenges
153                 However, progress of Li(2) S cathode has been plagued by its intrinsic drawbacks, inc
154 ggish oxygen reduction reaction (ORR) at the cathode has remained a longstanding challenge and requir
155                                     Selenium cathodes have attracted considerable attention due to hi
156 tu grown FeP/Fe(2) O(3) nanoparticles as the cathode in a flexible Zn-air battery (ZAB).
157 ed the structural evolution of a Ni-rich NMC cathode in a solid-state cell by in situ transmission el
158 ion-storage chemistries of the anode and the cathode in dual-ion batteries (DIBs) by allowing the ano
159 ysts for the oxygen reduction reaction (ORR) cathode in proton-exchange-membrane fuel cells remains a
160 nefits and restrictions of employing the air cathode in superoxide-based batteries.
161 olytes, and shows promising performance as a cathode in Zn-air and Li-air batteries.
162 port requirements for high-energy reversible cathodes in aqueous electrochemical cells.
163 been carefully investigated at glassy carbon cathodes in dimethylformamide containing 0.10 M tetra-n-
164 y affect electrochemical behaviors of sulfur cathodes in terms of liquid-species clustering, reaction
165   The accumulation of hydroxyl ions near the cathode increased the local solution pH, which promoted
166  electron-extraction layer at the perovskite/cathode interface.
167        Bathocuproine (BCP) is a well-studied cathode interlayer in organic photovoltaic (OPV) devices
168 sulated inside a microporous carbon, and the cathode is a Zn-insertion Prussian blue, Zn(3)[Fe(CN)(6)
169                                          The cathode is composed of uniformly embedded ZnS nanopartic
170 escape of oxygen from LiCoO(2) even when the cathode is cycled to 4.62 V.
171      Now, a highly reversible iodine plating cathode is presented that operates on the redox couples
172 ides, the electrochemical kinetics of sulfur cathode is significantly accelerated.
173                        Although using an air cathode is the goal for superoxide-based potassium-oxyge
174  high-performance single-crystalline Ni-rich cathode is very challenging, notwithstanding a fundament
175          Developing high capacity and stable cathodes is a key to successful commercialization of aqu
176 -K) alloy anode and gallium (Ga)-based alloy cathodes is demonstrated.
177 thium iron aluminum nickelate (NFA) class of cathodes, is introduced.
178 ing with tunable conductivity contacting the cathode-is implemented to intercept dendrites, control i
179  the valence state over large regions of the cathodes, it was found that the phase change is size-dep
180 e of low viscosity allows practically useful cathode mass loading up to ~16 mg cm(-2) .
181 CA and NMC, this study opens a new space for cathode material development for next-generation high-en
182 ical transformation reaction to be used as a cathode material for an aluminum-ion battery with a conf
183 bilized C/S composite renders it a promising cathode material for high-energy and long-cycle-life LSB
184  1.0 A g(-1) vs. 0.1 A g(-1) ) as an organic cathode material for lithium-ion batteries.
185  attracted considerable attention as a novel cathode material for potential use in rechargeable lithi
186 ble the atomistic imaging of Li-ions in this cathode material in kinetic states and provide an experi
187 ayered Li(2)RuO(3) is an important candidate cathode material in rechargeable lithium ion batteries b
188  nanowire (DPTS-Se) organic-inorganic hybrid cathode material is presented for rechargeable lithium b
189                    Pairing with a commercial cathode material LiNi(0.6)Mn(0.2)Co(0.2)O(2), full cells
190                                       If the cathode material used in a lithium-ion or sodium-ion bat
191 model of oxygen exchange in a representative cathode material, La(0.5)Sr(0.5)CoO(3-delta), and predic
192 r for the next generation sodium-ion battery cathode material, Na(2)Mn(2)FeO(6), is described.
193                      Herein, a novel Li-rich cathode material, O3-type Li(0.6) [Li(0.2) Mn(0.8) ]O(2)
194 rally for cells containing nickel-containing cathode materials (e.g., LiNi(x)Mn(y)Co(z)O(2); NMCs), a
195                  High-energy Li-rich layered cathode materials (~900 Wh kg(-1) ) suffer from severe c
196 equent collapse of the host structure of the cathode materials and sluggish kinetics of aluminum ion
197 nt study gives oxalate a role as a family of cathode materials and suggests a direction for the ident
198                                      Li-rich cathode materials are of significant interest for coupli
199  is the highest capacity among all COF-based cathode materials for all-solid-state LIBs reported so f
200 ased covalent organic framework (COF-TRO) as cathode materials for all-solid-state LIBs.
201 ational design of high-performance MOF-based cathode materials for efficient energy storage and conve
202 account when designing high-capacity layered cathode materials for high-voltage lithium-ion batteries
203  layered oxides are among the most promising cathode materials for Li-ion batteries with high theoret
204                               Single-crystal cathode materials for lithium-ion batteries have attract
205 m-rich layered oxides (LLOs) are prospective cathode materials for next-generation lithium-ion batter
206 to advance the development of both anode and cathode materials for sodium-ion batteries (SIBs).
207 metal compounds is crucial for the design of cathode materials in aqueous electrochemical cells.
208  a Li-metal anode and state-of-the-art (SOA) cathode materials is a promising path to develop inheren
209 ) (x) (-) (y) Co(x) Al(y) O(2) (NCA) are the cathode materials of choice for next-generation high-ene
210 However, Na- or K-ion batteries have limited cathode materials that can deliver stably large capacity
211 ith the possible solutions in the pursuit of cathode materials with high voltage, fast kinetics, and
212 grees C, comprising a mixture of Fe and LiCl cathode materials, a Li anode, a garnet-type Li-ion cera
213 bserved in nickel-rich layered oxide battery cathode materials, causing unsatisfactory high-voltage c
214            Transition-metal dissolution from cathode materials, manganese in particular, has been hel
215 or the design of the next generation battery cathode materials.
216 ss the instability of highly charged layered cathode materials.
217 ay shed light on the design of Li(2) S-based cathode materials.
218 the nonviability of insulating frameworks as cathode materials.
219 s in the cathode biofilms were shaped by the cathode materials.
220 eports suggests that O(2)-reducing microbial cathodes may be more sensitive to toxic shocks than anod
221 eatment suggests that electron uptake from a cathode might involve different mechanism(s) than those
222 atteries (MIBs) to be used commercially, new cathodes must be developed that show stable reversible M
223  comparing two closely related intercalation cathodes, Na(0.75)[Li(0.25)Mn(0.75)]O(2) and Na(0.6)[Li(
224 dium content (0.85) and plateau-free P2-type cathode-Na(0.85) Li(0.12) Ni(0.22) Mn(0.66) O(2) (P2-NLN
225 sition metal oxide (TMO) lithium-ion battery cathode nanomaterial, lithium cobalt oxide (LCO), on the
226 ctrolytes can be used with a Ni-rich layered cathode (NMC 811) to obtain over 100 cycles at a C/5 rat
227  LiNi(1-) (x) (-) (y) Mn(x) Al(y) O(2) (NMA) cathode of desirable electrochemical properties is demon
228 ctroscopy) study of a sputtered thin film Ag cathode on a Ge ATR crystal in CO(2)-saturated 0.1 M KHC
229 ) anode with an anion-intercalation graphite cathode, operating well over a wide discharge rate range
230 tions are either applying a coating layer on cathode or modifying the electrolyte chemistry.
231 y efficiency and cycling stability as an air-cathode, outperforming that of the benchmark Pt/C+RuO(2)
232 on for designing high-energy-density Li-rich cathode oxides with stable l-OR chemistry.
233 ensation to achieve high capacity in Li-rich cathode oxides.
234 he anode and 316 stainless steel (SS) as the cathode placed in a bench-scale electrochemical reactor.
235 preventing the consequent dissolution of the cathode-plated iodine as triiodides.
236 fe of lithium-sulfur batteries by decreasing cathode porosities from 70 to 40%.
237             Finally, we predict an optimized cathode porosity to maximize the cell level volumetric e
238 tteries, less attention has been paid to the cathode porosity, which is much higher in sulfur/carbon
239 d to a coplanar 3 x 15 mm Prussian Blue, PB, cathode printed over a transparent poly(3,4-ethylenediox
240   The product is produced at high yield (the cathode product consists of > 98% CNTs).
241 ing voltage when paired with essentially any cathode, promising a high cell-level energy density.
242 the capacities of devices using 2-SO(4) as a cathode rapidly diminish over several cycles due to the
243   The oxygen reduction reaction (ORR) is the cathode reaction in fuel cells and its selectivity for w
244                         However, polyanionic cathodes reported so far rely heavily upon transition-me
245 solid polymer electrolytes, and high-voltage cathodes represent promising candidates for next-generat
246 (pH > 12.9) regions around the anode and the cathode, respectively.
247 ovide a straightforward method for enhancing cathode reversibility by preventing anion cross-over in
248 )) and oxygen (O(2)) streams to an anode and cathode separated by a porous solid electrolyte, wherein
249 tion, cyclic voltammetry analysis of anammox cathode showed a redox peak centered at -140 mV Vs Ag/Ag
250                         Disordered rock salt cathodes showing both anionic and cationic redox are bei
251 state NaFe(II)Fe(III)(CN)(6) (Prussian Blue) cathode, showing approximately an order-of-magnitude gre
252  transport layer and expels electrons toward cathode side, which reduces the charge recombination the
253 t use of a surface-functionalized (oxidized) cathode significantly increased the electrosorption rati
254 s is determined by the superstructure in the cathode, specifically the local ordering of lithium and
255                          Conventional Li-ion cathodes store charge by reversible intercalation of Li
256                                          Our cathode structure shows improved performances in a pouch
257 ffusion pathways of Li-ions as they traverse cathode structures in the course of insertion reactions
258 rochemical performance reported for advanced cathode structures.
259                     Current state-of-the-art cathodes such as LiNi(1/3)Mn(1/3)Co(1/3)O(2) rely on red
260                       However, the developed cathodes suffer from sluggish Zn(2+) diffusion kinetics,
261 , discharge capacity, discharge voltage, and cathode sulfur content are systematically analyzed to st
262           Powered by an applied voltage, the cathode supplied enough reducing equivalents to support
263 u from pyridine (Py) in acidified water at a cathode surface and to be the key to selective CO(2) pho
264 thin disordered rocksalt layer formed on the cathode surface can effectively mitigate the surface deg
265                          The local pH on the cathode surface is 7.2, and the HCO(3)(-) concentration
266  on direct cell contact via a biofilm on the cathode surface rather than through secreted intermediat
267 with the thin film sensor directly from SOFC cathode surface via proposed spring-based wire connectio
268 tly binds directly with the electron rich Ni cathode surface without breaking the aromaticity of the
269 ch is much higher in sulfur/carbon composite cathodes than in traditional lithium-ion battery electro
270   Here, we report an O3-NaCr(2/3)Ti(1/3)S(2) cathode that delivers a high reversible capacity of ~186
271  4 V, which prevents the use of high-voltage cathodes that promise higher energy densities.
272  Using Ag (220 nm) instead of Al (100 nm) as cathode, the champion PCE was further improved to 17.6%.
273 homogeneous reactions of high-energy-density cathodes, the development of safe and reversible Li meta
274 strates were functionalized as the anode and cathode through electrochemical deposition of palladium
275 stable lithium (Li) metal batteries with LCO cathode, through the design of in situ formed, stable el
276 can be coupled with a potassium cobalt oxide cathode to achieve dendrite healing in a practical full-
277 ery is designed for a Li-ion-insertion-based cathode to deliver stable high capacity using a Na-K liq
278 ode to take in anions and a cation-deficient cathode to host cations, thus operating as a reverse dua
279 Li(3) N-LiF/Li(3) PS(4) SSE enables LiCoO(2) cathodes to achieve 101.6 mAh g(-1) for 50 cycles.
280 he current research aims at finding suitable cathodes to achieve proof-of-concept for a full Ca batte
281 synthesize highly effective bifunctional air cathodes to be applied in electrochemical energy devices
282 ceiving considerable interest as alternative cathodes to conventional oxides due to their advantages
283 CH) in aqueous solution over skeletal nickel cathodes to probe the various paths of reductive catalyt
284                      Metal-organic framework cathodes usually exhibit low capacity and poor electroch
285 and atomistic simulation, we reveal that the cathode-water interfacial reactions can lead to the surf
286 ode, and the generation of dihydrogen at the cathode were monitored.
287 4% vs. 70%) of MECs with the Mo(2)N nanobelt cathodes were also comparable to those with Pt/C cathode
288 e, inexpensive and efficient Mo(2)N nanobelt cathodes were prepared using an ethanol method with mini
289 trapped in the bulk structure of the charged cathode, which is reduced on discharge.
290                 High-energy nickel (Ni)-rich cathode will play a key role in advanced lithium (Li)-io
291  sulfur deposition enhances stability of the cathode with 99.0% capacity remaining (194 mA h g(-1)) a
292  performance is achieved as a Li-ion battery cathode with a high reversible capacity (387 mA h g(-1)
293 n MWCNT coated GCE (GCE|BOx) was used as the cathode with direct electron transfer (DET).
294 on derived V(2) O(5) can be an excellent ZIB cathode with high capacity and exceptional cycle stabili
295                           The iodine plating cathode with the theoretical capacity of 211 mAh g(-1) p
296 microstructures evolve in Na- and Li-layered cathodes with 3d transition metals.
297         Mechanically stable and foldable air cathodes with exceptional oxygen reduction reaction (ORR
298  iron phosphate (LFP) batteries in which LFP cathodes with high capacity (5 to 10 mAh/cm(2)) are pair
299 interphases on both the Li anode and the LCO cathode, with an advanced electrolyte, are reported.
300 de and a Li(+) extraction from an oxide host cathode without electrolyte oxidation in a high-voltage

 
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