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Current continuity

End Point Determination Adding a mediator solves the problem of maintaining 100% current efficiency, but does not solve the problem of determining when the analyte s electrolysis is complete. Using the same example, once all the Fe + has been oxidized current continues to flow as a result of the oxidation of Ce + and, eventually, the oxidation of 1T20. What is needed is a means of indicating when the oxidation of Fe + is complete. In this respect it is convenient to treat a controlled-current coulometric analysis as if electrolysis of the analyte occurs only as a result of its reaction with the mediator. A reaction between an analyte and a mediator, such as that shown in reaction 11.31, is identical to that encountered in a redox titration. Thus, the same end points that are used in redox titrimetry (see Chapter 9), such as visual indicators, and potentiometric and conductometric measurements, may be used to signal the end point of a controlled-current coulometric analysis. For example, ferroin may be used to provide a visual end point for the Ce -mediated coulometric analysis for Fe +. [Pg.500]

Continuous current rating (CMR) to carry the circuit current continuously. [Pg.312]

Laufblld, n. motion picture, -fanger, m.. -kammer,/. motion-picture camera, -werfer, m. motion-picture projector, laufen, v.i. run go, move, turn leak. — lau-fend, p.a. running, current continuous consecutive (numbers). — laufendes Bad, Dye-ing) standing bath. [Pg.271]

Able to carry starter rated full-load current continuously ... [Pg.224]

Fuel cells. In the fuel-cell mode of operation, reactants are fed into the cell (or battery) continuously while reaction products are removed continuously. Hence, fuel cells (the more appropriate term, e/ battery, is not commonly used) can deliver current continuously for a considerable length of time that depends primarily on external reactant storage. [Pg.343]

The shape of the hydrogenase catalytic voltammograms shown in Fig. 17.14 also changes as the temperamre is raised. At 10 °C, the current tends towards a plateau at high overpotential as catalysis becomes limited by the inherent turnover frequency of the enzyme, but at higher temperamres, the current continues to increase linearly with electrochemical driving force. This has been attributed to a range of different... [Pg.617]

The shape of the voltammogram can be qualitatively explained as follows on increasing the potential from the region where R is stable, anodic current starts to flow as the potential approaches E° for the O/R couple. The current continues to increase with increasing potential until the rate of consumption... [Pg.176]

Remediation currently continues at this site. Recovery of LNAPL will continue for the next few years. Further expansion of the biological treatment system is... [Pg.365]

Scientists are interested in superconductors because they have a number of properties that arise from their lack of resistance. For example, once a current is induced in a circuit made with a superconducting material, the current continues to flow through the circuit indefinitely, without ever diminishing. Also, superconductors have the ability to completely repel magnetic field lines. This means that a magnet placed over a superconductor hovers in mid-air, as shown in Figure 4.25. [Pg.206]

Laboratory studies of the rearrangement process began with semi-continuous operation in a single, 200-mL, glass reactor, feeding 1 as a liquid and simultaneous distillation of 2,5-DHF, crotonaldehyde and unreacted 1. Catalyst recovery was performed as needed in a separatory funnel with n-octane as the extraction solvent. Further laboratory development was performed with one or more 1000-mL continuous reactors in series and catalyst recovery used a laboratory-scale, reciprocating-plate, counter-current, continuous extractor (Karr extractor). Final scale-up was to a semiworks plant (capacity ca. 4500 kg/day) using three, stainless steel, continuous stirred tank reactors (CSTR). [Pg.333]

Note that summation of (1.1) multiplied by Fzi over all i yields, taking into account (1.2) and (1.4), the total electric current continuity equation... [Pg.5]

Equation (1.57a) implies that in the locally electro-neutral ambipolar diffusion concentration of both ions evolves according to a single linear diffusion equation with an effective diffusivity given by (1.57b). Physically, the role of the electric field, determined from the elliptic current continuity equation... [Pg.17]

By the current continuity (1.11a) in a one-dimensional system I is spatially invariant, that is... [Pg.17]

The stationary system, e.g., (5.3.1) (5.3.5) is replaced by its time-dependent counterpart. In this counterpart, the Poisson equation is replaced by the total current continuity equation (1.5), obtained as a linear combination of the original equations. The resulting system is then solved by quasilinearization [9] with a simultaneous solution of quasilinearized equations and subsequent Newton s iterations at each time step. Integration is continued in time until the steady state is reached. This numerical procedure is a modification of that suggested by Mock in [10]. [Pg.180]

The part of the plant yielding the odor, after having been braised or out into small pieces, is to be placed in tbe colandered vessel, or on the perforated bottom, with as muoh water only as Is necessary to drench the material and when the oil to be obtained is heavier than water, the density of the latter must be increased by nearly saturating it with table salt, which also raises its boiling point from 212" to 220°. The head of the still —Fig. 385—iB then put in place, and the joints closed. Steam iB next let on through the pipe, o, and the current continued until oily distillate ceases to come over. [Pg.670]

The most frequently used contactors in full-scale waste water ozonation systems are bubble column reactors equipped with diffusers or venturi injectors, mostly operated in a reactor-in-series counter-current continuous mode. Many full-scale ozone reactors are operated at elevated pressure (2-6 barabs) in order to achieve a high ozone mass transfer rate, which in turn increases the process efficiency. [Pg.29]

The main feature of a continuous process is that the final expl product does not remain in the app for a prolonged period of time and the quantiry accumulated at any period of time is much smaller than that in the batch process. The large quantity of expl material accumulated in a batch process, especially at the end of exothermic nitration,presents a serious safety hazard which is more or less absent in current continuous processes... [Pg.284]

The results of this calculation for the above-mentioned decomposition experiment are given in Fig. 6.14 by the continuous lines. The crosses illustrate the variation of the concentration of dithionite and sulphite in solution obtained by titration of samples taken at fixed times. It can be seen that the concentrations obtained by calculation from the experimental currents (continuous line) are in good agreement with the ones obtained by titration (crosses). Note also that the increase of the concentration of sulphite is twice as high as the drop of the sodium dithionite concentration. Indeed, for each dithionite ion that is decomposed, two sulphite ions are... [Pg.188]


See other pages where Current continuity is mentioned: [Pg.1926]    [Pg.499]    [Pg.511]    [Pg.42]    [Pg.174]    [Pg.357]    [Pg.239]    [Pg.430]    [Pg.125]    [Pg.638]    [Pg.81]    [Pg.435]    [Pg.218]    [Pg.32]    [Pg.7]    [Pg.36]    [Pg.35]    [Pg.180]    [Pg.168]    [Pg.259]    [Pg.89]    [Pg.227]    [Pg.395]    [Pg.342]    [Pg.87]    [Pg.1578]    [Pg.174]    [Pg.363]    [Pg.30]    [Pg.193]    [Pg.145]   
See also in sourсe #XX -- [ Pg.43 , Pg.45 , Pg.165 , Pg.221 ]




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Cathodic protection continued current density requirements

Cathodic protection continued current measurement

Cathodic protection continued current requirements

Cathodic protection continued current-measuring

Cathodic protection continued impressed-current

Cathodic protection continued stray-current

Continuous counter-current ion-exchang

Continuous current capacity

Continuous current generation

Continuous current ratings

Membrane (continued current

Rated continuous current capacity

Sampled-current voltammetry continued

Separator continuous counter-current

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