Effect of Thallium Ions on Anodic Dissolution of Gold in Alkali–Cyanide Electrolytes at Potentials More Positive Than the NHE Potential

The gold dissolution rate iin solutions containing 0.1 M KOH, 0.1 M KCN, and 2.5 × 10^–7to 1.5 × 10^–5M TlNO₃is studied as a function of potential Eof the electrode whose surface is renewed prior to each experiment, the TlNO₃concentration c, and the time tof the electrode contact with solution. At cexceeding 0.5 × 10^–5M and t 0, the rate is 1.5–2 times that at c= 0. Initial portions of ivs. tcurves in the absence and presence of TlNO₃coincide only at cbelow 10^–6M. Potentiostatic and potentiodynamic measurements show that, at positive E, only small coverages of the electrode surface with thallium are obtained, which make no impact on iat E< 0 and heavily increase it at 0 < E< 0.3 V. The discovered effects are attributed to the formation, during the adsorption of oxidized thallium forms, of dipoles comprising thallium adions and gold atoms. Presumably, the dipoles face the gold with their negative ends and make the potential of zero free charge more negative.     

Kinetics of Anodic Dissolution of Gold in Cyanide Solutions Containing Bismuth Hydroxy Compounds

Effective values of order of the reaction of the gold dissolution process by cyanide ions p, transfer coefficient , and exchange current i ₀ are measured at constant values of the coverage of the gold surface by bismuth adatoms . The constancy of is ensured by maintaining a constant value of the time t during which the electrode is in contact with solution after the renewal of its surface until the instant of taking measurements. The solutions under study contain 2.5 × 10^–6 to 7 × 10^–6 M bismuth hydroxy compounds, 0.1 M KCN, 0.01 M KAu(CN)₂, and 0.1 M KOH. With increasing t, quantities p, , and i ₀ increase from 0.17, 0.1, and 10^–5 A cm^–2, respectively, which are the values typical for the gold dissolution process in plain potassium cyanide solutions, to p 1.1, 0.45, and i ₀ 2 × 10^–4 A cm^–2. The increase in the quantity p by approximately a unity is interpreted as an evidence in favor of the assumption that the presence of bismuth adatoms alters the nature of the limiting stage: the latter starts involving cyanide ions localized outside an adsorption layer, rather than the adsorbed cyanide ions only, as is the case in plain solutions. A comparison of obtained results with the data of similar investigations performed earlier in thallium- and lead-containing solutions shows that possible mechanism of acceleration of anodic process suggested in the previous works may be used for explaining regularities of the gold dissolution process observed in the presence of bismuth adatoms as well.     

Silver Electrodeposition from Cyanide Solutions: Effect of Lead Ions

Effect of lead hydroxy compounds on the process of electrodeposition of silver from cyanide electrolytes is studied on an electrode whose surface is renewed in solution by cutting off a thin layer of metal. This permitted to perform the study on both the freshly renewed electrode and at controlled values of the time of the electrode contact with solution t. Shown is that on the freshly renewed electrode (t<1 s) the presence in the solution of lead ions in concentrations c ₁ on the order of 10^–5 M leads to the process depolarization only in the initial portion of a polarization curve. With c ₁ increased to 10^–4 M the effect of depolarization extends on the entire polarization curve. Keeping the electrode in solution after the renewal of the metal surface magnifies depolarization, and the greater the concentration c ₁, the shorter the time period t required to achieve the same effect. These regularities are attributed to catalytic influence of lead adatoms, whose surface concentration depends on c ₁ and t, as well as on the intensity of their incorporation in the silver deposit.     

Adsorption of n-Butanol on Polycrystalline Silver–Gold Alloys

The adsorption kinetics for n-butanol (c _L = 0.033–1.2 M) on polycrystalline electrodes of silver, gold, and their homogeneous alloys (X _Au = 0.15–0.80) formally obeys the Roginskii–Zel'dovich equation. The steady-state coverage of their surface by the alcohol, _L ^st, is described by the Temkin isotherm. The ratio between the slopes of the _L vs. logt and _L ^st, vs. logc _L dependences perceptibly alters with X _Au. The experimental data are discussed in terms of a quasi-equilibrium competing co-adsorption of water and alcohol at an energetically-nonuniform surface accompanied by a relatively slow redistribution of adsorbate molecules between adsorption centers of different nature. It is shown that quantitative characteristics of the n-butanol adsorption on Ag–Au alloys cannot be calculated in the approximation of additivity of properties on the basis of relevant parameters of adsorption on Ag and Au.     

Kinetic Parameters of Gold Dissolution in Cyanide Solutions: The Effect of Complex Cyanide Ions of Mercury

The kinetics of the gold dissolution in cyanide solutions is studied at constant values of the coverage () of the gold surface by mercury atoms. The constancy of is ensured by maintaining an identical value of the duration (t) of contact of electrode with solution (after renewing its surface by cutting off a thin surface layer of metal) at a potential of –1.3 V, at which the discharge of mercury ions is limited by their diffusion to the electrode. At t = const kinetic dependences of the gold dissolution process correspond to the Tafel equation. Effective values of exchange current i ₀, transfer coefficient , and reaction order by cyanide ions P are determined. With increasing value of their magnitude increases from values 10^–5 A cm^–2, 0.1, and 0.17 that are characteristic of purely cyanide solutions (composition 0.1 M KCN, 0.1 M KOH, and 0.01 M KAu(CN)₂) to i ₀ 2 × 10^–4 A cm^–2, = 0.46, and P 1 at t = 270 s. These results are compared with the data obtained earlier during similar investigations in solutions containing thallium, lead, and bismuth. Common and individual features in the behavior of mercury-containing electrolytes are revealed. It is shown that the possible mechanism of the acceleration of the gold dissolution process in the presence of catalytically active atoms, which had been proposed in these works, may be used also for explaining the action of mercury atoms on this process.     

Kinetics of Anodic Dissolution of Gold in Alkali–Cyanide Solutions: Effect of Lead Ions

Effective order of the gold dissolution reaction by cyanide ions, p, transfer coefficient , and exchange current i ₀are measured at constant coverages of the gold surface by lead adatoms, . Constancy of is ensured by maintaining the time period t, during which the electrode is in contact with solution after the renewal of its surface and before taking measurements, constant. Solutions under study contain (0.5–2) × 10^–5M lead acetate, 0.05–0.2 M KCN, 0.1 M KOH, and 0.01 M KAu(CN)₂. With increasing t, quantities p, , and i ₀increase from, respectively, 0.17, 0.1, and 10^–5A dm^–2(in 0.05 M KCN) to p 1.2, 0.45, and i ₀ 10^–4A dm^–2. The increase in psuggests that the limiting stage alters in the presence of lead adatoms: in addition to adsorbed cyanide ions, as is the case with pure alkali–cyanide solutions, it involves cyanide ions located outside the adsorption layer. A feasible mechanism for the acceleration of gold dissolution by lead adatoms is offered.     

Effect of Thallium Adatoms on Electrode Processes in the System Gold–Cyanide Solutions

The possibility of determining kinetic parameters of the gold electrodeposition in the presence of thallium adatoms is considered. The coverage of the electrode surface by thallium adatoms is monitored. The steady-state values of potential used correspond to current densities i that are directly proportional to the concentration of thallium ions in solution. The procedure is based on the assumption that the rate of incorporation of adatoms is proportional to the product i. With increasing to 0.25, the exchange current and transfer coefficient increase from 5 × 10^–5 A cm^–2 and 0.23 in pure solutions to1.5 × 10^–4 A cm² and 0.6 at = 0.25–0.3, whereas the reaction order by cyanide ions remains practically invariant with increasing . Variations in the kinetic parameters with are compared to similar measurements obtained earlier for the anodic process. These may be made consistent by assuming that mechanisms of cathodic and anodic reactions differ in pure solutions and are identical in the presence of catalytically active adatoms. An explanation to the above regularities is given.     

Solid-Solute Phase Equilibria in Aqueous Solution. XI. Aqueous Solubility and Standard Gibbs Energy of Cadmium Carbonate

The solubilities of CdCO₃ (otavite) in aqueous NaClO₄ solutions have been investigated as a function of ionic strength (0.15 I/mol-kg^–1 5.35, 25°C) and temperature (25°C T 75°C, I = 1.00 mol-kg^–1). A new Chemsage optimization routine was employed to simultaneously evaluate solubility data from this work and other sources, as well as standard electrode potentials determined at different ionic strengths. With the Pitzer equations the solubility constants, , were extrapolated to infinite dilution resulting in log and the ternary ion-interaction parameters ^S_Na,Cd = 0.19 and at 25°C. In addition, the following set of thermodynamic quantities can be derived from the present solubility data for otavite: _f G = –674.2±0.6 kJ-mol^–1; _f H = –755.3±3.4 kJ-mol^–1; S = 93±10 J-mol^–1K^–1. However, the present solubility data are also consistent with a recent determination of the standard entropy of otavite which leads to a recommended set of thermodynamic quantities [_f G (CdCO₃) = –674.2±0.6; _f H (CdCO₃) = –752.1±0.6; S (CdCO₃) = 103.9±0.2].     

Kinetics of Gold Electrodeposition from Cyanide Electrolytes at a Monitored Surface Coverage by Thallium Atoms

A procedure for measuring kinetic parameters of gold electrodeposition in the presence of catalytically active thallium(I) ions while monitoring the coverage of the gold surface by thallium adatoms, , is described. The procedure accounts for the duration of contact between a freshly renewed surface of gold and a thallium-containing solution and assumes that the incorporation rate of thallium adatoms is proportional to and the current density of gold electrodeposition. At = const, kinetic dependences correspond to the Tafel equation. Values of and i ₀ increase with . At = 0.3, 0.6 and i ₀ 3 × 10^–4 A cm^–2, which conforms to values calculated from anodic curves obtained in similar conditions.     

Kinetics of Anodic Dissolution of Gold in Cyanide Solutions Containing Thallium Ions: Potentiostatic Measurements

Effective reaction order by cyanide ions, p, effective transfer coefficient _ef, and exchange current i ₀of the gold dissolution process are measured at a constant surface coverage by thallium adatoms _Tl. The constancy of _Tlis ensured by constant time tof the electrode's contact with solution after renewal of its surface and before starting the measurements. Solutions containing 2.5 × 10^–6to 10^–5M TlNO₃, 0.1 M KCN, and 0.1 M KOH are studied. With an increase in t, quantities p, _ef, and i ₀increase from values typical for pure KCN solutions (0.17, 0.1, and 10^–5A/dm², respectively) to p 1.1, _ef 0.4, and i ₀ 3 × 10^–4A/dm². The increase in pby nearly unity is interpreted as indicating a change in the limiting stage in the presence of thallium ions: in the latter case, it involves not only adsorbed cyanide ions (as in pure cyanide solutions), but also those located beyond the adsorption layer. A possible mechanism explaining the acceleration of gold dissolution in the presence of thallium adatoms is put forward.     

On the role of ion bombardment parameters in AES sputter depth profiling of Ta2O5/Ta with Ar+ and Xe+

Summary In order to study the influence of the ion bombardment parameters on the achievable depth resolution of AES sputter depth profiles, 500 Å thick Ta₂O₅-layers produced by anodic oxidation of polished polycrystalline Ta-substrates were sputter depth profiled with Ar⁺- and Xe⁺-ions in a Scanning Auger Microprobe. The 90%–10% interface widthsz were measured for bombarding ion energies from 0.5 to 5 keV and angles of incidence of 15°, 33° and 56°, respectively.z reduces from 48 Å for Ar⁺-bombardment at = 15° andE = 5 keV to 20 Å when bombarding at = 56° andE = 1 keV. The corresponding values for Xe⁺-bombardment are 31 Å and 18 Å. The influence of the ion bombarding energy and angle on the interface broadening is discussed by means of a simple model. From corresponding evaluations the maximum transportation length of layer species into the substrate is found to be proportional toE ^0.5.

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Zum Einfluß der Ionenbeschußparameter auf die Tiefenauflösung bei der AES-Sputtertiefenprofil-analyse von Ta₂O₅/Ta mit Ar⁺ und Xe⁺

     

Computation of heat capacities of solid state benzene,p-oligophenylenes and poly-p-phenylene

Heat capacities (C_p) of solid benzene, biphenyl,p-terphenyl,p-quaterphenyl, and poly-p-phenylene were analyzed using the ATHAS Scheme of computation. The calculated heat capacities based on approximate vibrational spectra of solid benzene and the series of oligomers containing additional phenylene groups were compared to experimental data newly measured and from the literature to identify possible additional large-amplitude motion. The skeletal heat capacity was fitted to the Tarasov equation to obtain the one- and three-dimensional vibration frequencies ₁ and ₃ using a new optimization approach. Their relationship to the number of phenylene groupsn is: ₁=426.0–150.3/n; and ₃=55.4+81.8/n. Except for benzene, the quantitative thermal analyses do not show significant contributions from large-amplitude motion below the melting temperatures.This work was financially supported by the Div. of Materials Res., NSF, Polymers Program, Grant # DMR 90-00520 and Oak Ridge National Laboratory, managed by Lockheed Martin Energy Research Corp. for the U. S. Department of Energy, under contract number DE-AC05-96OR22464.     

Electrode kinetics in cyanide silver-plating electrolytes at different surface coverages by lead adatoms

Effective values of exchange current i ₀, cathodic and anodic transfer coefficients and , and cathodic and anodic reaction orders with respect to cyanide ions (P _c, P _a) are measured in cyanide silver-plating electrolytes at different surface coverages by lead adatoms . With increasing coverage, i ₀ and increase from 5 × 10^–5 A cm^–2 and 0.24 in pure solutions to 8 × 10^–5 A cm^–2 and 0.3 at = 0.4, with P _c and P _a hardly altering. The cathodic process markedly accelerates at = 0.6, while at 0.5 the kinetics of the cathodic process is unstable. Different effects of lead adatoms on cathodic and anodic gold and silver plating in cyanide solutions are due to lead salts not affecting the metal substrate dissolution mechanism in the latter case.__________Translated from Elektrokhimiya, Vol. 41, No. 4, 2005, pp. 468–474.Original Russian Text Copyright © 2005 by Bek, Shuraeva.     

Effect of Lead Ions on the Kinetics of Gold Deposition from Cyanide Electrolytes

The depolarization of the gold electrodeposition in the presence of lead ions depends on their concentration and the duration of electrode contact with solution preceding a potential scan in an extremum fashion. At constant coverages of the gold surface by lead adatoms , the process rate depends on the overvoltage in accord with the Tafel equation. Effective values of the exchange current i ₀ and transfer coefficient increase with from i ₀ 3 × 10^–5 A cm^–2 and = 0.23 in pure solutions to 3 × 10^–4 A cm^–2 and 0.53 at 0.4. The reaction order by cyanide ions is independent of and equals nearly –0.9. Effects of lead adatoms on the kinetics of cathodic and anodic processes are compared and the obtained data may be brought to conformance given that their mechanisms in pure solutions differ and converge in the presence of lead adatoms.     

Relative thermodynamic stabilities of allyl vinyl and propenyl vinyl ethers

The relative thermodynamic stabilities of a number of isomeric allyl vinyl and propenyl vinyl ethers were determined by chemical equilibration in DMSO solution with KOBu-t as catalyst. From the temperature dependence of the values of the equilibrium constant the parameters G _m , H _m and S _m of isomerization at 298.15 K were evaluated. Propenyl vinyl ethers, owing to their low enthalpy contents, are much more stable than the isomeric allyl vinyl ethers. It appears that in the parent propenyl vinyl ether, the Me group attached to C- of the divinyl ether skeleton has a strong stabilizing effect, comparable to that of alkyl groups in ordinary olefins, on the unsaturated system. In more heavily alkyl-substituted divinyl ethers, however, the stabilizing effects of alkyl groups are less prominent, being comparable to the low stabilization energies of alkyl groups in vinyl ethers, and depend moreover, on the pattern of substitution.     

Gold Dissolution Electrocatalysis in Thiourea Electrolytes in the Presence of Chemisorbed Sulfide Ions

Adding a microscopic quantity of sodium sulfide (～10^?5 M) into acid solutions of thiourea leads to a dramatic acceleration of anodic dissolution of gold. The acceleration effect is greater at larger thiourea concentrations (c) and longer times of the electrode contact with solution (Δt) before the beginning of measurements. The effect diminishes after a polarization curve passes through a maximum at E ? 0.5 V. Regularities of the gold dissolution in a solution containing 0.1 M thiourea and 0.5 M H₂SO₄ at given values of c and Δt are studied with use made of the technique of renewing the electrode surface by cutting off a thin surface layer of metal. The discovered regularities are given an explanation which is based on the assumption that the dissolution process is catalyzed by sulfide ions adsorbed on the electrode surface.     

Stripping Voltammetry of Thallium at a Film Mercury Electrode

The electrochemical dissolution of thallium from the surface of a mercury film electrode was studied in different supporting electrolytes. The effects of the concentration of thallium(I), electrolysis potential and time, and the potential sweep rate on anodic voltammograms were studied. The electrode process in solutions containing EDTA, HCl, and ascorbic acid at a potential sweep rate of 0.020 V/s is reversible. A stripping voltammetric procedure was developed for determining thallium(I) in the concentration range 1 × 10^–9 to 5 × 10^–7 M. The detection limit (3, n = 3) is 5 × 10^–10 M.     

The effect of chemisorbed sulfide ions on the gold electrodeposition from acidic thiocarbamide electrolytes

Introducing sodium sulfide (about 10^?5 M) into acidic thiocarbamide solutions reduces the gold reduction overpotential. The reaction rate passes through a maximum at a potential of 0.1 V. The overpotential depends on the sulfide ion concentration and the time of electrode exposure to solution prior to the beginning of scanning. Transients of potential measured on a renewable gold electrode in thiocarbamide electrolytes containing catalytically active species served as the basis for calculations of the coefficient of trapping of sulfide ions by the growing gold deposit. The kinetics of gold electrodeposition at fixed surface coverages with adsorbed sulfide ions θ is studied. It is shown that at θ = const, the dependence of the reaction rate on the overpotential is described by the Tafel equation. It is shown that with an increase in θ, the effective values of exchange current and transfer coefficient increase from i ₀ ≌ 10^?5 A/cm² and α ≌ 0.25 in pure solutions to α ≌ 0.5 and i ₀ ≌ 10^?4 A/cm² at θ ≥ 0.3 and then remains virtually unchanged. The reaction order decreases in the absolute magnitude, remaining negative. Thus for θ ≌ 0, p _k = ?logi/?logc = ?1, whereas for θ ≥ 0.3, p _k = ?0.3. A possible explanation is proposed for the catalytic effect of the sulfide ion adsorption on the mechanism of the gold reduction from acidic thiocarbamide electrolytes.     

Potential transients on a renewed electrode as a source of information on the surface concentration of catalytically active adatoms

Potential transients on renewable gold and silver electrodes in cyanide solutions containing catalytically active ions of lead and thallium are measured. The transients are recorded both on freshly renewed electrodes and on renewed electrodes kept in solution for specified time periods t. The behavior of transients following a change in the concentration of lead and thallium ions, current density, and t qualitatively conforms to regularities that could be expected if the catalytically active adatoms were inserted into the deposit similarly to the admixtures. Methods for determining coefficients of capture of such adatoms by the growing metal deposit are suggested. Factors that hamper determination of these coefficients and make it worthwhile to select a method for their determination that would use potential transients are considered. The capture coefficient for the incorporation of lead adatoms in the growing silver deposit is nearly 20 times that for gold.__________Translated from Elektrokhimiya, Vol. 41, No. 4, 2005, pp. 460–467.Original Russian Text Copyright © 2005 by Bek, Shuraeva.     

On the crystal chemistry of three copper(II)-arsenates: Cu3(AsO4)2-III,Na4Cu(AsO4)2, and KCu4(AsO4)3

The three copper(II)-arsenates were synthesized under hydrothermal conditions; their crystal structures were determined by single-crystal X-ray diffraction methods:Cu₃(AsO₄)₂-III:a=5.046(2) Å,b=5.417(2) Å,c=6.354(2) Å, =70.61(2)°, =86.52(2)°, =68.43(2)°,Z=1, space group ,R=0.035 for 1674 reflections with sin / 0.90 Å^–1.Na₄Cu(AsO₄)₂:a=4.882(2) Å,b=5.870(2) Å,c=6.958(3) Å, =98.51(2)°, =90.76(2)°, =105.97(2)°,Z=1, space group ,R=0.028 for 2157 reflections with sin / 0.90 Å^–1.KCu₄(AsO₄)₃:a=12.234(5) Å,b=12.438(5) Å,c=7.307(3) Å, =118.17(2)°,Z=4, space group C2/c,R=0.029 for 1896 reflections with sin / 0.80 Å^–1.Within these three compounds the Cu atoms are square planar [4], tetragonal pyramidal [4+1], and tetragonal bipyramidal [4+2] coordinated by O atoms; an exception is the Cu(2)^[4+1] atom in Cu₃(AsO₄)₂-III: the coordination polyhedron is a representative for the transition from a tetragonal pyramid towards a trigonal bipyramid. In KCu₄(AsO₄)₃ the Cu(1)^[4]O₄ square and the As(1)O₄ tetrahedron share a common O—O edge of 2.428(5) Å, resulting in distortions of both the CuO₄ square and the AsO₄ tetrahedron. The two Na atoms in Na₄Cu(AsO₄)₂ are [6] coordinated, the K atom in KCu₄(AsO₄)₃ is [8] coordinated by O atoms.Die drei Kupfer(II)-Arsenate wurden unter Hydrothermalbedingungen gezüchtet und ihre Kristallstrukturen mittels Einkristall-Röntgenbeugungsmethoden ermittelt:Cu₃(AsO₄)₂-III:a = 5.046(2) Å,b = 5.417(2) Å,c = 6.354(2) Å, = 70.61 (2)°, = 86.52(2)°, = 68.43(2)°,Z = 1, Raumgruppe ,R = 0.035 für 1674 Reflexe mit sin / 0.90 Å^–1.Na₄Cu(AsO₄)₂:a = 4.882(2) Å,b = 5.870(2) Å,c = 6.958(3) Å, = 98.51(2)°, = 90.76(2)°, = 105.97(2)°,Z = 1, Raumgruppe ,R = 0.028 für 2157 Reflexe mit sin / 0.90 Å^–1.KCu₄(AsO₄)₃:a = 12.234(5) Å,b = 12.438(5) Å,c = 7.307(3) Å, = 118.17(2)°,Z = 4, Raumgruppe C2/c,R = 0.029 für 1896 Reflexe mit sin / 0.80 Å^–1.Die Cu-Atome in diesen drei Verbindungen sind durch O-Atome quadratisch planar [4], tetragonal pyramidal [4 + 1] und tetragonal dipyramidal [4 + 2]-koordiniert; eine Ausnahme ist das Cu(2)^{[4 + 1]}-Atom in Cu₃(AsO₄)₂-III: Das Koordinationspolyeder stellt einen Vertreter des Übergangs von einer tetragonalen Pyramide zu einer trigonalen Dipyramide dar. In KCu₄(AsO₄)₃ haben das Cu(1)^[4]O₄-Quadrat und das As(1)O₄-Tetraeder eine gemeinsame O—O-Kante von 2.428(5) Å, was eine Verzerrung der beiden Koordinationsfiguren CuO₄-Quadrat und AsO₄-Tetraeder bedingt. Die zwei Na-Atome in Na₄Cu(AsO₄)₃ sind durch O-Atome [6]-koordiniert, das K-Atom in KCu₄(AsO₄)₃ ist [8]-koordiniert.

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Zur Kristallchemie dreier Kupfer (II)-Arsenate: Cu₃(AsO₄)₂-III, Na₄Cu(AsO₄)₂ und KCu₄(AsO₄)₃