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Continuous Charge

Electrodeposition of metals can be performed under different electrochemical modes. In the work mentioned in Ref. [18], it was performed in potentiostatic mode. The potential value for formation of platinum nanoparticles is —25 mV vs. SCE the deposition is performed from 2.5 mM solution of H2[PtCl6] in 50 mM KCl. The size of nanoparticles formed depends on the reduction charge. Continuous monitoring of the charge in potentiostatic mode is provided by different potentiostats, for example, by Autolab-PG-stat (EcoChemie, The Netherlands). Conditions for deposition of other metals should be selected according to their electrochemical properties. [Pg.323]

So the dilemma is Where does the energy come from that is pouring out of the charge continuously ... [Pg.658]

On a commercial scale, hexamine is manufactured from anhydrous NHi and a 45% solution of methanol-free formaldehyde. These raw materials, plus recycle mother liquor, arc charged continuously ai carefully controlled rates 10 a high-velocity reactor. Tile reaction is exothermic. "Die reactor effluent is discharged into a vacuum evaporator which also serves as a... [Pg.773]

Consider a region of S in our neighbourhood (this is our three-dimensional space), where there exists an electromagnetic field E, B and an associated current J. Let these three vector quantities obey Ampere s Eq. (9). Operate with V- on (10) and substitute Eq. (10) to get the charge continuity condition [62, p. 2] ... [Pg.346]

The stable products that escaped the geminate backward reaction are not survived forever. They meet in the bulk with partners separated from other pairs, and in these encounters the reverse transfer of energy or charge continues to the point of their disappearance. This bimolecular reaction is represented by terms that are proportional to Na in Eqs. (3.114) and (3.127). These terms omitted in Eqs. (3.135) as insignificant during the geminate stage of transfer, will be restored and discussed in Section VIII. [Pg.169]

Consider a liquid feed stream containing reactant species A entering an MSMPR crystallizer at a volumetric flow rate F. A solid reactant B is also charged continuously at a molar flow rate W. The solid reactant B dissolves, and reacts with A in the liquid phase in the presence of an inert solvent S. The reaction rate can be generally given as a function of the concentrations of the reactant species, (c). An amount of product P in excess of the solubility limit precipitates out of the solution as a solid product. [Pg.351]

Sodium sulfate. A single-hearth furnace like that shown in Fig. 19-24g is used. Sodium chloride and sulfuric acid are charged continuously to the center of the pan, and the rotating scrapers gradually work the reacting mass to the periphery, where the sodium sulfate is discharged at 540°C (1000°). Pans are 3.3 to 5.5 m (11 to 18 ft) in diameter and can handle 5500 to 9000 kg/d (12,000 to 20,000 lbm/d) of salt. Rotary kilns also are used for this purpose. Such a unit 1.5 m (4.9 ft) in diameter by 6.7 m (22 ft) has a capacity of... [Pg.38]


See other pages where Continuous Charge is mentioned: [Pg.89]    [Pg.414]    [Pg.138]    [Pg.1219]    [Pg.2070]    [Pg.2127]    [Pg.254]    [Pg.78]    [Pg.217]    [Pg.220]    [Pg.163]    [Pg.505]    [Pg.168]    [Pg.262]    [Pg.404]    [Pg.79]    [Pg.312]    [Pg.89]    [Pg.352]    [Pg.578]    [Pg.726]    [Pg.414]    [Pg.223]    [Pg.389]    [Pg.121]    [Pg.197]    [Pg.638]    [Pg.117]    [Pg.310]    [Pg.223]    [Pg.76]    [Pg.1042]    [Pg.1827]    [Pg.91]    [Pg.55]    [Pg.352]    [Pg.578]    [Pg.608]    [Pg.352]    [Pg.578]   
See also in sourсe #XX -- [ Pg.17 ]




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