1996
DOI: 10.1021/je9600414
|View full text |Cite
|
Sign up to set email alerts
|

Vapor−Liquid Equilibrium of the Acetic Acid + Octane Binary System at 323.15 K and 343.15 K

Abstract: In this work P−T−x−y vapor liquid equilibrium data were obtained for the acetic acid + octane mixture at two temperatures, 323.15 and 343.15 K. This mixture is very nonideal due to the association of acetic acid, and the data could only be correlated with sufficient accuracy by using two recently proposed activity coefficient models that include association in both the liquid and vapor phases.

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
5

Citation Types

0
7
0

Year Published

2003
2003
2024
2024

Publication Types

Select...
6
1

Relationship

0
7

Authors

Journals

citations
Cited by 14 publications
(7 citation statements)
references
References 5 publications
(10 reference statements)
0
7
0
Order By: Relevance
“…The different panels correspond to different association schemes: PC-SAFT-1A (a), PC-SAFT-2B (b), and PC-SAFT-DBD (c). The points are the experimental data of Plesnar et al The prediction of an azeotropic behavior is expected for this mixture, even with k ij = 0, as the experimental vapor pressures of the pure components are rather close. All the three models predict positive azeotropes (dashed lines), but none of them is able to quantitatively predict either the maximal pressure or the composition with k ij = 0.…”
Section: Resultsmentioning
confidence: 79%
See 1 more Smart Citation
“…The different panels correspond to different association schemes: PC-SAFT-1A (a), PC-SAFT-2B (b), and PC-SAFT-DBD (c). The points are the experimental data of Plesnar et al The prediction of an azeotropic behavior is expected for this mixture, even with k ij = 0, as the experimental vapor pressures of the pure components are rather close. All the three models predict positive azeotropes (dashed lines), but none of them is able to quantitatively predict either the maximal pressure or the composition with k ij = 0.…”
Section: Resultsmentioning
confidence: 79%
“…The pure component parameters for carboxylic acids are reported in Tables 1−3. The parameters for the n-alkanes (hexane, heptane and octane) are taken from Table 2 of 42 The prediction of an azeotropic behavior is expected for this mixture, even with k ij = 0, as the experimental vapor pressures of the pure components are rather close. All the three models predict positive azeotropes (dashed lines), but none of them is able to quantitatively predict either the maximal pressure or the composition with k ij = 0.…”
Section: Resultsmentioning
confidence: 99%
“…In our data collection, an electronic database, i.e., EVLM92 has been referenced, which contains the citation of the experimental data from the year of 1888 until 2004. The Korean database93 and DECHEMA94 series as well as literature data70, 76, 95–139 were referenced.…”
Section: Resultsmentioning
confidence: 99%
“…In our data collection, an electronic database, i.e., EVLM92 has been referenced, which contains the citation of the experimental data from the year of 1888 until 2004. The Korean database93 and DECHEMA94 series as well as literature data70, 76, 95–139 were referenced.…”
Section: Resultsmentioning
confidence: 99%