1977
DOI: 10.1021/j100519a009
|View full text |Cite
|
Sign up to set email alerts
|

Internal pressures and solubility parameters for carbon disulfide, benzene, and cyclohexane

Abstract: Densities of carbon disulfide, benzene, and cyclohexane were measured in the region 23-65 °C at pressures to 1 kbar. The data were used to calculate internal pressures and these were compared with solubility parameters obtained from liquid molar volumes at saturation and isothermal energies of vaporization to the ideal-gas state. Along the saturation line, the square root of the internal pressure is somewhat larger than the solubility parameter (square root of cohesive energy density). For benzene and cyclohex… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1

Citation Types

0
8
0

Year Published

1983
1983
2015
2015

Publication Types

Select...
9

Relationship

0
9

Authors

Journals

citations
Cited by 28 publications
(8 citation statements)
references
References 4 publications
0
8
0
Order By: Relevance
“…(3) should equal to be unity for nonpolar and nonassociating materials, as well as for polar materials where the dipole moment was less than 2 D; in addition, Jack et al [52,53] strongly suggested that the value of m for CO 2 should be near unity. Therefore, the internal pressure and cohesive energy density of CO 2 in Eq.…”
Section: Solubility Parameter Of Sccomentioning
confidence: 99%
“…(3) should equal to be unity for nonpolar and nonassociating materials, as well as for polar materials where the dipole moment was less than 2 D; in addition, Jack et al [52,53] strongly suggested that the value of m for CO 2 should be near unity. Therefore, the internal pressure and cohesive energy density of CO 2 in Eq.…”
Section: Solubility Parameter Of Sccomentioning
confidence: 99%
“…The Tait equation has been used extensively in recent years to represent volume-pressure isotherms on poly-mers1" 13 and low molecular weight liquids. 14,15 In its integrated form, it is usually quoted as 1 -V/V0 = C'ln (1 + P/b) (1) where V is the specific volume in cm3/g at pressure P, and V0 is the corresponding volume at the reference pressure P = 0 bar. (Some authors use a reference pressure of P0 = 1 bar,14 but more generally, it is given as P0 = 0 bar, even in cases where the tabulated data begin at P = 1 bar.9) C is taken as a universal constant, having a value of 0.0894, as defined by Simha et al5"10 The parameter b is a constant along any isotherm for which there is no pressureinduced transition.…”
Section: Introductionmentioning
confidence: 99%
“…[22][23][24][25][26][27][28] Using the reported ultrasonic speed, u, and density, ρ, data of liquid mixtures internal pressure have been calculated experimentally using Eqn (1). Internal pressure using Flory's statistical theory has been computed by putting the required parameters of pure components (Table 1) and reported mole fractions of the liquid mixtures in Eqn (6).…”
Section: Resultsmentioning
confidence: 99%
“…Its importance in the study of the thermodynamic properties of liquid mixtures was recognised by Hilderbrand. 1 Also, significant contributions were made by Barton, 2 Bagley et al, 3 Rosseinsky, 4 Berkowitz et al, 5 Renuncio et al, 6 and Suryanarayana, 7 who have stressed that internal pressure is a fundamental property of the liquid state and correlated it with other thermodynamic parameters. Attempts have been made by some investigators 4,8,9 to calculate theoretically the internal pressure of liquids and their mixtures.…”
mentioning
confidence: 99%