1981
DOI: 10.1021/je00025a008
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Viscosities of aqueous hydrochloric acid solutions, and densities and viscosities of aqueous hydroiodic acid solutions

Abstract: The three-phase liquld-liquld-vapor loci of four binary C02-n-paraffin systems (n-dodecane, n-trktecane, n-tetradecane, n-pentadecane) are studied, and temperature, pressure, and molar volumes and compositions of both liquid phases are reported. It Is within this group of n-parafflns that the nature of the upper critical end point for the C02-contalnlng binary systems changes from a UCST (L-L-V) to a K point (L-L-V) with Increasing carbon number. These four loci are compared with earlier obtained loci on C02-n… Show more

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Cited by 63 publications
(29 citation statements)
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“…This occurrence agrees with the trend presented in the literature [10]. On the other hand, the increase in the pH level from pH 4 -8 of a liquid increases the interfacial tension from 2.98 mN/m to 103 mN/m.…”
Section: Effect Of Ph In External Phasesupporting
confidence: 92%
“…This occurrence agrees with the trend presented in the literature [10]. On the other hand, the increase in the pH level from pH 4 -8 of a liquid increases the interfacial tension from 2.98 mN/m to 103 mN/m.…”
Section: Effect Of Ph In External Phasesupporting
confidence: 92%
“…Water is used as the working fluid in all simulations to represent the aqueous Bromine solution that passes through one side of an H 2 /Br 2 flow battery. Actual electrolyte fluids may have higher viscosities [31,32,33,34], which would further increase the pressure drops presented in this analysis.…”
Section: Simulated Casesmentioning
confidence: 99%
“…Furthermore, in many flow battery chemistries the viscosity of the electrolyte can be larger than the viscosity of water used in this model [31,32,33,34]. Higher viscosities will further drive pressure losses, and of the large cross channels that transport reactants to and from individual flow channels, is therefore a realistic option for reducing pressure drops in industrially sized, high power designs.…”
Section: Pressure Lossesmentioning
confidence: 99%
“…These solvents were selected, among the most common extractants in DLLME, to face most of the main problems arising from DLLME-ICP-AES coupling (e.g. solvent viscosity and volatility) (see Table 1) [21][22][23].…”
Section: Solutionsmentioning
confidence: 99%