2008
DOI: 10.1016/j.jct.2008.03.010
|View full text |Cite
|
Sign up to set email alerts
|

Solvation model for estimating the properties of (vapour+liquid) equilibrium

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1

Citation Types

0
2
0

Year Published

2010
2010
2017
2017

Publication Types

Select...
6

Relationship

1
5

Authors

Journals

citations
Cited by 12 publications
(2 citation statements)
references
References 37 publications
0
2
0
Order By: Relevance
“…At the same time the use of nine molecular descriptors of compounds very different in structure guarantees a large range of applicability of SERLAS‐i to more complex systems and allows for an improved calculative description of the real behaviour of various kinds of mixtures including a ionic liquid, with particular focus on phase behaviour of quaternary LLE systems . By combining Senol's VLE model SERAS (solvation energy relation for associated systems) with SERLAS‐i along with appropriately rearranging the limiting conditions, we will be able to simulate accurately the phase behaviour of complex VLE and VLLE systems . as well.…”
Section: Resultsmentioning
confidence: 99%
“…At the same time the use of nine molecular descriptors of compounds very different in structure guarantees a large range of applicability of SERLAS‐i to more complex systems and allows for an improved calculative description of the real behaviour of various kinds of mixtures including a ionic liquid, with particular focus on phase behaviour of quaternary LLE systems . By combining Senol's VLE model SERAS (solvation energy relation for associated systems) with SERLAS‐i along with appropriately rearranging the limiting conditions, we will be able to simulate accurately the phase behaviour of complex VLE and VLLE systems . as well.…”
Section: Resultsmentioning
confidence: 99%
“…Modeling of thermodynamic properties and phase equilibrium of a mixture involving associating components such as alcohols is still challenging because such systems show extremely non-ideal behaviour [1]. Strong attractive (chemical) interactions of pure associating fluids and their mixtures make their thermodynamic properties different from non-associating solutions [2].…”
Section: Introductionmentioning
confidence: 99%