Volumetric and Viscometric Properties of Methanol, Ethanol, Propan-2-ol, and 2-Methylpropan-2-ol with a Synthetic C6+ Mixture from 298.15 K to 318.15 K
Abstract:Densities and viscosities were measured for the systems of methanol, ethanol, propan-2-ol, and
2-methylpropan-2-ol separately with a synthetic C6+ mixture at temperatures from 298.15 K to 318.15 K
and atmospheric pressure. The synthetic C6+ is a five-component hydrocarbon mixture. Densities were
determined using a vibrating-tube densimeter. Viscosities were measured with an automatic Ubbelohde
capillary viscometer. The estimated uncertainties are less than ±0.0004 g·cm-3 for density and ±0.8%
for viscosity. By… Show more
“…Table shows that our densities for these two pure substances agree with the literature values within an average value of ±0.24 kg·cm -3 . …”
Section: Resultsmentioning
confidence: 99%
“…Figure 2. Percentage deviations of experimental densities of methanol from the equation of state given by de Reuck and Craven: 14 b, this work; 9, Nikam et al; 35 2, Dizechi and Marshall; 1 1, Ortega; 36 [, Papanastasiou and Ziogas; 37 O, Garcia; 38 4, Tu et al; 39 0, Tu et al40 …”
We present experimental density measurements for the binary systems acetone + water, propionic acid + water, and acetone + propionic acid from 283.15 K to 323.15 K over the entire composition range. A vibrating tube densimeter produced the experimental densities. We have also calculated excess volumes and correlated them with a Redlich-Kister polynomial form.
“…Table shows that our densities for these two pure substances agree with the literature values within an average value of ±0.24 kg·cm -3 . …”
Section: Resultsmentioning
confidence: 99%
“…Figure 2. Percentage deviations of experimental densities of methanol from the equation of state given by de Reuck and Craven: 14 b, this work; 9, Nikam et al; 35 2, Dizechi and Marshall; 1 1, Ortega; 36 [, Papanastasiou and Ziogas; 37 O, Garcia; 38 4, Tu et al; 39 0, Tu et al40 …”
We present experimental density measurements for the binary systems acetone + water, propionic acid + water, and acetone + propionic acid from 283.15 K to 323.15 K over the entire composition range. A vibrating tube densimeter produced the experimental densities. We have also calculated excess volumes and correlated them with a Redlich-Kister polynomial form.
“…These oxygenated compounds are added to improve the octane rating and pollution-reducing capability of gasoline. This work has been carried out as a part of the project to investigate the thermophysical behavior of liquid mixtures of the oxygenated compounds included in a hydrocarbon mixture. − The main purpose of the present paper is to investigate the thermophysical properties for binary and ternary systems formed by two oxygenated compounds, such as ethanol and diisopropyl ether, and a hydrocarbon liquid, such as 2,2,4-trimethylpentane. The hydrocarbon liquid is the component that generally appears in gasoline.…”
Densities, viscosities, and refractive indices of the ternary system diisopropyl ether + ethanol + 2,2,4trimethylpentane at T ) 298.15 K and the binary systems diisopropyl ether + ethanol and diisopropyl ether + 2,2,4-trimethylpentane were measured at T ) (288.15, 298.15, and 308.15) K and atmospheric pressure over the whole composition range. Densities were determined using a vibrating-tube density meter. Viscosities were measured with an automatic Ubbelohde capillary viscometer, and refractive indices were measured using a digital Abbetype refractometer. Excess molar volumes (V E ), deviations in the viscosity from mole fraction average (∆η), and deviations in the refractive index from volume fraction average (∆n D ) for the mixtures were derived from experimental data. The binary and ternary data of V E , ∆η, and ∆n D were correlated with liquid composition by using the Redlich-Kister and the Cibulka equations.
“…Their densities were measured with a DMA 58 digital densimeter (Anton Paar) at 298.15 K, and the measured densities of the chemicals are compiled in Table 1 along with their recent published values. 5,[10][11][12][13] Apparatus and Procedure. Excess molar enthalpies were determined by a flow microcalorimeter at 298.15 K. Details of its experimental setup and operational procedures were described previously.…”
Section: Methodsmentioning
confidence: 99%
“…The purities of all the chemicals were estimated to be >99.7 mass %. Their densities were measured with a DMA 58 digital densimeter (Anton Paar) at 298.15 K, and the measured densities of the chemicals are compiled in Table along with their recent published values. ,− …”
Ternary excess molar enthalpies for the ethanol + 2-propanol + methyl tert-butyl ether (MTBE) and 1-propanol + 2-propanol + MTBE systems have been measured by a flow microcalorimeter at 298.15 K and ambient pressure. The pseudobinary excess molar enthalpies are positive over the whole range of composition. The ternary experimental results are correlated with a polynomial equation. The results have been compared with those calculated from a UNIQUAC associated-solution model taking into account the self-association of alcohols as well as the solvation between unlike alcohols and alcohols with MTBE using only binary parameters.
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