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1  the algal growth medium (which was also the catholyte).
2 lyte with a more concentrated anolyte than a catholyte.
3 een achieved when coupled with a I3(-) /I(-) catholyte.
4 atively stable pH values in both anolyte and catholyte.
5 notube cathode and a liquid-type polysulfide catholyte.
6 lectrolyte as anolyte and organic solvent as catholyte.
7 -propyl phenothiazine (C3-PTZ), were used as catholytes.
8                         Even concentrated MB catholyte (1.5 m) is still able to deliver stable capaci
9 ired with a high redox potential Fe-Dcbpy/CN catholyte, 2,2'-bipyridine-4,4'-dicarboxylic (Dcbpy) aci
10                    Batteries with an aqueous catholyte and a Li metal anode have attracted interest o
11            With 12.5 mul of 5 M Li2S8 as the catholyte and a rate of C/5, we can reach the theoretica
12 oped a dual-redox EC consisting of a bromide catholyte and an ethyl viologen anolyte with the additio
13 of bipolar electrolytes that act as both the catholyte and anolyte.
14 sing hydroquinone (H2BQ) aqueous solution as catholyte and graphite in aprotic electrolyte as anode.
15 ion of this approach with the use of bromide catholyte and tetrabutylammonium cation that induces rev
16 ium sulfide cathodes and lithium polysulfide catholytes, as well as recent burgeoning efforts in the
17                            Here we develop a catholyte based on an emerging class of porous materials
18                        The most stable 2e(-) catholyte candidate was paired with a viologen derivativ
19         Ultimately, SH-ZIT enables ultrahigh catholyte capacity utilization up to over 120 ampere-hou
20     Therefore, we engineer a gradient in the catholyte concentration to match the Li(+) flux distribu
21  MBSBs were initially evaluated at different catholyte concentrations (0.1, 0.3, and 0.5 M) under sta
22  but not the salinity ratio, indicating high catholyte conductivity was essential for maximizing hydr
23                  MECs typically use a liquid catholyte containing a buffer or salts.
24 (2)V, in excess with the [Fe(bpy)(3)](2+/3+) catholyte containing ACC exhibited high-voltage discharg
25                   The lithium cell with DMTS catholyte delivers an initial specific capacity of 720 m
26                                          The catholyte demonstrated bactericidal properties, compared
27 A(2) anolyte (0.67 M) is paired with a Fe-CN catholyte, demonstrates exceptional cycling stability ov
28 nt of anolytes has lagged far behind that of catholytes due to the major limitations of the redox spe
29 bility in the above two new classes of 2e(-) catholytes, even when current strategies failed to stabi
30 lso been extended to the use of a Br2 -based catholyte, exhibiting a higher cell voltage with a theor
31 e water profile direction and the anolyte to catholyte filtrate ratio.
32 0 m is demonstrated as a high-energy-density catholyte for redox flow battery applications.
33 igned a high-potential (0.5 V vs. Ag/Ag(+) ) catholyte for RFBs, where the charged and discharged spe
34 lized) benzene derivatives as high-potential catholytes for non-aqueous redox flow batteries.
35 f diaminocyclopropenium-phenothiazine hybrid catholytes for non-aqueous redox flow batteries.
36   High redox potential, two-electron organic catholytes for nonaqueous redox flow batteries were deve
37 w battery via linkage of an I3(-)/I(-) based catholyte, for the simultaneous conversion and storage o
38 d tetra (ethylene glycol) dimethyl ether) as catholytes, forming membrane-free batteries with solid p
39  alters hydrolytic speciation of the charged catholyte from the typical dimeric species mu-O-[Fe(III)
40 divalent cations from the feedwater into the catholyte, further extends from the cathode chamber to t
41            A lack of suitable high-potential catholytes hinders the development of aqueous redox flow
42 al derivative was successfully deployed as a catholyte in a non-aqueous redox flow cell with butyl vi
43  MFCs were designed to harvest the generated catholyte in the internal chamber, which showed that liq
44       We report herein a new class of N-ORFB catholytes in the form of squaric acid quinoxaline (SQX)
45 iform distribution of the solid electrolyte (catholyte) in the conventional composite cathode and the
46  integrated methodology relies on exchanging catholyte, initially introduced in the nanoCEasy interfa
47 ilibrium at cation exchange membrane-anolyte/catholyte interfaces, the Na(+) ion in the anolyte actua
48 rine into electricity, while producing clean catholyte into an initially empty cathode chamber throug
49  ZPEs are seamlessly incorporated as a solid catholyte into pre-fabricated high-areal-capacity (10.0
50                                         This catholyte is shown to be compatible with cathode active
51            We employ a stationary unbuffered catholyte layer between BPM and cathode to promote C(2+)
52 velop a model that enables the design of the catholyte layer, finding that limiting the diffusion pat
53 low-cost, high-potential [Fe(bpy)(3)](2+/3+) catholyte-limited aqueous redox flow batteries extends t
54  developed in the 1970s using SOCl(2) as the catholyte, lithium metal as the anode and amorphous carb
55 en demonstrated that uses this molecule as a catholyte material and operated stably for 100 charge/di
56 9 h; and a proof-of-concept two-electron SQA catholyte material with oxidation potentials of 0.48 and
57 ocene/ferrocenium redox couple as the active catholyte material.
58  previously reported space of high-potential catholyte materials and showcase the power of mechanisti
59 indow of organic solvents, but the design of catholyte materials, which can exploit the upper range o
60 of the pure alcohol anolyte from the aqueous catholyte minimizes competing oxygen evolution and mitig
61  4-trimethylammonium-TEMPO (N(Me) -TEMPO) as catholyte, [(NPr)2 TTz]Cl4 enables a 1.44 V AORFB with a
62                It is the first time that the catholyte obtained as a by-product of electricity genera
63       Neodymium was further extracted in the catholyte of a three-compartment electrochemical system,
64                      Long-term impact of the catholyte on the pathogen killing was evaluated by plati
65 liquid-to-solid phase transition of oxidized catholyte (or reduced anolyte) with confinement in the p
66 phimurium on agar plates and showed that the catholyte possesses a long-term killing efficacy and con
67 go redox events at as low (anolyte) or high (catholyte) potentials as possible while exhibiting the s
68 ode, the two-electron-active (PEG3/PerF)-TTF catholyte produced a cell voltage of 3.56 V for the firs
69  ion transport (52%) from the anolyte to the catholyte rather than through a change in the transport
70  battery discharges by lithium oxidation and catholyte reduction to sulfur, sulfur dioxide and lithiu
71 om the pH difference between the anolyte and catholyte remained relatively constant during electrolys
72 out three subsequent feeding cycles, despite catholyte replacement and no new ZVI addition.
73 m(-2) coupled with Br(2)/Br(-) and I(2)/I(-) catholyte respectively.
74                     However, anions in these catholytes result in charge being balanced predominantly
75        Similar effects are observed when the catholyte's graphite felt electrode is electrochemically
76  performance of all solid-state batteries, a catholyte should demonstrate high ionic conductivity, go
77 l-solid-state Li/LiFePO4 cell with a polymer catholyte shows good cyclability and a long cycle life.
78  master mixture composition, field strength, catholyte, SL composition, focusing time, and capillary
79        In flow battery cycling at a standard catholyte SoC of 66.6 per cent (stoichiometrically X(3)(
80 e cathode overpotential was dependent on the catholyte (sodium bicarbonate) concentration, but not th
81               However, the effect of a mixed catholyte solution of alkali cations in the presence of
82  oxidized (overcharged) and by modifying the catholyte solution's pH, which was monitored in situ for
83                      Results showed that the catholyte solutions were efficacious in the inactivation
84 g derivatized fullerenes as both anolyte and catholyte species in a series of battery cells, includin
85 hing the accumulated salt and decreasing the catholyte temperature prolong together the catalyst's op
86 rty analysis enabled the identification of a catholyte that displays stable two-electron cycling at p
87                                         As a catholyte, the addition of an appropriate amount of wate
88                            When applied as a catholyte, the NaCrO(2)||Na(0.7)Zr(0.3)La(0.7)Cl(4)||Na(
89                       Paired with an NH(4) I catholyte, the resulting pH-neutral AORFB with an energy
90 tends to acidify (or basify) the anolyte (or catholyte), their effects are buffered by a cascade of c
91 e, a basic electrolyte bridge, and an acidic catholyte to achieve low-overpotential lactate oxidation
92 yed to prevent Cu(2+) from crossing from the catholyte to the anode side.
93 (2.2-2.8 V vs Na(9)Sn(4)), making them ideal catholytes to pair with commonly used oxide cathode mate
94 g the strength of ammonia diffusion from the catholyte toward the anolyte, will help effective design
95         Hydrolysis of the charged (oxidized) catholyte typically occurs when its redox potential appr
96 ITs enable homogeneous cycling of the halide catholyte up to 90 per cent SoC at 2 moles per litre (47
97                                          The catholyte was collected and used ex situ as a killing ag
98                                         This catholyte was deployed in a high energy density two-elec
99 e ((PEG3/PerF)-TTF) as a high energy density catholyte was developed.
100                            Once inoculum and catholyte were added to the MFC, a current of 74 muA was
101                                    These new catholytes were deployed in two-electron redox flow batt
102 hia coli target, as a surrogate coliform, to catholyte where a rapid kill rate was observed.
103 ueous redox flow batteries with halide-based catholytes (where the halogen atom (X) is Br or I) are p
104        Debromination released bromide to the catholyte, while lower-order brominated aromatic interme
105 M KOH for the anolyte and 0.5 M NaCl for the catholyte with a constant current (100 mA/cm(2) for 20 h
106  addressed by separating the anolyte and the catholyte with a membrane that only allows for Mg(2+) tr
107 solve this conundrum by replacing the liquid catholyte with a solid-state proton conductor to regulat
108  novel vapor-fed MEC configuration lacking a catholyte with closely spaced electrodes and an anion ex
109 ack of electroactive compounds (anolytes and catholytes) with the necessary combination of (1) redox
110 of wastewater towards the self-generation of catholyte within the same reactor.

 
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