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Electrochemical channel flow

Fig. 4.13 RF-heated electrochemical channel flow system. From [126], with permission... Fig. 4.13 RF-heated electrochemical channel flow system. From [126], with permission...
Miniaturisation of various devices and systems has become a popular trend in many areas of modern nanotechnology such as microelectronics, optics, etc. In particular, this is very important in creating chemical or electrochemical sensors where the amount of sample required for the analysis is a critical parameter and must be minimized. In this work we will focus on a micrometric channel flow system. We will call such miniaturised flow cells microfluidic systems , i.e. cells with one or more dimensions being of the order of a few microns. Such microfluidic channels have kinetic and analytical properties which can be finely tuned as a function of the hydrodynamic flow. However, presently, there is no simple and direct method to monitor the corresponding flows in. situ. [Pg.85]

Peter EM, Wang RL (1999) Channel flow ceU electrodeposition of CdTe for solar cells. Electrochem Commun 1 554-558... [Pg.152]

Channel electrode -> electrochemical cell (practical aspects) (subentry channel flow electrochemical cell), and... [Pg.82]

Channel flow electrochemical cell — A cell that is used in a flow system, where an examined liquid or... [Pg.186]

Ahmed S, Kemp TJ, Unwin PR (2001) Photomineralisation Kinetics of Aqueous Chlorophenols at a Supported Ti02 Surface Studied by the Channel-flow Method with Electrochemical Detection, J. Photo-chem. Photobiol. A Chem. 141 69-78. [Pg.136]

Finally, mention should be made of a new generation of channel flow cells, in which the electrochemically generated species are transported by a laminar flow from the working electrode to an optically transparent part of the cell [316-318]. [Pg.159]

Fig. 31. Typical channel flow electrochemical reactors (CER) with flow-by (a, b) and packed-bed (c) working electrodes. The control volume (d) includes the active electrocatalyst area (67). A, reactant B, C, products E, electrolyte ce, counter electrode we, working electrode. (Reprinted by permission of the publisher. The Electrochemical Society, Inc.)... Fig. 31. Typical channel flow electrochemical reactors (CER) with flow-by (a, b) and packed-bed (c) working electrodes. The control volume (d) includes the active electrocatalyst area (67). A, reactant B, C, products E, electrolyte ce, counter electrode we, working electrode. (Reprinted by permission of the publisher. The Electrochemical Society, Inc.)...
The combination of electrochemistry and photochemistry is a form of dual-activation process. Evidence for a photochemical effect in addition to an electrochemical one is normally seen in the form of photocurrent, which is extra current that flows in the presence of light [88, M and M] In photoelectrochemistry, light is absorbed into the electrode (typically a semiconductor) and this can induce changes in the electrode s conduction properties, thus altering its electrochemical activity. Alternatively, the light is absorbed in solution by electroactive molecules or their reduced/oxidized products inducing photochemical reactions or modifications of the electrode reaction. In the latter case electrochemical cells (RDE or channel-flow cells) are constructed to allow irradiation of the electrode area with UVWIS light to excite species involved in electrochemical processes and thus promote further reactions. [Pg.1945]

Cell Design Albery and coworkers [9-14] used tubular electrodes for ex situ electrochemical EPR experiments. The tubular electrode is equivalent to the channel electrode in all respects, except that the cross section is circular rather than rectangular [82, 137]. Like the later-developed channel flow cell, this setup (shown in Fig. 23) permits the interrogation of electrode reaction mechanisms of relatively long-lived radical species, [9-14] since the convective-diffusion equations are mathematically well defined, which at steady state are given by Eq. (37)... [Pg.732]

Cell Design Waller and Compton [85] effectively mimicked the Allendo-erfer coaxial design vide supra), whilst simultaneously maintaining the mathematically well-defined laminar flow of the channel flow cell. This improved cell for electrochemical EPR [85] allowed an improvement in the channel cell regarding lifetimes of radicals amenable to study, whilst retaining the hydrodynamic flow that is essential for the investigation of electrode reaction mechanisms. [Pg.734]

Wang H, Rus E, Abruna HD (2010) New double-band-electrode channel flow differential electrochemical mass spectrometry cell application for detecting product formation during methanol electrooxidation. Anal Chem 82(11) 4319 324... [Pg.515]

A typical membrane-electrode assembly is a two-scale structure its inplane size ( 10 cm) exceeds its thickness ( 0.1 cm) by three orders of magnitude. The reactants are usually distributed over the cell surface through a system of feed channels (flow field). Reactants are consumed in electrochemical reactions and hence part of the cell located close to the channel inlet receives more feed than the remote part at the outlet. Nonuniformity of the feed concentration along the channel leads to a specific voltage loss, which is not captured by ID models. [Pg.117]

Mathematical solution depends on the boundary conditions governed by the geometry of the reactor system. We will confine our attention to plate electrodes. Electrochemical reactors can be divided into two categories tank electrolyzers and channel flow electrolyzers. [Pg.206]

The rotating disc electrode (RDE) is the classical hydrodynamic electroanalytical technique used to limit the diffusion layer thickness. However, readers should also consider alternative controlled flow methods including the channel flow cell (38), the wall pipe and wall jet configurations (39). Forced convection has several advantages which include (1) the rapid establishment of a high rate of steady-state mass transport and (2) easily and reproducibly controlled convection over a wide range of mass transfer coefficients. There are also drawbacks (1) in many instances, the construction of electrodes and cells is not easy and (2) the theoretical treatment requires the determination of the solution flow velocity profiles (as functions of rotation rate, viscosities and densities) and of the electrochemical problem very few cases yield exact solutions. [Pg.451]

Qiu F, Compton RG, Coles BA, Marken F (2000) Thermal activation of electrochemical processes in a Rf-heated channel flow cell experiment and finite element simulation. J Electroanal Chem 492 150-155... [Pg.387]

Cardwell, T. J. and M. J. Christophersen, 2000. Determination of sulfur dioxide and ascorbic acid in beverages using a dual channel flow injection electrochemical detection system. Anal. Chim. Acta 416 105-110. [Pg.117]

Ahmed, S., Kemp, T.J., and Unwin, P.R. (2001) Photomineralisation kinetics of aqueous chlorophenols at a supported Ti02 surface studied by the channel-flow method with electrochemical detection. /. Photochem. Photobiol A, 141 (1),... [Pg.565]

Although ceramic electrodes have received much attention (101), they have not been successful in channels operating with slag-laden flows, because of excessive electrochemical corrosion caused by the slag. Only weU-cooled metallic elements have been used successfully in slagging environments. [Pg.429]

OPTIMISATION OF MICROBAND ELECTRODE SIZES AND LOCATIONS WITHIN A RECTANGULAR MICROFLUIDIC CHANNEL FOR ELECTROCHEMICAL MONITORING OF HYDRODYNAMIC FLOW PROFILES... [Pg.127]


See other pages where Electrochemical channel flow is mentioned: [Pg.70]    [Pg.187]    [Pg.553]    [Pg.309]    [Pg.184]    [Pg.672]    [Pg.726]    [Pg.727]    [Pg.3025]    [Pg.243]    [Pg.47]    [Pg.519]    [Pg.187]    [Pg.135]    [Pg.173]    [Pg.131]    [Pg.189]    [Pg.190]    [Pg.428]    [Pg.80]   
See also in sourсe #XX -- [ Pg.169 , Pg.170 , Pg.175 ]




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