Total vapour pressure measurements made by a modified static method for the ternary mixture (N -methylacetamide + ethanol + water) and for the binary mixture (N -methylacetamide + ethanol) at the temperature 313.15 K are presented. Different expressions for the excess Gibbs free energy are tested, a
( Vapour  +  liquid ) equilibrium measurement and correlation of the refrigerant ( propane  +  1,1,1,3,3,3-hexafluoropropane) atT =  ( 283.13, 303.19, and 323.26) K
β Scribed by Sergio Bobbo; ; Roberto Camporese; ; Roman Stryjek
- Publisher
- Elsevier Science
- Year
- 2000
- Tongue
- English
- Weight
- 129 KB
- Volume
- 32
- Category
- Article
- ISSN
- 0021-9614
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β¦ Synopsis
Vapour + liquid) equilibrium (v.l.e.) data were measured for the refrigerant {propane (R290) + 1,1,1,3,3,3-hexafluoropropane (R236fa)} at T = (283. 13, 303.19, and 323.26) K, using forced recirculation of the vapour through the liquid by means of a magnetic pump. The composition of both phases was determined by gas chromatography.
Due to the presence of more than negligible amounts of impurities in the R290, two sets of data are presented and correlated: the first was determined disregarding the impurities in the composition measurement, assuming that the mixture was binary; the second set was obtained assuming that the mixture was quaternary, considering the two impurities detected {n-butane (R600) and isobutane (R600a)} as components of the mixtures. The results were correlated using the Carnahan-Starling-De Santis equation of state. The experimental findings show a strong positive deviation from Raoult's law and the presence of an azeotropic composition at high R290 concentrations. Applying the homomorph concept, the hydrogen-bonding energy in (dimethyl ether + R236fa) was estimated using previously published results and those presented here. The v.l.e. of the system are not reported elsewhere in the literature.
π SIMILAR VOLUMES
TABLE 1. Densities Ο for the pure liquids at T = 298.15 K Liquid Ο/(g β’ cm -3 ) expt lit 1-Cholorooctane 0.86875 0.86876 (4) 1-Butanol 0.80575 0.80576
TABLE 1. Densities Ο for the pure liquids at T = 298.15 K Ο/(gβ’cm -3 ) Liquid expt lit 1-Chlorobutane 0.88069 0.88079 (4) 1-Butanol 0.80575 0.80576 (5)
Isobaric (vapour + liquid) equilibrium (v.l.e.) of (1,3-dioxolane, or 1,4-dioxane + 1butanol, or 2-butanol) at 40.0 kPa and 101.3 kPa have been studied with a dynamic recirculating still. The experimental data for all mixtures were checked for thermodynamic consistency using the method of Van Ness.
Measurements of ( p, Ο, T ) for {x NH 3 + (1 -x)H 2 O} at x = (1.0000, 0.8374, 0.6005, and 0.2973) and at specified temperatures and pressures in the compressed liquid phase were carried out with a metal-bellows variable volumometer between T = 310 K and T = 400 K at pressures up to 17 MPa. The resu
Measurements of ( p, Ο, T ) for {xCH 3 OH + (1x)H 2 O} with x = (1.0000 and 0.4993) at specified temperatures and pressures in the compressed liquid phase were carried out with a metal-bellows variable volumometer along six isotherms between T = 320 K and T = 420 K at pressures from the bubble point