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A Electrochemical Cells

Electroanalytical chemistry encompasses a group of qualitative and quantitative analytical methods based on the electrical properties of a solution of the anahie when it is made part of an electrochemical cell. Electroan-alytical techniques are capable of producing loir detection limits and a wealth of characterization information describing electrochcmically accessible systems. Such information includes the stoichiometry and rate of interfacial charge transfer the rate of mass transfer, the e.ite.nt of adsorption or chemisorption, and the rates and equilibrium constants for chemical reactions. [Pg.628]

Throughout this chapter, this logo indicates an opportunity for online self-study at whw. 1homsonedn.com/dieniistr)/skoog. linking you to interactive tutorials, simulations, and exercises. [Pg.628]

Thoughtful application of the various electroana-lyiical methods described in Chapters 23-25 requires an understanding of the basic theory and the practical aspects of the operation of electrochemical cells. This chapter is devoted largely to these topics. [Pg.628]

A dc electrochemical cell consists of two electrical conductors called electrodes, each immersed in a suitable electrolyte solution. 1 or a current to develop in a cell, it Is necessary (1) that the electrodes be connected externally with a metal conductor. (2) that the two electrolyte. solutions be in contact to permit niovemenl of ions from one to the other, and (.3) that an eleciron-tratisfer reaction can occur at each of the two electrodes. I igure 22-la shows an example of a simple electrochemical cell, ll consists of a silver eleclrode [Pg.628]

FIGURE 22-1 (a) A galvanic electrochen ical cell al open circuil (bi a galvanic cell doing work (c) an electrolytic cell. [Pg.629]


Fig. 4.1 (a) Electrochemical cell dipped in ultrasonic bath, (b) Klima sonoelectrochemical cell (Reprinted from [35]. Copyright (1999) with the permission from Elsevier)... [Pg.111]

Figure 14.5 shows the basic arrangement of a electrochemical cell called the Daniell cell. This cell is named for John Frederick Daniell (1790-1845) who constructed this type of cell in 1836. The Daniell cell components include zinc and copper solutions in separate containers. Between the solutions is a salt bridge... [Pg.180]

Define the following terms used in Section 6.3 (a) electrochemical cell, (b) ideally nonpolarizable and polarizable interfaces, (c) relative electrode potential, (d) outer potential, (e) inner potential, (1) surface potential, (g) image forces, (h) Coulombic forces, (i) electrochemical potential, (j) chemical potential, (k) electron work function, (1) just outside the metal, and (m) absolute potential. (Gamboa-Aldeco)... [Pg.299]

A preferred method for producing a composition comprising silver according to this invention utilizes a electrochemical cell comprising electrodes and comprises the steps... [Pg.3]

ESI nebulization involves a variety of electrochemical processes at the needle and at the counter electrode [27, 30]. The ESI interface can be considered as a electrochemical cell, in which part of the ion transport takes place through the gas phase (Figure 6.1). In positive-ion mode, an emichment of positive electrolyte ions occurs at the solution meniscus as the result of an electrophoretic charge separation. The liquid meniscus is pulled into a cone which emits a fine mist of droplets with an excess positive charge. Charge balance is attained by electrochemical oxidation at the capillary tip and reduction at the counter electrode. The topic arose significant discussion in 2000 and the discussion partners continued to disagree on the role of electrochemistry inESI-MS [39]. [Pg.148]

I See the Saunders Interactive General Chemistry CD-ROM, Screen 21 A, Electrochemical Cells. [Pg.849]

Fig. 2 (A) Electrochemical cell with three electrodes connected to a potentiostat. (B) Electronic sketch illustrating the mode of operation of a typical potentiostat. Fig. 2 (A) Electrochemical cell with three electrodes connected to a potentiostat. (B) Electronic sketch illustrating the mode of operation of a typical potentiostat.
Figure 7.11. Schematic picture of electron transfer in a electrochemical cell. Figure 7.11. Schematic picture of electron transfer in a electrochemical cell.
Fig. 7.10 (a) Electrochemical cell for operando XRR measurements (b) XRR results collected during emodic polarization of a LiMn204 thin film in cell (a) (1) patterns, (2) potential dependence of surface roughness, and (3) potential dependence of film thickness. Reproduced with permission from [201] copyright 2007, The Electrochemical Society... [Pg.344]

The primary procedure for pH is based on the measurement of the potential difference of a electrochemical cell without liquid junction, involving a selected buffer solution, a platinum hydrogen electrode, and a silver/silver chloride reference electrode, in cell I [15] ... [Pg.80]

Fig. 16. (a) Electrochemical cells used for EMF and Faradic Efficiency measurements (b) variation of the average electronic transport numbre of Lao.9Sro.iGao.8Mgo.203-5 determined by different techniques, from [Kharton et al., 2007]. [Pg.191]

A wide variety of molecules and ions have shown SERS (more than 80 different species have been observed to give SERS in a electrochemical cell ), and nearly all of these species can enter into a bonding relationship with the metal surface. It would appear, then, that for the 10 to 10 enhancements in the electrochemical environment, the formation of a weak chemical bond with the active site is a necessity. The total enhancement can be attributed to both a classical electromagnetic enhancement, which does not require a surface bond, and a chemical enhancement, most likely a charge transfer resonance Raman enhancement, which would require the surface-molecule interaction. [Pg.270]

FIGURE 8. (a) Electrochemical cell and ancillary components for quasi in situ conversion electron Mossbauer measurements/The counter and reference electrodes are not shown in this figure, (b) Schematic diagram of rotating system. A. Motor, B. aluminum support, C. reduction gear, D. phenolic shaft, E. brass contact, F. Teflon bushing, G. aluminum support, H. electrochemical cell, I. working electrode (disk), J. conversion electron counter, K. Mossbauer source, L. Mossbauer Doppler velocity transducer, M. carbon brush assembly. [Pg.415]

One of the main uses of these wet cells is to investigate surface electrochemistry [94, 95]. In these experiments, a single-crystal surface is prepared by UFIV teclmiqiies and then transferred into an electrochemical cell. An electrochemical reaction is then run and characterized using cyclic voltaimnetry, with the sample itself being one of the electrodes. In order to be sure that the electrochemical measurements all involved the same crystal face, for some experiments a single-crystal cube was actually oriented and polished on all six sides Following surface modification by electrochemistry, the sample is returned to UFIV for... [Pg.314]

Koop T, Schindler W, Kazimirov A, Scherb G, Zegenhagen J, Schulz T, Feidenhans l R and Kirschner J 1998 Electrochemical cell tor in situ x-ray diffraction under ultrapure conditions Rev. Sc/, instrum. 69 1840... [Pg.321]

A special example of electrical work occurs when work is done on an electrochemical cell or by such a cell on the surroundings -w in the convention of this article). Themiodynamics applies to such a cell when it is at equilibrium with its surroundings, i.e. when the electrical potential (electromotive force emi) of the cell is... [Pg.327]

In electrochemical cells (to be discussed later), if a particular gas participates in a chemical reaction at an electrode, the observed electromotive force is a fiinction of the partial pressure of the reactive gas and not of the partial pressures of any other gases present. [Pg.359]

As seen in previous sections, the standard entropy AS of a chemical reaction can be detemiined from the equilibrium constant K and its temperature derivative, or equivalently from the temperature derivative of the standard emf of a reversible electrochemical cell. As in the previous case, calorimetric measurements on the separate reactants and products, plus the usual extrapolation, will... [Pg.370]

In order to describe any electrochemical cell a convention is required for writing down the cells, such as the concentration cell described above. This convention should establish clearly where the boundaries between the different phases exist and, also, what the overall cell reaction is. It is now standard to use vertical lines to delineate phase boundaries, such as those between a solid and a liquid or between two innniscible liquids. The junction between two miscible liquids, which might be maintained by the use of a porous glass frit, is represented by a single vertical dashed line, j, and two dashed lines, jj, are used to indicate two liquid phases... [Pg.602]

Figure A3.10.1 (a) A schematic illustration of the corrosion process for an oxygen-rich water droplet on an iron surface, (b) The process can be viewed as a short-circuited electrochemical cell [4],... Figure A3.10.1 (a) A schematic illustration of the corrosion process for an oxygen-rich water droplet on an iron surface, (b) The process can be viewed as a short-circuited electrochemical cell [4],...
Several designs for STM electrochemical cells have appeared in the literature [M]- hr addition to an airtight liquid cell and the tip insulation mentioned above, other desirable features include the incorporation of a reference electrode (e.g. Ag/AgCl in saturated KCl) and a bipotentiostat arrangement, which allows the independent control of the two working electrodes (i.e. tip and substrate) [ ] (figure BL19.11). [Pg.1685]

Migration is the movement of ions due to a potential gradient. In an electrochemical cell the external electric field at the electrode/solution interface due to the drop in electrical potential between the two phases exerts an electrostatic force on the charged species present in the interfacial region, thus inducing movement of ions to or from the electrode. The magnitude is proportional to the concentration of the ion, the electric field and the ionic mobility. [Pg.1925]

The apparatus consists of a tip-position controller, an electrochemical cell with tip, substrate, counter and reference electrodes, a bipotentiostat and a data-acquisition system. The microelectrode tip is held on a piezoelectric pusher, which is mounted on an inchwomi-translator-driven x-y-z tliree-axis stage. This assembly enables the positioning of the tip electrode above the substrate by movement of the inchwomi translator or by application of a high voltage to the pusher via an amplifier. The substrate is attached to the bottom of the electrochemical cell, which is mounted on a vibration-free table [, and ]. A number... [Pg.1941]

Two major sources of ultrasound are employed, namely ultrasonic baths and ultrasonic immersion hom probes [79, 71]- The fonuer consists of fixed-frequency transducers beneath the exterior of the bath unit filled with water in which the electrochemical cell is then fixed. Alternatively, the metal bath is coated and directly employed as electrochemical cell, but m both cases the results strongly depend on the position and design of the set-up. The ultrasonic horn transducer, on the other hand, is a transducer provided with an electrically conducting tip (often Ti6A14V), which is inuuersed in a three-electrode thenuostatted cell to a depth of 1-2 cm directly facing the electrode surface. [Pg.1942]

Figure Bl.28.8. Equivalent circuit for a tliree-electrode electrochemical cell. WE, CE and RE represent the working, counter and reference electrodes is the solution resistance, the uncompensated resistance, R the charge-transfer resistance, R the resistance of the reference electrode, the double-layer capacitance and the parasitic loss to tire ground. Figure Bl.28.8. Equivalent circuit for a tliree-electrode electrochemical cell. WE, CE and RE represent the working, counter and reference electrodes is the solution resistance, the uncompensated resistance, R the charge-transfer resistance, R the resistance of the reference electrode, the double-layer capacitance and the parasitic loss to tire ground.
The combination of electrochemistry and photochemistry is a fonn of dual-activation process. Evidence for a photochemical effect in addition to an electrochemical one is nonnally seen m the fonn of photocurrent, which is extra current that flows in the presence of light [, 89 and 90]. 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 chaimel-flow cells) are constmcted to allow irradiation of the electrode area with UV/VIS light to excite species involved in electrochemical processes and thus promote fiirther reactions. [Pg.1945]

When the reaction between zinc and copper(II) sulphate was carried out in the form of an electrochemical cell (p. 94), a potential difference between the copper and zinc electrodes was noted. This potential resulted from the differing tendencies of the two metals to form ions. An equilibrium is established when any metal is placed in a solution of its ions. [Pg.97]

From the theory of the electrochemical cell, the potential in volts of a silver-silver chloride-hydrogen cell is related to the molarity m of HCI by the equation... [Pg.67]

The concept of the reversed fuel cell, as shown schematically, consists of two parts. One is the already discussed direct oxidation fuel cell. The other consists of an electrochemical cell consisting of a membrane electrode assembly where the anode comprises Pt/C (or related) catalysts and the cathode, various metal catalysts on carbon. The membrane used is the new proton-conducting PEM-type membrane we developed, which minimizes crossover. [Pg.220]

A regenerative fuel cell system can also be a single electrochemical cell in which both the oxidation of fuels (i.e., production of electric power) and reduction of CO2 (to obtain fuels) can be carried out by simply reversing the mode of operation. [Pg.220]

To a 250-ml not-partitioned electrochemical cell, 135 ml of CH3CN, 15 ml ofHiO, 6.20 g of NaBr and 2.82 g of olefin ( ) is added. The mixture, kept at 2(f C, is electrolysed by using the same electrodes as of Example 1, but with a constant current density of 1.7 A being used,until through the cell 4,000 Coulombs have been passed. The reaction mixture is then processed as described in Example 4.2.56 g is obtained of ketone (III), with a yield of 83.2%, as computed relatively to the olefin (I) used as the starting material. [Pg.192]


See other pages where A Electrochemical Cells is mentioned: [Pg.595]    [Pg.221]    [Pg.595]    [Pg.221]    [Pg.85]    [Pg.86]    [Pg.183]    [Pg.351]    [Pg.212]    [Pg.316]    [Pg.600]    [Pg.1686]    [Pg.1926]    [Pg.1942]    [Pg.1947]    [Pg.1948]    [Pg.1948]    [Pg.67]    [Pg.190]    [Pg.191]   


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