The Experts below are selected from a list of 4683 Experts worldwide ranked by ideXlab platform

Kosuke Izutsu - One of the best experts on this subject based on the ideXlab platform.

Takashi Kakiuchi - One of the best experts on this subject based on the ideXlab platform.

Yutaka Aoki - One of the best experts on this subject based on the ideXlab platform.

  • Liquid Junction Potential between different solvents. A Junction with an alkali metal salt as electrolyte
    Journal of Electroanalytical Chemistry, 1992
    Co-Authors: Kosuke Izutsu, Toshio Nakamura, Yutaka Aoki
    Abstract:

    Abstract The characteristics of the three components of a Liquid Junction Potential between different solvents were studied at a Junction with an alkali metal salt as the electrolyte. As for a Junction with a tetraalkylammonium salt as the electrolyte, the equation previously reported for component (a) was proved to be valid in many cases. Component (b) at H 2 O/organic solvent and MeOH/dipolar aprotic solvent Junctions also behaved similarly to that at a Junction with a tetraalkylammonium salt. At Junctions between aprotic solvents, however, lithium and sodium ions did not make an appreciable contribution to component (b), even when this was expected theoretically. This fact was found to be the cause of the apparently different behavior of component (c) in the case of salts of these metal ions. Thus component (c) can be considered to be almost independent of electrolyte species and concentrations, even when alkali metal salts are used as the electrolyte.

  • Liquid Junction Potential between different solvents: A Junction with different electrolytes on the two sides
    Journal of Electroanalytical Chemistry, 1992
    Co-Authors: Kosuke Izutsu, Mitsuo Muramatsu, Yutaka Aoki
    Abstract:

    Abstract The characteristics of the Liquid Junction Potential (ljp) between different solvents were investigated using different electrolytes on the two sides of a Junction, denoted as c 1 MX(S 1 )| c 2 NY(S 2 ). The ljp consists of three components, a, b and c, as reported previously. The calculated values of components a and b were obtained by numerical integration of the following equations, E j (a) = ( − RT / F )∫ S 1 S 2 {( t M – t X ) d ln a MX + ( t N – t Y ) d ln a NY} E j (b) = ( − 1 / F )∫ S 1 S 2 {itt M dμ°(M) – t X dμ°(X) + t N dμ°(N) – t Y dμ°(Y)} where t are the ionic transport numbers, a the electrolyte activities, and μ° the standard chemical Potentials. Linear variations in t, a and μ° at the interphase region were assumed. In a cell containing the above Junction, when the electrolyte concentrations, c 1 and c 2 , are varied, components a and b vary simultaneously. However, by making a proper correction for the actual values of component b, the emf variation corresponding to the actual variation in component a could be obtained. Thus, the above equation for component a was confirmed to be valid. The results also suggest that the previously reported method of estimation of component b is reasonable.

  • a new method of estimation of the Liquid Junction Potential between different solvents
    Analytical Sciences, 1991
    Co-Authors: Kosuke Izutsu, Toshio Nakamura, Mitsuo Muramatsu, Yutaka Aoki
    Abstract:

    Based on the experimental study of the three components of the Liquid Junction Potential (LJP) between different solvents, a new method was developed for the estimation of the LJP. In the method, each of the three components was estimated separately from the others, and then they were summed up. The results obtained by this method agreed well with the results obtained by the conventional method.

  • Liquid Junction Potential between different solvents: Component due to the differences in electrolyte concentrations and ionic mobilities
    Journal of Electroanalytical Chemistry and Interfacial Electrochemistry, 1991
    Co-Authors: Kosuke Izutsu, Toshio Nakamura, Mitsuo Muramatsu, Yutaka Aoki
    Abstract:

    Abstract Among the three components of the Liquid Junction Potential at a Junction between different solvents, the component due to the differences in electrolyte concentrations (or activities) on the two sides of the Junction and the differences between the cationic and anionic mobilities was investigated. An equation was derived for the component at a Junction with the same electrolyte (MX) on the two sides, where t represents the ionic transport numbers and a the electrolyte activity. Linear variations of t and a were assumed at the interphase region of the Junction. The equation was confirmed experimentally to be approximately valid in many cases and may be used in estimating the component. In some cases, apparent deviations from the equation were observed. The deviations were attributed to the influence of electrolyte concentration, which caused partial decreases in the component due to the solvent-solvent interactions at the Junction. Some theoretical and experimental studies were also carried out for a Junction with different electrolytes (MX and NY) on the two sides,

C. Kalidas - One of the best experts on this subject based on the ideXlab platform.

  • Gibbs Energies of Solvation and Solvent Transport of Some Silver(I) Salts in Water + N-Methyl-2-pyrrolidinone at 30 .degree.C
    Journal of Chemical & Engineering Data, 1995
    Co-Authors: T. K. Varadarajan, R. Parvathy, T. V. Ramakrishna, C. Kalidas
    Abstract:

    The preferential solvation of the silver salts silver(I) bromate, iodate, sulfate, and oxalate in the binary solvent mixtures of water and N-methyl-2-pyrrolidinone has been studied by solubility and solvent transport number measurements. The Gibbs transfer energies of the salts from water to water + N-methyl-2-pyrrolidinone mixtures, calculated from solubility data, were split into their ionic values by using the transfer energies of silver ion determined on the basis of the negligible Liquid Junction Potential method. These data have also been compared with those obtained on the basis of the tetraphenylarsonium tetraphenylborate method. Solvent transport numbers (Δ') of N-methyl-2-pyrrolidinone were determined for all the salts by employing a concentration cell with transference as suggested by Wagner. The results have been interpreted in terms of heteroselective solvation of all the salts, with silver ion being selectively solvated by N-methyl-2-pyrrolidinone and anions by water.

Juan Manuel Madariaga - One of the best experts on this subject based on the ideXlab platform.

  • Determination of ion exchange equilibrium constants of strongly acidic resins with alkaline-earth metals by means of the potentiometric titrations technique.
    Talanta, 1999
    Co-Authors: Gregorio Borge, Gorka Arana, Luis Fernández, Juan Manuel Madariaga
    Abstract:

    Abstract A recently developed methodology for the determination of ion exchange equilibrium constants has been applied to ion exchange systems of 1:2 stoichiometry. Potentiometric titrations with variable ionic strength were carried out. Ionic medium titrations were performed for the estimation of the Liquid Junction Potential. The modified Bromley's methodology and the Wilson model were used for the estimation of the activity coefficients of the species in the aqueous and resin phase, respectively. A modification of the Henderson equation is used for the estimation of Liquid Junction Potentials in the mixtures including 1:2 electrolytes. Equilibrium constants for the H + /M 2+ (M=Mg, Ca, Sr and Ba) exchange systems in the strongly acidic resins Dowex CM-15 and Dowex C650 were studied.

  • On the Liquid Junction Potential for the determination of equilibrium constants by means of the potentiometric technique without constant ionic strength
    Journal of Electroanalytical Chemistry, 1997
    Co-Authors: Gregorio Borge, Luis A. Fernāndez, Juan Manuel Madariaga
    Abstract:

    Abstract A modified method for the calculation of Liquid Junction Potentials based on the Henderson equation is proposed. The estimation of the activity coefficients and the conductivities is performed by means of the Modified Bromley Methodology [ G. Borge, R. Castano, M.P. Carril, M.S. Corbillon, J.M. Madariaga, Fluid Phase Equilibria 121 (1996) 85–98; G. Borge, N. Etxebarria, L.A. Fernandez, M.A. Olazabal, J.M. Madariaga, Fluid Phase Equilibria 121 (1996) 99–109. ] and the Extended Falkenhagen Equation [ A. De Diego, Conductivity of concentrated electrolytic solutions: study of the dependence with concentration and temperature, Ph.D. Thesis, University of the Basque Country, Bilbao, 1996. ]. The efficiency of the method has been tested in potentiometric titrations without constant ionic strength. Its applicability to potentiometric titrations with constant ionic strength is also discussed.