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Electrochemical cell configuration

Electrochemical Cell Configuration Corresponding Energy-Band Diagrams... [Pg.101]

Figure 3.7 Schematics of two electrochemical cell configurations used in NR experiments ... Figure 3.7 Schematics of two electrochemical cell configurations used in NR experiments ...
Figure4.5 The most common flow-through electrochemical cell configurations are as follows (A) thin-layer, (B) wall-jet, (C) tubular, (D) porous. The direction of fluid flow is... Figure4.5 The most common flow-through electrochemical cell configurations are as follows (A) thin-layer, (B) wall-jet, (C) tubular, (D) porous. The direction of fluid flow is...
All of the catalysts synthesized are listed in Table 2, and the performance in rotating disk electrode (RDE) in acid conditions are depicted in Fig. 6 [65, 67, 70-72]. In RDE tests (RRDE-3A ALS coupled with a Bio-Logic SP-150 multi-potentiostat), a conventional three-electrode electrochemical cell configuration, equipped with a glassy carbon disk working electrode (0.1256 cm geometric area), a Pt helical wire counter electrode, and a saturated calomel (SCE) reference electrode, was used. The activity of a commercial 40 % Pt/C (Hyspec 6000 from Johnson Matthey) catalyst was assessed as well, as reference catalyst toward ORR. [Pg.76]

In order to study Y2C coating on anodized aluminum, the following electrochemical cell configuration is used to study the overall impedance and interface model of the coated samples or parts as shown in Fig. 27 [28, 78]. [Pg.25]

Fig. 27. Electrochemical cell configuration during EIS study of Y2Q3 coated anodized aluminum in 3.5wt% NaCl solution [78]. Fig. 27. Electrochemical cell configuration during EIS study of Y2Q3 coated anodized aluminum in 3.5wt% NaCl solution [78].
The diffusion layer thickness depends on the flow rate and the cell geometry, which leads to a characteristic dependence of limiting current on the flow rate. Table 4.1 summarizes the limiting current equations calculated for popular electrochemical cell configurations in terms of their hydrodynamics where it can be seen that the response (current) at an amperometric electrode is proportional to the molar concentration of analyte in the eluate. [Pg.80]

In the two first cases the membrane is usually considered as catalytically inert and is coupled with a conventional fixed bed of catalyst placed on one of the membrane sides. In the case of reactor design based on an electrochemical cell configuration, the catalyst is coated on one of the electrodes or can serve as an electrode itself. [Pg.1351]

Figure 8. Schematic illustrations of (a) two-electrode and (b) three-electrode electrochemical cell configurations. Figure 8. Schematic illustrations of (a) two-electrode and (b) three-electrode electrochemical cell configurations.
Figure 14. Nyquist plots of (a) cathode, (b) anode, and (c) full cell, obtained from the fresh and aged cells at the cell potential of 4.1 V (vs. LifLi). The lines in (a) and (b) were determined from the CNLS fittings of the impedance spectra to the equivalent circuits. In (c), the summation of the impedance spectra of cathode and anode obtained under three-electrode electrochemical cell configuration (lines) were compared with the spectra measured tmder two-electrode electrochemical cell configuration (symbols). (a)-2, (b)-2, and (c)-2 represent the corresponding Bode plots. Figure 14. Nyquist plots of (a) cathode, (b) anode, and (c) full cell, obtained from the fresh and aged cells at the cell potential of 4.1 V (vs. LifLi). The lines in (a) and (b) were determined from the CNLS fittings of the impedance spectra to the equivalent circuits. In (c), the summation of the impedance spectra of cathode and anode obtained under three-electrode electrochemical cell configuration (lines) were compared with the spectra measured tmder two-electrode electrochemical cell configuration (symbols). (a)-2, (b)-2, and (c)-2 represent the corresponding Bode plots.
Much caution should be taken regarding the effect of the lithium anode on impedance spectra and polarization transients when they are obtained under a two-electrode electrochemical cell configuration. The impedance and polarization caused by a lithium anode significantly changes the overall spectra and transients, respectively, in value and shape. [Pg.115]

Although higher conductivities are preferable, 100-fold or 1000-fold increases are not essential, as a thin-film electrochemical cell configuration can largely compensate for these lower values. Less favorable is the tendency for ion association and low cationic relative mobility (a property shared with aprotic liquids, as opposed to ceramic or glassy electrolytes) in polyether-based materials. These fundamental properties can affect cell performance and must influence the design of new polymeric electrolytes to make them competitive as battery materials. [Pg.629]

We first consider the localized photoelectrodeposition of metals onto semiconductor surfaces (3i )(32). In almost every case the precursor to a metal In a plating bath is a positive ion, so that the deposit is formed by reduction. Thus, a p-type semiconductor is required for positive photoelectrochemical imaging. If the deposition is done in an electrochemical cell configuration, the semiconductor electrode should... [Pg.203]

Figure 1. Sketch of an electrochemical cell whose equilibrium (open circuit) potential difference is AE. (a) Conventional configuration and (b) short-circuited configuration with an air gap. M and R are the electrodes, S is the solvent (electrolyte solution). Cu indicates the cables connecting the two electrodes to a measuring instrument (or to each other).

Figure 1. Sketch of an electrochemical cell whose equilibrium (open circuit) potential difference is AE. (a) Conventional configuration and (b) short-circuited configuration with an air gap. M and R are the electrodes, S is the solvent (electrolyte solution). Cu indicates the cables connecting the two electrodes to a measuring instrument (or to each other). <P is the work to transfer an electron from M (or R) to the exterior of the phase through S.
The electrochemical cell consists of high surface area Pd/C or unsupported Pd-Ru cathodes interfaced to Nafion with a Pt-black/H2 counter electrode. The cell configuration, as well as the reactions taking place on the anode and the cathode are the following ... [Pg.466]

Figure 12.10. Multiple-channel electrochemical cell termed bipolar configuration of second generation. 1 Reprinted with permission from Elsevier Science. Figure 12.10. Multiple-channel electrochemical cell termed bipolar configuration of second generation. 1 Reprinted with permission from Elsevier Science.
SXS measurements. (A) Single-crystal disk electrode, (B) Pt counter electrode, (C) Ag/AgCl reference electrode, (D) Mylar window, (E) electrolyte solution, (F) inlet for electrolyte solution, (G) outlet for electrolyte solution, (H) cell body, (1) micrometer, (J) electrode holder, (K) outer chamber, (b) Cell configuration for electrochemical measurement, (c) Cell configuration for SXRD measurement. (From Kondo et al., 2002, with permission from Elsevier.)... [Pg.475]

Chen Y-X, Heinen M, Jusys Z, Behm RJ. 2006h. Kinetics and mechanism of formic acid electrooxidation—Spectro-electrochemical studies in a novel flow cell configuration. Angew ChemIntEd 45 981-985. [Pg.455]

The electrochemical cell for the polarographic measurements had a four-electrode configuration equipped with a microsyringe, and was connected to a computer-assisted data-acquisition system [7]. On the other hand, the cyclic voltammetric measurements that are also assisted by a computer data-acquisition system were carried out using a gel electrode that contains the aqueous phase [8]. The cell structure was as follows ... [Pg.630]

Figure 2.67 Typical cell configurations employed in obtaining in situ electrochemical X-ray diffraction measurements (a) transmission (Laue configuration), (b) reflection (Bragg configuration). Figure 2.67 Typical cell configurations employed in obtaining in situ electrochemical X-ray diffraction measurements (a) transmission (Laue configuration), (b) reflection (Bragg configuration).
The electrochemical cell used by Flcischmann and co-workers (1986) employing the Bragg configuration is shown in Figure 2.67(b). The source is a copper anode X-ray tube employing a Ni filter to select out the Cu Ka line the detector is a PS PD. [Pg.143]

Figure 2.3 Electrochemical cell with a three-electrode configuration. Figure 2.3 Electrochemical cell with a three-electrode configuration.
G. Yu, Polymer Light-Emitting Electrochemical Cells in Surface Cell Configuration, U.S. Patent... [Pg.42]

Fig. 18b.1. Electrochemical cells and representative cell configurations, (a) Schematic diagram of a cell-potentiostat system, (b) Typical laboratory cell with Hg-drop electrode and drop knocker, (c) Voltammetric cell as detector at the end of a high-performance liquid chromatographic column, (d) A two-electrode (graphite) chip cell for biosensor development, (e) Three-electrode chip cells on a ceramic substrate for bioanalytical work. Fig. 18b.1. Electrochemical cells and representative cell configurations, (a) Schematic diagram of a cell-potentiostat system, (b) Typical laboratory cell with Hg-drop electrode and drop knocker, (c) Voltammetric cell as detector at the end of a high-performance liquid chromatographic column, (d) A two-electrode (graphite) chip cell for biosensor development, (e) Three-electrode chip cells on a ceramic substrate for bioanalytical work.

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