TY - JOUR
T1 - Activity coefficients of NaCl in PEG 4000 + water mixtures at 288.15, 298.15 and 308.15 K
AU - Morales, Jaime W.
AU - Galleguillos, Héctor R.
AU - Taboada, María E.
AU - Hernández-Luis, Felipe
N1 - Funding Information:
The authors thank CONICYT-Chile for the support provided through Fondecyt Project No. 1070909 and the ORI (International Relations Office) of the Universidad de La Laguna for its collaboration that made the stay of J.W.M. possible. We also thank the Vice-Rectory of Research and Technological Development of the Universidad de La Laguna for the support provided through its Support Fund for Maintaining Consolidated Research Groups (No. 1802440702).
PY - 2009/7/25
Y1 - 2009/7/25
N2 - The electromotive force of the cell containing two ion-selective electrodes (ISE),Na-ISE | NaCl (m), PEG 4000 (Y), H2 O (100 - Y) | Cl-ISE. has been measured at temperatures of 288.15, 298.15, and 308.15 K as a function of the weight percentage Y of PEG 4000 in a mixed solvent. Y was varied between 0 and 25% in five-unit steps and the molality of the electrolyte (m) was between ca. 0.003 and 5 mol kg-1. The values of the standard electromotive force were determined using routine methods of extrapolation, together with Debye-Hückel and Pitzer equations. The results obtained produced good internal consistency for all the temperatures studied. Once the standard electromotive force was determined, the mean ionic activity coefficients for NaCl, the Gibbs energy of transfer from the water to the PEG 4000-water mixture and the primary NaCl hydration number were calculated.
AB - The electromotive force of the cell containing two ion-selective electrodes (ISE),Na-ISE | NaCl (m), PEG 4000 (Y), H2 O (100 - Y) | Cl-ISE. has been measured at temperatures of 288.15, 298.15, and 308.15 K as a function of the weight percentage Y of PEG 4000 in a mixed solvent. Y was varied between 0 and 25% in five-unit steps and the molality of the electrolyte (m) was between ca. 0.003 and 5 mol kg-1. The values of the standard electromotive force were determined using routine methods of extrapolation, together with Debye-Hückel and Pitzer equations. The results obtained produced good internal consistency for all the temperatures studied. Once the standard electromotive force was determined, the mean ionic activity coefficients for NaCl, the Gibbs energy of transfer from the water to the PEG 4000-water mixture and the primary NaCl hydration number were calculated.
KW - Activity coefficient
KW - Emf
KW - Ion-selective electrode (ISE)
KW - NaCl
KW - PEG 4000
UR - http://www.scopus.com/inward/record.url?scp=67349280304&partnerID=8YFLogxK
U2 - 10.1016/j.fluid.2009.03.013
DO - 10.1016/j.fluid.2009.03.013
M3 - Article
AN - SCOPUS:67349280304
SN - 0378-3812
VL - 281
SP - 120
EP - 126
JO - Fluid Phase Equilibria
JF - Fluid Phase Equilibria
IS - 2
ER -