Lead, electrodeposition

Agullo E, Gonzalez-Garcia J, Exposito E et al (1999) Influence of an ultrasonic field on lead electrodeposition on copper using a fluoroboric bath. New J Chem 23 95-101... 

Studies on lead electrodeposition on conducting solid substrates are related mainly to electrocatalysis, searching for alternative collectors/grids for lead-acid batteries, as well as for removing Pb(II) ions from aqueous solutions and stripping for analytical purposes. 

Properties of thin layers of lead electrodeposited on vitreous carbon have been found identical with that of metallic lead [304]. Therefore Pb and Pb02 coated reticulated vitreous carbon (RVC) electrodes [185] can be applied as electrodes in lead-acid batteries, as reviewed in [305]. The deposition of lead on carbon is through the diffusion-controlled process with instantaneous or progressive nucleation, for high and low Pb + concentration, respectively, and three-dimensional growth mechanism. The number of nucleation sites increases with deposition overpotential, as shown for vitreous [306] and glassy carbon [307] electrodes. The concentration dependence of the nucleation... 

Kawamoto (2) developed a two-dimensional model that is based on a double iterative boundary element method. The numerical method calculates the secondary current distribution and the current distribution within anisotropic resistive electrodes. However, the model assumes only the initial current distribution and does not take into account the effect of the growing deposit. Matlosz et al. (3) developed a theoretical model that predicts the current distribution in the presence of Butler-Volmer kinetics, the current distribution within a resistive electrode and the effect of the growing metal. Vallotton et al. (4) compared their numerical simulations with experimental data taken during lead electrodeposition on a Ni-P substrate and found limitations to the applicability of the model that were attributed to mass transfer effects. 

Electrodeposition and the characterization of alloys and composite materials Mechanistic aspects of lead electrodeposition Electrophoretic deposition of ceramic materials onto metal surfaces Metal oxides for energy conversion and storage Electrochemical aspects of chemical mechanical polishing... 

Nikolic ND, Popov KI, Zivkovic PM, Brankovic G (2013) A new insight into the mechanism of lead electrodeposition ohmic-diffusion control of the electrodeposition process. J Electroanal Chem 691 66-76... 

Nikolic ND, Popov KI (2014) A new approach to the understanding of the mechanism of lead electrodeposition. In Djokic SS (ed) Electrodeposition and surface finishing, modem aspects of electrochemistry, vol 57. Springer, New York, pp 85-132... 

Popov KI, Pavlovic MG, Stojilkovic ER, Stevanovic ZZ (1997) The current density distribution on stationary wire electrodes during copper and lead electrodeposition. Hydrometallurgy 46 321-336... 

Fig. 2.11 Polarization curve for lead electrodeposition from 0.50 M Pb(N03)2 in 2.0 M NaNOa...

Copper is universally used as the metal plating for tape because it can be easily laminated with copper and the various plastic tapes. Copper is readily etched and has excellent electrical and thermal conductivity in both electrodeposited and roUed-annealed form. The tape metal plating is normally gold- or tin-plated to ensure good bondabiUty during inner- and outer-lead bonding operations and to provide better shelf life and corrosion resistance. 

Solvent for Electrolytic Reactions. Dimethyl sulfoxide has been widely used as a solvent for polarographic studies and a more negative cathode potential can be used in it than in water. In DMSO, cations can be successfully reduced to metals that react with water. Thus, the following metals have been electrodeposited from their salts in DMSO cerium, actinides, iron, nickel, cobalt, and manganese as amorphous deposits zinc, cadmium, tin, and bismuth as crystalline deposits and chromium, silver, lead, copper, and titanium (96—103). Generally, no metal less noble than zinc can be deposited from DMSO. 

Electrodeposition. Electro deposition, the most important of the unit processes in electrorefining, is performed in lead- or plastic-lined concrete cells or, more recently, in polymer—concrete electrolytic cells. A refinery having an aimual production of 175,000 t might have as many as 1250 cells in the tank house. The cells are multiply coimected such that anodes and cathodes are placed alternately and coimected in parallel. Each cell is a separate unit and electrically coimected to adjacent cells by a bus bar. 

In the field of electrowinning and electrorefining of metals, titanium has an advantage as a cathode, upon which copper particularly can be deposited with finely balanced adhesion that allows the electrodeposited metal to strip easily when required. Titanium anodes are also being employed as a replacement for lead or graphite in the production of electrolytic manganese dioxide. 

Magnetite may also be used in combination with lead or electrodeposited onto a titanium substrate". The latter anode system has been shown to exhibit good operating characteristics in seawater but at present it is only of academic interest. 

Cathodic electrodeposition of microcrystalline cadmium-zinc selenide (Cdi i Zn i Se CZS) films has been reported from selenite and selenosulfate baths [125, 126]. When applied for CZS, the typical electrocrystallization process from acidic solutions involves the underpotential reduction of at least one of the metal ion species (the less noble zinc). However, the direct formation of the alloy in this manner is problematic, basically due to a large difference between the redox potentials of and Cd " couples [127]. In solutions containing both zinc and cadmium ions, Cd will deposit preferentially because of its more positive potential, thus leading to free CdSe phase. This is true even if the cations are complexed since the stability constants of cadmium and zinc with various complexants are similar. Notwithstanding, films electrodeposited from typical solutions have been used to study the molar fraction dependence of the CZS band gap energy in the light of photoelectrochemical measurements, along with considerations within the virtual crystal approximation [128]. 

The formation of colloidal sulfur occurring in the aqueous, either alkaline or acidic, solutions comprises a serious drawback for the deposits quality. Saloniemi et al. [206] attempted to circumvent this problem and to avoid also the use of a lead substrate needed in the case of anodic formation, by devising a cyclic electrochemical technique including alternate cathodic and anodic reactions. Their method was based on fast cycling of the substrate (TO/glass) potential in an alkaline (pH 8.5) solution of sodium sulfide, Pb(II), and EDTA, between two values with a symmetric triangle wave shape. At cathodic potentials, Pb(EDTA)2 reduced to Pb, and at anodic potentials Pb reoxidized and reacted with sulfide instead of EDTA or hydroxide ions. Films electrodeposited in the optimized potential region were stoichiometric and with a random polycrystalline RS structure. The authors noticed that cyclic deposition also occurs from an acidic solution, but the problem of colloidal sulfur formation remains. 

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