Developing a predictive group-contribution-based SAFT-VR equation of state

被引:102
作者
Peng, Yun [1 ]
Goff, Kimberly D. [1 ]
dos Ramos, M. Carolina [1 ]
McCabe, Clare [1 ]
机构
[1] Vanderbilt Univ, Dept Chem & Biomol Engn, Nashville, TN 37215 USA
基金
美国国家科学基金会;
关键词
Phase equilibria; Pure fluids; Mixtures; Group contribution; Heteronuclear; SAFT; GC-SAFT-VR; ASSOCIATING FLUID THEORY; VAPOR-LIQUID-EQUILIBRIA; DIRECTIONAL ATTRACTIVE FORCES; PRESSURE PHASE-EQUILIBRIA; PERTURBED-CHAIN SAFT; PLUS N-ALKANES; BINARY-MIXTURES; VARIABLE RANGE; CARBON-DIOXIDE; GC-SAFT;
D O I
10.1016/j.fluid.2008.11.008
中图分类号
O414.1 [热力学];
学科分类号
摘要
The hetero-segmented version of the statistical associating fluid theory for potentials of variable range (hetero-SAFT-VR) is used to develop a predictive molecular-based group-contribution SAFT-VR equation of state (GC-SAFT-VR), The hetero-SAFT-VR approach models molecules composed of segments of different size and/or energies of interaction enabling an accurate description of real molecules composed Of different functional groups. The differences in interactions between functional groups are maintained throughout the theory in contrast to other approaches in which the parameters for functional groups are averaged in order to model a molecule as a homonuclear chain With "group-averaged" parameters. Through the GC-SAFT-VR approach we can study the effect of molecular functionality and topology oil the thermodynamic properties of real fluid systems, since parameters are determined for each functional group and chain connectivity is explicitly specified. In this initial study GC-SAFT-VR parameters are developed for key organic functional groups (CH3, CH2, CH2=CH, C=O, C6H5, OCH3 and OCH2) by fitting to experimental vapor pressure and saturated liquid density data for a selected group of compounds that contain these functional groups. The transferability of the parameters obtained is tested by comparing theoretical predictions with experimental data for pure fluids not included in the fitting process and binary Mixtures. Using the GC-SAFT-VR approach good agreement is obtained between experimental data and the theoretical predictions for pure Substances, including isomers, and their Mixtures. The GC-SAFT-VR approach is able to accurately predict the effect of molecular functionality Oil mixture phase behavior without fitting to any experimental data for the system being studied. (c) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:131 / 144
页数:14
相关论文
共 104 条
[81]  
SMITH BD, 1986, THERMODYNAMIC DATA A
[82]  
Sponer J, 2001, BIOPOLYMERS, V61, P3, DOI 10.1002/1097-0282(2001)61:1<3::AID-BIP10048>3.0.CO
[83]  
2-4
[84]   Predicting the phase epuilibria of petroleum fluids with the SAFT-VR approach [J].
Sun, Lixin ;
Zhao, Honggang ;
McCabe, Clare .
AICHE JOURNAL, 2007, 53 (03) :720-731
[85]   Application of SAFT-VRX to binary phase behaviour: alkanes [J].
Sun, LX ;
Zhao, HG ;
Kiselev, SB ;
McCabe, C .
FLUID PHASE EQUILIBRIA, 2005, 228 :275-282
[86]   Predicting mixture phase equilibria and critical behavior using the SAFT-VRX approach [J].
Sun, LX ;
Zhao, HG ;
Kiselev, SB ;
McCabe, C .
JOURNAL OF PHYSICAL CHEMISTRY B, 2005, 109 (18) :9047-9058
[87]   Solubility of block copolymer surfactants in compressed CO2 using a lattice fluid hydrogen-bonding model [J].
Takishima, S ;
ONeill, ML ;
Johnston, KP .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (07) :2821-2833
[88]   Application to binary mixtures of a group contribution SAFT EOS (GC-SAFT) [J].
Tamouza, S ;
Passarello, JP ;
Tobaly, P ;
de Hemptinne, JC .
FLUID PHASE EQUILIBRIA, 2005, 228 :409-419
[89]   Group contribution method with SAFT EOS applied to vapor liquid equilibria of various hydrocarbon series [J].
Tamouza, S ;
Passarello, JP ;
Tobaly, P ;
de Hemptinne, JC .
FLUID PHASE EQUILIBRIA, 2004, 222 :67-76
[90]   Application of group contribution SAFT equation of state (GC-SAFT) to model phase behaviour of light and heavy esters [J].
Thi, TXN ;
Tamouza, S ;
Tobaly, P ;
Passarello, JP ;
de Hemptinne, JC .
FLUID PHASE EQUILIBRIA, 2005, 238 (02) :254-261