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Cell potential electrode potentials

The first difference between these two batteries is the voltage they produce a watch battery produces about 3 V and a lead-acid cell about 2 V. The obvious cause of the difference in emf are the different half-cells. The electrode potential E is the energy, expressed as a voltage, when a redox couple is at equilibrium. [Pg.303]

Generally, a continuous recording of electrically available data - for example, current, cell voltage, electrode potentials, temperatures - is beneficial to supervise the proper procedure of each experiment. Especially in case of a failure this will be a valuable help to find the reason. Today, the best way is to use a data acquisition system in a computer that offers the results directly for further calculations, for example, integration of the consumed current (converted charge). For continuously operated experiments the addition of scales, which acquire the weight of input and output reservoirs, will be advantageous in order to supervise the mass balances continuously. [Pg.61]

L electromotive force, emf (in an electrochemical cell) equilibrium electrode potential in volts... [Pg.5]

Half-reactions, half-cells and electrode potentials... [Pg.28]

Figure 19. Experimental steady-state cell current electrode potential behavior. Figure 19. Experimental steady-state cell current electrode potential behavior.
Figure 3.4. Fuel cell negative electrode potential 0, and positive electrode potential 0., as a function of current. The main cause of the diminishing potential difference A0., for increasing current is at first incomplete electrocatalysis at the electrodes, for larger currents also ohmic losses in the electrolyte solution, and finally a lack of ion transport (cf. Bockris and Shrinivasan, 1969). From B. Sorensen, Renewable Energy, 2004, used by permission from Elsevier. Figure 3.4. Fuel cell negative electrode potential 0, and positive electrode potential 0., as a function of current. The main cause of the diminishing potential difference A0., for increasing current is at first incomplete electrocatalysis at the electrodes, for larger currents also ohmic losses in the electrolyte solution, and finally a lack of ion transport (cf. Bockris and Shrinivasan, 1969). From B. Sorensen, Renewable Energy, 2004, used by permission from Elsevier.
Half-cell potential The potential of an electrochemical half-cell measured with respect to the standard hydrogen electrode. Half-life, fi/i The time interval during which the amount of reactant has decreased by one half. [Pg.1109]

Lines 23, that is, 23(0), 23(-2), etc., represent the equilibrium half-cell or electrode potential of iron as a function of Fe2+ activity. [Pg.63]

Basic equations for almost every subfield of electrochemistry from first principles, referring at all times to the soundest and most recent theories and results unusually useful as text or as reference. Covers coulometers and Faraday s Law, electrolytic conductance, the Debye-Hueckel method for the theoretical calculation of activity coefficients, concentration cells, standard electrode potentials, thermodynamic ionization constants, pH, potentiometric titrations, irreversible phenomena. Planck s equation, and much more, a indices. Appendix. 585-item bibliography. 197 figures. 94 tables, ii 4. 478pp. 5-% x 8. ... [Pg.287]

We can better understand the oxidizing or reducing tendencies of substances by studying electrochemical cells and electrode potentials. [Pg.355]

To develop a useful list of relative half-cell or electrode potentials, we must have a carefully delined reference electrode that is adopted by the entire chemical community. The standard hydrogen electrode, or the normal hydrogen electrode, is such a half-cell,... [Pg.636]

I or each of the following half-cells, compare electrode potentials calculated from (I) concentration and (2) activity data,... [Pg.653]

MTL cells. The other simple factor is the relatively low cell potential. Cell potentials at the power point were 100 mV, i.e., about 35% of E° ph = 2 of the cell. Most of this deficiency can be ascribed to selectivity of electrodes being only partial. The two loss-factors together account for reduction of S.E.E. by a factor of 12. [Pg.305]

Half-cell reactions cannot be stndied in isolation all that can be measnred is the difference in potential (A ) when two half-cells are linked to form an electrochemical cell. Relative electrode potentials for half-cells are obtained by reference to a standard half-cell, the hydrogen electrode that is assigned an Eq of 0.0 V. [Pg.54]

The basic corrosion instrumentation requirement involves the measurement of potential difference. Currents are measured as the potential across a resistor (R ) as shown in Fig. 1.2, where the potential difference is again determined with an operational amplifier. More sophisticated measurements such as polarisation characteristics and zero resistance ammetry involve the use of potentiostats which again use operational amplifiers in a differential mode. The potentiostat is an instrument for maintaining the potential of an electrode under test at a fixed potential compared with a reference cell, and the basic circuit is similar to that for potential measurement with the earth return circuit broken to an auxiliary electrode in the electrochemical cell. Such a circuit would maintain the potential of the test electrode at the reference cell potential. This potential may be varied by inserting a variable potential source (V ) in the input circuit as shown in Fig. 1.3. The actual cell potential (V ) and the current required to polarise the test electrode to this potential may be measured using the basic circuits shown in Figs. 1.1 and 1.2 respectively. [Pg.13]

Identical metab in contact with solutions of different concentrations The metal dissolves from the electrode immersed in a dilute solution, and is deposited on the electrode that is immersed in a more concentrated solution. The corrosion stops when the electrolyte concentration is homogeneous at the interfaces of both of electrodes. The other type of electrochemical concentration cell is known as a differential aeration cell. The electrode potential difference in this case results from different oxygen aeration of the electrodes. This type of corrosion initiates crevice corrosion in aluminum or stainless steel when exposed to a chloride environment. [Pg.32]

Throughout these sections, the lUPAC (Stockholm) conventions for cells and electrode potentials are used. [Pg.140]


See other pages where Cell potential electrode potentials is mentioned: [Pg.465]    [Pg.5]    [Pg.303]    [Pg.303]    [Pg.305]    [Pg.307]    [Pg.2498]    [Pg.92]    [Pg.354]    [Pg.356]    [Pg.358]    [Pg.360]    [Pg.362]    [Pg.364]    [Pg.366]    [Pg.368]    [Pg.189]    [Pg.653]    [Pg.127]    [Pg.29]    [Pg.37]    [Pg.5]    [Pg.277]   
See also in sourсe #XX -- [ Pg.561 ]




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Reference electrode (half cell) potential measurements

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