2010
DOI: 10.1016/j.fuel.2010.04.017
|View full text |Cite
|
Sign up to set email alerts
|

Application of Chebyshev polynomials to predict phase behavior of fluids containing asphaltene and associating components using SAFT equation of state

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
8
0

Year Published

2014
2014
2018
2018

Publication Types

Select...
5

Relationship

1
4

Authors

Journals

citations
Cited by 13 publications
(8 citation statements)
references
References 19 publications
0
8
0
Order By: Relevance
“…Statistical associating fluid theory (SAFT) is a more advanced EoS which is used in some modelling studies of asphaltene precipitation. [25][26][27] One of the disadvantages of the EoS based models is their need for fluid characterization generally up to C 30þ . Furthermore, these models sometimes encounter convergence problems particularly when the polydispersity of the asphaltene particles is considered.…”
Section: Eos Based Modelsmentioning
confidence: 99%
See 1 more Smart Citation
“…Statistical associating fluid theory (SAFT) is a more advanced EoS which is used in some modelling studies of asphaltene precipitation. [25][26][27] One of the disadvantages of the EoS based models is their need for fluid characterization generally up to C 30þ . Furthermore, these models sometimes encounter convergence problems particularly when the polydispersity of the asphaltene particles is considered.…”
Section: Eos Based Modelsmentioning
confidence: 99%
“…Li and Firoozabadi applied cubic‐plus‐association (CPA) EoS to study asphaltene precipitation from normal alkane diluted model solution and heavy oil and bitumen. Statistical associating fluid theory (SAFT) is a more advanced EoS which is used in some modelling studies of asphaltene precipitation . One of the disadvantages of the EoS based models is their need for fluid characterization generally up to C 30+ .…”
Section: Introductionmentioning
confidence: 99%
“…The bubble curve data is seen to fall on the boundary of a three-phase vapour-liquid-liquid equilibrium (VLLE) region, whereas the asphaltene-precipitation data is shown to be related to the liquid-liquid (LLE) boundary of the diagram. The PC-SAFT equation of state has also shown to be successful to model the phase behaviour of asphaltene mixtures, as demonstrated by the numerous works of Chapman and coworkers [155,[198][199][200][201][202][203][204][205][206][207][208] and others [65,163,[214][215][216]. In most of these studies, the effects of size asymmetry and van der Waals interactions are assumed to dominate the phase behaviour, and association interactions are therefore not considered.…”
Section: Statistical Associating Fluid Theorymentioning
confidence: 99%
“…The algorithm starts by interpolating the logarithm of the objective function on Chebyshev polynomials (Burden et al, 1981;Tabatabaei-Nejad and Khodapanah, 2010a) in the specified interval to provide a closed form expression for the logarithm of the objective function. The Chebyshev polynomials are then converted to ordinary polynomials to obtain an approximation for the logarithm of the objective function as an ordinary polynomial.…”
Section: Dew Point Pressure(s) Calculation-using Chebyshev Polynomialsmentioning
confidence: 99%