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Potential Electrolysis

In order to find optimal conditions for the soluble copper determination we examined the influence of electrolysis potential, electrolysis time, and the solution stirring rate on the accuracy and sensitivity of determination. We found that the optimal parameters for PSA determination of copper were electrolysis potential of -0.9 V vs. 3.5 mol/dm Ag/AgCl, electrolysis time of 300 s, and solution stirring rate of 4000 rpm. The soluble copper content in samples investigated in this study varied from 1.85 to 4.85 ppm. Very good correlation between the copper content determined by PSA and AAS indicated that PSA could be successfully applied for the soluble copper content determination in various dental materials. [Pg.373]

Make the connections to the polarographic analyser and adjust the applied voltage to —0.8 V, i.e. a value well in excess of the deposition potential of lead ions. Set the stirrer in motion noting the setting of the speed controller, and after 15-20 seconds, switch on the electrolysis current and at the same time start a stopclock allow electrolysis to proceed for 5 minutes. On completion of the electrolysis time, turn off the stirrer, but leave the electrolysis potential applied to the cell. After 30 seconds to allow the liquid to become quiescent, replace the electrolysis current by the pulsed stripping potential and set the chart recorder in motion. When the lead peak at ca 0.5 V has been passed, turn... [Pg.625]

Entries Electrolysis potential E(V) Coulometry Products n(F mol - ) (yield of conversion %) ... [Pg.1011]

The electrolysis was carried out with a potential programme including only two plateaux, because of weak poisoning of the electrode surface, with a first, one at 0.2 V/RHE, during 0.2 s for the adsorption of glyoxal, and a second one at 1.9 V/RHE corresponding to the electrolysis potential (20 s). [Pg.468]

On the other hand, for the highest electrolysis potential (2.13 V/RHE), glyoxal conversion is more important, and the amount of oxalic acid increases, whereas the concentration of FA decreases. This confirms the selectivity dependence of the C-C bond breaking with the electrode potential, and shows that the optimal potential for a maximal selectivity towards GA production is close to 2.13 V/RHE. [Pg.469]

Fry and Powers51 examined the electroreduction of PhCHBrCMe3 (29) on carbon electrodes and observed a similar product dependence on the electrolysis potential (equation 25). They observed an interesting increase in the meso/dl ratio of head-to-head coupled... [Pg.1016]

Fig. 6. Thermodynamic and electrochemical values for water dissociation to H2 and O2 as a function of temperature.3 The curves without squares are calculated at one bar, for liquid water through 100 °C and for steam at higher temperatures. The high pressure utilized in this additional curve (pFhO = 500 bar pfh = pOz = 1 bar) is of general interest as (i) the electrolysis potential is diminished compared to that of water at 1 bar, (ii) the density of the high pressure fluid is similar to that the liquid and (iii) may be generated in a confined space by heating or... Fig. 6. Thermodynamic and electrochemical values for water dissociation to H2 and O2 as a function of temperature.3 The curves without squares are calculated at one bar, for liquid water through 100 °C and for steam at higher temperatures. The high pressure utilized in this additional curve (pFhO = 500 bar pfh = pOz = 1 bar) is of general interest as (i) the electrolysis potential is diminished compared to that of water at 1 bar, (ii) the density of the high pressure fluid is similar to that the liquid and (iii) may be generated in a confined space by heating or...
In the presence of higher concentrations of phosphines, di- and trisub-stituted products may be obtained (727), and interesting examples of the stereospecific formation of isomers by electron-transfer catalysis have been reported (123,124). The flyover complex [Co2(CO)4 /u,-C6(CF3)6 ] (53) forms the bis(phosphite) derivative [Co2(CO)2 P(OMe)3 2(/u-C6(CF3)6 ] when reduced in the presence of excess P(OMe)3, but two different isomers can be exclusively produced depending on the applied electrolysis potential. At the potential of the one-electron reduction of 53 (E = -0.1 V vs Ag/AgCl), isomer 54 is formed, but, at a potential appropriate for the reduction of 54 ( = —0.7 V), quantitative conversion to isomer 55 is achieved. The reaction is electrocatalytic in both cases. [Pg.109]

It was established previously that the selectivity towards the production of acetic acid is increased when the electrolysis potential is set in the so-called oxygen region. This is understandable, because the reaction requires an extra oxygen atom which can be provided by an oxygenated Pt(OH, OOH, O) species. The adsorbed acetyl is the precursor of the acetic acid (steps 4 and 5) and the COads gives carbon dioxide (steps 5, 5" and 6 ). [Pg.469]

Analyses for "copper, cadmium, and lead were carried out continually by DPASV. Zinc determinations were excluded to permit use of a lower electrolysis potential. The samples were analyzed at pH 4.9 by sparging with carbon dioxide. An 8-min. electrolysis at —1.0 V vs. silver/ silver chloride and a 25-mV pulse were used during the Seattle-Saanich portion of the trip (Leg 1) while a 10-min. electrolysis and a 50-mV pulse were used from Saanich to Seattle (Leg 2). Application of the DPASV technique resulted in greater sensitivity and thus shorter plating times for the low levels encountered. It also afforded better resolution for "copper than linear-sweep ASV. It should be pointed out, however, that DPASV does not result in shorter analyses times because the stripping portion of the analysis is very slow. Nevertheless, it is worthwhile to limit the time of electrolysis because this also reduces the concentrations of interfering metals accumulated in the mercury fllm. Under the... [Pg.93]

Fig. 14.23 Microtiter plate anodic electrooxidation from lb to form 3ba in the presence of CH3OH, c(lb) = 4mM, c(lu) = 50mM, c(CH3OH) = 2M, electrolysis potential E = +0.4 V vs. id fc+ (a) steady-state microdisk electrode (d = 25 pm) cyclic voltammetry during electrolysis, v = 0.02 V s 1, times after start of electrolysis indicated, (b) current development during electrolysis, (c) steady-state voltammograms before (1) and after 900 s of electrolysis with (3) and without (2) mixing by convection. (Figure reprinted from Markle et al.72). Copyright Elsevier Ltd. (2005)... Fig. 14.23 Microtiter plate anodic electrooxidation from lb to form 3ba in the presence of CH3OH, c(lb) = 4mM, c(lu) = 50mM, c(CH3OH) = 2M, electrolysis potential E = +0.4 V vs. id fc+ (a) steady-state microdisk electrode (d = 25 pm) cyclic voltammetry during electrolysis, v = 0.02 V s 1, times after start of electrolysis indicated, (b) current development during electrolysis, (c) steady-state voltammograms before (1) and after 900 s of electrolysis with (3) and without (2) mixing by convection. (Figure reprinted from Markle et al.72). Copyright Elsevier Ltd. (2005)...
Nevertheless, CO2 reduction does not take place easily, and the actual electrolysis potentials for CO2 reduction are much more negative in most cases than the equilibrium ones. The reason is that the intermediate species CO2, formed by an electron transfer to a CO2 molecule, proceeds as the first step at highly negative potential, such as -2.21 V vs. saturated calomel electrode (SCE) measured in dimethyl fonnamide (DMF), as discussed later in detail. [Pg.92]


See other pages where Potential Electrolysis is mentioned: [Pg.508]    [Pg.54]    [Pg.94]    [Pg.188]    [Pg.176]    [Pg.176]    [Pg.837]    [Pg.840]    [Pg.850]    [Pg.504]    [Pg.647]    [Pg.463]    [Pg.54]    [Pg.171]    [Pg.174]    [Pg.184]    [Pg.199]    [Pg.93]    [Pg.88]    [Pg.100]    [Pg.101]    [Pg.101]    [Pg.104]    [Pg.111]    [Pg.115]    [Pg.91]    [Pg.210]    [Pg.211]    [Pg.647]    [Pg.76]    [Pg.156]    [Pg.605]    [Pg.88]    [Pg.100]    [Pg.101]    [Pg.101]    [Pg.104]   
See also in sourсe #XX -- [ Pg.3 , Pg.70 , Pg.700 , Pg.701 , Pg.706 , Pg.707 ]

See also in sourсe #XX -- [ Pg.700 , Pg.701 , Pg.703 , Pg.706 , Pg.707 ]




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Cells for Controlled Potential Electrolysis

Constant cathode potential electrolysis

Constant potential coulometry electrolysis

Constant potential electrolysis

Controlled potential difference electrolysis

Controlled potential difference electrolysis interface

Controlled potential, electrolysis voltammetry

Controlled-Potential Bulk Electrolysis

Controlled-potential electrolysi

Controlled-potential electrolysis electrode geometry

Controlled-potential electrolysis equipment

Electrochemistry Cell potential Electrolysis

Electrode potentials Electrolysis

Electrolysis circuit, controlled potential

Electrolysis controlled potential

Electrolysis potential-current curves

Electrolysis, at controlled potential

Kolbe electrolysis critical potential

Poly electrolysis, controlled potential

Polymerization electrolysis, controlled potential

Potential s. Electrolysis

Potential step electrolysis

Significance of Controlled Potential Electrolysis

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