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1 ribution of Cu to buffer volume change of Sn anode.
2 ls in monolayer migrated collectively to the anode.
3 cy with a Muntz brass cathode and an Inconel anode.
4 4)(+) in solution and the composition of the anode.
5 gy density batteries offered by the Li metal anode.
6 enoxyl that are generated transiently at the anode.
7 thout chloride corrosion, especially for the anode.
8 uction in viable cells was achieved over the anode.
9 athode chemistry limits the used of Mg as an anode.
10 arresting uncontrolled polymer growth at the anode.
11 e capacity reported for any carbon-based KIB anode.
12 ensity beyond those of a commercial standard anode.
13 thode coupled to cation incorporation in the anode.
14 metal batteries using a pristine metallic Li anode.
15 dendrite growth and side reactions of the Zn anode.
16  remedy for the limited cycle life of the Zn anode.
17 hanced interfacial stability to the Li metal anode.
18 ial 74% of its capacity by pairing with such anode.
19 uppress dendrite growth with a lithium metal anode.
20 se and extend the cycle life of the Li metal anode.
21 ity in comparison with conventional graphite anodes.
22 e-fluorinated mesocarbon microbeads (MCMB-F) anodes.
23 neous plating and stripping of lithium metal anodes.
24  exemplary cyclability against lithium metal anodes.
25 terpart and the challenges faced by Na metal anodes.
26 chlorinated byproduct formation at Ti(4)O(7) anodes.
27 than reported values for boron-doped diamond anodes.
28 rther progress in the field of lithium metal anodes.
29 tion behavior towards dendrite-free Na metal anodes.
30 lems related to volume expansion of alloying anodes.
31 thium ion batteries containing lithium metal anodes.
32 tal to achieve stable and long life Li metal anodes.
33 grafted hollow carbon spheres (SHCS) for KIB anodes.
34 spectively, in a full cell) of lithium metal anodes.
35 ons in rechargeable batteries based on metal anodes.
36 d high Coulombic efficiency of lithium metal anodes.
37 oying approaches for room temperature liquid anodes.
38 h doubles that of the cell based on graphite anodes.
39 batteries compared with bare potassium metal anodes.
40 e to overcome pulverization of silicon-based anodes.
41 -salt electrolytes and aluminum oxide coated anodes.
42 wth exhibited a severe growth defect with an anode (+0.4 V(SHE)) or Fe(III)-NTA as the terminal elect
43 voltage cathodes with low-potential graphite anodes(1-4).
44     A full-cell battery, using the protected anode, a 4 V Li-ion cathode, and a commercial carbonate
45 xture of Fe and LiCl cathode materials, a Li anode, a garnet-type Li-ion ceramic electrolyte, and Mo
46     With a more stable environment for the K anode, a K-air (dry) battery delivers over 100 cycles (>
47 O nanosheets as an example, the protected Li anodes achieve Coulombic efficiency of ~99% and ultralon
48                 A high-performance potassium anode achieved by confining potassium metal into a titan
49 e significant bacterial cell damage over the anode after 24 h of electroceutical treatment.
50                                         Such anodes also deliver significantly improved electrochemic
51 r a pure magnesium (Mg) or a Mg alloy as the anode and 316 stainless steel (SS) as the cathode placed
52 asymmetric device assembled with SF-3D GA as anode and 3D-printed GA decorated with MnO(2) as cathode
53 oth dendrite-free plating of a lithium-metal anode and a Li(+) extraction from an oxide host cathode
54                             By adopting a Li anode and a Li-ion ceramic electrolyte, the corrosion pr
55 ntly, a full cell built with a 3D-printed Li anode and a LiFePO(4) cathode exhibits a high capacity o
56 lectronically insulating side contacting the anode and a partially electronically conductive (PEC) co
57 ne oxide) polymer contacts the lithium-metal anode and a poly(N-methyl-malonic amide) contacts the ca
58  electrolyzers that operate with an alkaline anode and acidic cathode at 500 mA.cm(-2) with a total e
59 7 V pouch full-cells matched with a graphite anode and an ultralean electrolyte (2 g Ah(-1) ).
60 ity of enzymes and electron mediators at the anode and by enhancing reductant concentrations at the c
61 s among the electrolytes and the diversified anode and cathode chemistries therein.
62  expected to advance the development of both anode and cathode materials for sodium-ion batteries (SI
63 rogen (H(2)) and oxygen (O(2)) streams to an anode and cathode separated by a porous solid electrolyt
64 m (NF) substrates were functionalized as the anode and cathode through electrochemical deposition of
65 prove the Coulombic efficiencies of both the anode and cathode.
66 ate the morphological evolution of the metal anode and explore the role of bulk-distortion and anchor
67 from Zn anode by coating a thin MOF layer on anode and filling the pores of MOF with hydrophobic Zn(T
68 mong the longest cycle life of lithium metal anode and five times longer than that of blank separator
69 ry employing a sodium-potassium (Na-K) alloy anode and gallium (Ga)-based alloy cathodes is demonstra
70 ar ratio at stoichiometric operation) at the anode and H(2) at the cathode.
71 oulombic efficiency of >99 % for both the Li anode and LiNi(0.8) Mn(0.1) Co(0.1) O(2) (NMC811) cathod
72 es of the IC-WiS electrolyte, the NaTiOPO(4) anode and Prussian blue analog Na(1.88) Mn[Fe(CN)(6) ](0
73  of solid-state electrolytes with a Li-metal anode and state-of-the-art (SOA) cathode materials is a
74              The incompatibility between the anode and the cathode chemistry limits the used of Mg as
75  the anion/cation-storage chemistries of the anode and the cathode in dual-ion batteries (DIBs) by al
76  and alkaline (pH > 12.9) regions around the anode and the cathode, respectively.
77 lize the highly reductive lithium (Li) metal anode and the high-voltage cathode for long-life, high-e
78 trode/electrolyte interphases on both the Li anode and the LCO cathode, with an advanced electrolyte,
79 provides dendrite-free plating of a Li-metal anode and the other allows a Li(+) extraction from an ox
80 fficiency were both demonstrated in Li metal anode and thick S cathode (4.5 mg cm(-2) ) with a low el
81 ical energy via the oxidation of fuel at the anode and usually the reduction of oxygen or peroxide at
82            Full cells made of such composite anodes and commercially available LiNi(0.6) Co(0.2) Mn(0
83 g the oxygen reduction reaction on lithiated anodes and enable good cycle performance over 1000 times
84 ave to be compatible with both lithium metal anodes and high voltage cathodes, and can be regulated b
85 sity of 212 Wh/kg (based on both cathode and anode) and maitain 95.3% of the capacity over 500 cycles
86 ported organic molecules are employed in the anode, and molecules with highly reversible capacity for
87 , the K ion working as charge carrier on the anode, and Na as the medium to liquefy K metal, such a t
88 tial (OCP), the formation of struvite on the anode, and the generation of dihydrogen at the cathode w
89  are paired with thin (50 mum) lithium metal anodes, and investigate their galvanostatic electrochemi
90 rent density, and cycle life of the solid Li anode are improved.
91 lelly aligned holey nanosheets on a Li metal anode are reported to simultaneously redistribute the Li
92                                Lithium metal anodes are not only required for the development of inno
93                                     Alloying anodes are promising high-capacity electrode materials f
94                              Potassium metal anodes are then critically reviewed, emphasizing electro
95 emical cells that utilize lithium and sodium anodes are under active study for their potential to ena
96 d electrodes (V(2) O(5) cathode and Li metal anode) are realized through a combination of imprint lit
97 electrolyte interphase (SEI) formed on an Li anode as a point of departure to discuss the structural,
98 ochemistry of S-based cathode and of K metal anode, as well as the holistic aspects of full-cell perf
99 ves to form optimal nanostructures for alloy anodes, as we show through electrochemical experiments i
100 fundamentals of ECR systems, including photo-anode-assisted ECR systems and bio-anode-assisted ECR sy
101 ing photo-anode-assisted ECR systems and bio-anode-assisted ECR systems, are explained in detail.
102 ) in the biofilm viability observed over the anode at both conditions.
103 ing to develop well-performing lithium metal anodes, because they can act as a mechanical barrier to
104 ative electroactive bacterium dominating the anode biofilm microbiomes.
105                     The highly reversible Zn anode brings a high energy density of 210 Wh kg(-1) (of
106 hway for extending lifetime of lithium metal anodes, but also sheds light on the role of separator en
107 ere, we separate aqueous electrolyte from Zn anode by coating a thin MOF layer on anode and filling t
108 ior and constructed a dendrite-free Li metal anode by elevating temperature from room temperature (20
109              We demonstrate that the K-metal anode can be coupled with a potassium cobalt oxide catho
110 xchange membrane fuel cell with Ru(7)Ni(3)/C anode can deliver a high peak power density of 2.03 W cm
111 ithium titanate anode or other intercalation anode candidates (Li(3)VO(4) and LiV(0.5)Ti(0.5)S(2))(8,
112                 Electrolyte reduction at the anode carbon active material initiates dissolution, diff
113 t 95 degrees C, surpassing that using PtRu/C anode catalyst, and good durability with less than 5% vo
114 s also paired with a very low loading PtRu/C anode catalyst, to create AEMFCs with a total PGM loadin
115 vinyl alcohol-potassium hydroxide gel as the anode, cathode, and solid-state electrolyte, respectivel
116        A self-organized core-shell composite anode, comprising an outer sheath of lithiated liquid me
117 ique is based on a 3-D double-functional bio-anode concurrently exhibiting bio-electrocatalytic energ
118  a lactate oxidase and osmium-polymer -based anode connected to a coplanar 3 x 15 mm Prussian Blue, P
119      By using the Ru(7)Ni(3)/C catalyst, the anode cost can be reduced by 85% of the current state-of
120               The use of potassium (K) metal anodes could result in high-performance K-ion batteries
121 report of successful potassium metal battery anode cycling with an aluminum-based rather than copper-
122   Consequently, the Zn@Nafion-Zn-X composite anode delivers high coulombic efficiency (ca. 97 %), dee
123                      The resultant composite anode demonstrates an excellent combination of capacity,
124               This work is a leap in silicon anode development and provides insights into the design
125 n pressing leads to highly loaded integrated anodes displaying volumetric charge capacity 6-10 fold h
126        In particular, we weigh the graphitic anode during its initial lithiation process with an elec
127 s in the achievement of highly reversible Li anodes, e.g. as measured by the coulombic efficiency (CE
128 ar intercalation of Na into both cathode and anode electrodes during cycling, which is often problema
129 ts a promising strategy to revolutionize the anode-electrolyte interface chemistry for SSLBs and prov
130 s and recent progress regarding sodium-metal anodes employed in sodium-metal batteries (SMBs).
131 (TFSI)(2) -TFEP@MOF electrolyte protected Zn anode enables a Zn||Ti cell to achieve a high average Co
132                          As a result, the Sn anode enhanced by the Cu-Sn ICL shows a significant impr
133 nsequently, the as-developed potassium metal anodes exhibit a dendrite-free morphology with high Coul
134 on is lithium titanate (Li(4)Ti(5)O(12)), an anode exhibiting extraordinary rate capability apparentl
135 eposited Li, the obtained planar columnar Li anode exhibits excellent cycle stability at an ultra-hig
136 cell with rGO-guided planar Li layers as the anode exhibits stable cycling performance and high speci
137 robial activity continued to spread from the anode for at least 2 days, even after turning off the cu
138                    Lithium metal is an ideal anode for high-energy rechargeable batteries at low temp
139 m (Li) metal is a promising candidate as the anode for high-energy-density solid-state batteries.
140 t use of black phosphorus (BP) as the active anode for high-rate, high-capacity Li storage.
141 ew insights into realizing a stable Li metal anode for high-temperature Li metal batteries with a sim
142  considered the ultimate choice as a battery anode for mobile, as well as in some stationary applicat
143 cently been proposed to serve as the "inert" anode for molten oxide electrolysis (MOE).
144 ium in safer positions, enabling a promising anode for next-generation lithium batteries.
145 l building units as a significantly improved anode for potassium-ion batteries (PIBs).
146 acity and has been considered as a candidate anode for sodium-ion batteries.
147 entials, carbon materials can serve as ideal anodes for 'Rocking-Chair' alkali metal-ion batteries.
148 on can be used to identify other metal oxide anodes for fast-charging, long-life lithium-ion batterie
149  to the practical implementation of Li metal anodes for high-energy Li-ion batteries.
150 chieve good rate capability of lithium metal anodes for high-energy-density batteries, one fundamenta
151 gulation can be applicable to other alloying anodes for high-performance KIBs.
152                           Similar to silicon anodes for lithium-ion batteries, the electrochemical pe
153 ly pure silicon, the creation of carbon-free anodes for oxygen production, and silicon electrodeposit
154 owards high-performance red-phosphorus-based anodes for sodium-ion batteries.
155                    The interfaces a Li metal anode forms with any other material (liquid or solid) in
156 d self-healing capabilities, development of "anode-free" Li batteries to minimize the interaction bet
157 , we develop in situ NMR metrology to study "anode-free" lithium metal batteries where lithium is pla
158  is demonstrated in LMB with a zero-excess ("anode-free") configuration where a 100% improved perform
159                 We demonstrate that Li-metal anodes >20 mum can be electroplated onto a current colle
160  storage, the implementation of the Na metal anode has been primarily hindered by dendritic and "dead
161 lable dendrite growth on the potassium metal anode has restrained their practical applications.
162 ility and good adaptability to lithium metal anodes have attracted extensive attention in recent year
163                                Lithium metal anodes have attracted extensive attention owing to their
164 ighest projected energy density as a battery anode, however its extremely high reactivity induces den
165 by the lack of high-performance and low-cost anode hydrogen oxidation reaction catalysts.
166                       With a 245 um thick Li anode in a full Li||LFP (LiFePO(4) ) cell, introducing t
167 p reduction of TPPO to TPP using an aluminum anode in combination with a supporting electrolyte that
168 inum nanoparticles cathode and a polyaniline anode in Fe(2+)/Fe(3+) redox electrolyte via isothermal
169 this material can be applied as a recyclable anode in molten CaCl(2) .
170 en hinder the application of a lithium metal anode in solid-state batteries.
171 flector, magnet-based mass spectrometer, and anode in the laboratory to demonstrate the 3DI prototype
172  lithium dendrites impedes the service of Li anodes in high energy and safety batteries.
173  The practical applications of lithium metal anodes in high-energy-density lithium metal batteries ha
174 nd tolerating volume variations of the MS(x) anodes in Na-ion batteries are reviewed.
175 n physical and functional properties of CrFe anodes in the corrosive environment of MOE are studied v
176 he ZnCl(2)-H(2)O-DMSO electrolyte enables Zn anodes in Zn||Ti half-cell to achieve a high average Cou
177 hanism of cathodes, and the reactions at the anodes including intercalation and alloying to explore p
178 late all interfacial processes at a Li metal anode, including electrodeposition during battery rechar
179 lation below 1 V, enabling application as an anode (initial specific capacity >200 mAh g(-1) with rem
180 lating and stripping of calcium at the metal-anode interface was achieved only recently and for very
181                          The anion-insertion anode is a nanocomposite having ferrocene encapsulated i
182         Developing a viable metallic lithium anode is a prerequisite for next-generation batteries.
183                        The metallic tin (Sn) anode is a promising candidate for next-generation lithi
184                                          The anode is composed of an elastic outermost carbon coverin
185                                    When this anode is employed in lithium-oxygen full batteries, the
186             However, the application of a Zn anode is hindered by severe dendrite formation and side
187 drite-free and long-term reversible Li metal anode is reported.
188 , the Li dendrite growth of metallic lithium anode is suppressed by forming a lithium fluoride (LiF)-
189                                    The metal anode is the essential component of emerging energy stor
190 ver, as a proof of concept, the protected Li anode is used in a next-generation Li-O(2) battery syste
191           Plating of metallic Li on graphite anodes is a critical reason for Li-ion battery capacity
192 er, practical application of porous alloying anodes is challenging because of limitations such as cal
193 lkali metals, their practical application as anodes is still limited by the inherent dendrite-growth
194 s in structural heterogeneities of the metal anode, leading to battery failure by short-circuit and c
195   The development of a rechargeable Li metal anode (LMA) is an important milestone for improved batte
196 um (Li) metal batteries (LMBs) with Li metal anode (LMA) were first developed in the 1970s, but their
197 at, besides interfacial manganese species on anode, manganese(II) in bulk electrolyte also significan
198 rgy density of 210 Wh kg(-1) (of cathode and anode mass) and a low capacity decay rate of 0.0047 % pe
199 lly, we demonstrate that using a sacrificial anode material (magnesium or aluminum), combined with a
200     Lithium metal is considered the ultimate anode material for future rechargeable batteries(1,2), b
201               Lithium is the most attractive anode material for high-energy density rechargeable batt
202     Metallic lithium is the most competitive anode material for next-generation lithium (Li)-ion batt
203                     Lithium metal, the ideal anode material for rechargeable batteries, suffers from
204 al specific capacity, making it the ultimate anode material for rechargeable batteries.
205 or efficiency in lithium-ion batteries as an anode material in terms of rate capacity and cycle stabi
206 graphene systems might be a highly promising anode material in the lithium-ion battery owing to its r
207                   Li metal is the most ideal anode material to assemble rechargeable batteries with h
208 of the ideal alternatives for Li metal as an anode material while maintaining large capacity, low pot
209 state by global aromaticity, resulting in an anode material with extraordinarily stable cycling perfo
210 nts the ultimate high-energy-density battery anode material, its use is limited by dendrite formation
211 , a safe, low-cost, and energy-dense battery anode material.
212 ging challenges and some perspective on both anode materials and cathodic catalysts are also outlined
213                          High-capacity alloy anode materials for Li-ion batteries have long been held
214 s considered to be one of the most promising anode materials for next-generation batteries.
215  most aromatic organic compounds assessed as anode materials in SIBs to date exhibit significant degr
216 ly a zero-order kinetic rate law for both Mg anode materials, and the rate constants (k) depended upo
217 ates, originally developed as Li-ion battery anode materials, as promising candidates for memristive-
218 t allows for handling of the treated lithium anode membrane in a standard dry room during cell fabric
219 xperiments showed that O(2) evolution at the anode not only eliminates the need for an external reduc
220 ggish oxygen evolution reaction (OER) at the anode of water electrolyzer that limits the overall effi
221 trical current and transfer electrons to the anodes of different types of bioelectrochemical systems.
222                        High-capacity silicon anodes offer a viable alternative to carbonaceous materi
223                                Lithium metal anodes offer high theoretical capacities (3,860 milliamp
224 charge and discharge cycles of lithium-metal anodes often leads to short-circuiting by puncturing the
225 osed by partially dealloying the Li-Mg alloy anode on a garnet-type solid-state electrolyte.
226  a commercial fast-charging lithium titanate anode or other intercalation anode candidates (Li(3)VO(4
227 ve cells to migrate to the cathode or to the anode or to lose migration direction.
228 their lifespan is limited by irreversible Zn anodes owing to water decomposition and Zn dendrite grow
229 to Au(III) was successfully achieved through anode oxidation, which enabled facile access to either s
230                                           Li anodes paired with lithium cobalt oxide (LiCoO(2) ) and
231 lly adsorbed on the surface of lithium metal anodes, particularly on the tips of lithium buds, throug
232 ndamental mechanisms governing lithium metal anode performance in combination with inorganic solid el
233 Here, we stimulated 60 DoC patients with the anode placed over left-dorsolateral prefrontal cortex in
234 Among all the strategies, only with positive anode potential, AGS was successfully shifted from metha
235 nce and organic loading and manipulating the anode potential.
236  and hydrodynamic instabilities at the metal anode produce uneven metal electrodeposition and poor an
237                                  The pure Mg anode produced a porous 0.6-4.1 mum thick film, while th
238 ates the cathode display from the biosensing anode, protecting it from the sample.
239 bon anode with a safe, dendrite-free lithium anode provides a fast charge while reducing the cost of
240 cal alcohol oxidation is considered a viable anode reaction that can be paired with H(2) evolution or
241 ly grown biofilms (>20 um), and at different anode redox potentials.
242 ctrolytes and low Coulombic efficiency of Li anode require excess electrolytes and Li metal, which si
243 -optimal intercalation potentials of current anodes result in a trade-off between energy density, pow
244 e that achievement of the remaining ~0.5% in anode reversibility will require fresh approaches, perha
245 duce uneven metal electrodeposition and poor anode reversibility, which, are among the many known cha
246 ctrochemical requirements for achieving high anode reversibility.
247  deposit preferentially at the bottom of the anode, safely away from the separator.
248                                    The dense anode showed a better performance.
249                    This sulfur-doped silicon anode shows highly stable battery cycling at a fast-char
250            Particularly, the reaction at the anode side, namely the oxygen evolution reaction (OER),
251                        The resulting lithium anodes significantly reduce the probability of dendrite-
252                              The cathode and anode simultaneously generate the corresponding reactive
253   Lithium metal batteries featuring Li metal anodes, solid polymer electrolytes, and high-voltage cat
254 re we report a self-smoothing lithium-carbon anode structure based on mesoporous carbon nanofibres, w
255                          Potassium (K) metal anodes suffer from a challenging problem of dendrite gro
256 , but rechargeable batteries built with such anodes suffer from dendrite growth and low Coulombic eff
257 ect comparisons of the SEI grown on graphite anodes suggest that LEMC, instead of LEDC, is likely to
258 lyte interphase (SEI) formed on the Li-metal anode surface is strongly bonded to Li and experiences t
259 eposition of the transition-metal cations on anode surface, in elemental form or as chelated-complexe
260 ported mechanisms of PFAS degradation at the anode surface.
261     We have developed a micro-pixel read-out anode technique that significantly saves power in the pa
262 electrolyte interphase on a metallic-lithium anode that allows for handling of the treated lithium an
263 (3+x)V(2)O(5) can be used as a fast-charging anode that can reversibly cycle two lithium ions at an a
264 , low-cost fabrication of a metallic-lithium anode that is stable in air and plated dendrite-free fro
265 ctrolyte interphase passivation layer on the anode that is unstable during cycling.
266  With in situ formed NaK liquid alloys as an anode, the dendritic growth of alkali metals can be elim
267 ources and the role of materials used at the anode, the fundamentals of ECR systems, including photo-
268  system that can stabilize the lithium-metal anode, the solvation behavior of the solvent molecules m
269 ated to the design of highly reversible zinc anodes, the exploration of electrolytes satisfying both
270 ionally high energy density of lithium metal anodes, the practical application of lithium-metal batte
271 presses the anion-insertion potential in the anode, thus widening the full cell's voltage by 0.35 V c
272  designed carbonate electrolyte enables a Li anode to achieve a high Li plating/stripping Coulombic e
273 ver stable high capacity using a Na-K liquid anode to avoid dendrites.
274              Metallic lithium is a promising anode to increase the energy density of rechargeable lit
275 ogether with Mg (x)Mo(6)S(8) ( x ~ 2) as the anode to investigate the structural evolution and oxidat
276 e macroporous architecture for a Si-graphite anode to maximize the volumetric energy density.
277 in dual-ion batteries (DIBs) by allowing the anode to take in anions and a cation-deficient cathode t
278       Consequently, very high areal capacity anodes (up to 23.3 mAh cm(-2)) have been demonstrated.
279 rase to transfer the electrons to conducting anode via the redox active pheromone lipoproteins locali
280 lectro-flow cell with a porous graphite felt anode was designed to ensure efficient turnover.
281 f graphite felt for both the cathode and the anode was key to ensuring chemoselectivity and high deut
282                               This molecular anode was subsequently combined with a cathode consistin
283                              The cathode and anode were separated by a porous solid electrolyte (PSE)
284                     Protons generated at the anode were transported through the cation exchange membr
285 vidence for liquid water accumulation at the anode, which causes severe ionomer swelling and performa
286 ng a thin layer of tungsten oxide within the anode, which serves as a rapid-response hydrogen reservo
287 oupling the pre-lithiated MCMB-F (Li@MCMB-F) anode with a commercial LiFePO(4) cathode at the positiv
288 ochemical oxidation at a boron-doped diamond anode with a low potential for the generation of stable
289            Replacing the low-capacity carbon anode with a safe, dendrite-free lithium anode provides
290 ectrolyte interphase by treating the lithium anode with a tin-containing electrolyte.
291 mbled by combining the modified alpha-MoO(3) anode with an anion-intercalation graphite cathode, oper
292  also promote reversible cycling of Li metal anodes with high Coulombic efficiency (CE) on both conve
293          Developing reversible lithium metal anodes with high rate capability is one of the central a
294 hanically robust graphene tubes, we show tin anodes with high volumetric and gravimetric capacities,
295 roperties of the interlayer lead to Li metal anodes with longer cycle life, higher efficiency, and be
296 ion batteries, however, adopt graphite-based anodes with low tap density and gravimetric capacity, re
297 ent and new strategies for achieving such Li anodes with the specific aim of engaging established con
298 y to fabricate this interfacial layer for Li anodes without any inert atmosphere protection and limit
299             There are numerous studies on Li anodes, yet little attention has been paid to the intrin
300 ry with a disordered rock salt Li(3)V(2)O(5) anode yields a cell voltage much higher than does a batt

 
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