Correlation and prediction of liquid-liquid equilibria for alcohol/hydrocarbon mixtures using PC-SAFT equation of state at high pressure up to 150 MPa

被引:18
作者
Dong NguyenHuynh [1 ]
机构
[1] PetroVietNam Manpower Training Coll, Petr Fac, 43,Rd 30-4,Ward 9, Vung Tau City, Vietnam
关键词
PC-SAFT; LLE; Alkanes; Methanol; Ethanol; Prediction modeling; High pressure; PERTURBED-CHAIN SAFT; MODELING PHASE-EQUILIBRIA; ASSOCIATING FLUID THEORY; VAPOR-LIQUID; BINARY-SYSTEMS; POLAR SYSTEMS; N-ALKANES; GC-SAFT; HYDROCARBON SYSTEMS; METHANOL;
D O I
10.1016/j.fluid.2016.06.002
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this paper, we present a systematic study of the ability of the PC-SAFT equation of state to predict of liquid-liquid equilibria (LLE) for alcohol/hydrocarbon mixtures at high pressure on the basis of LLE data at 0.1 MPa. The adjustable temperature-independent binary interaction parameters, k(ij), in the PC-SAFT model were determined from LLE data at 0.1 MPa. The new proposed parameters set for methanol and ethanol with the two-site association scheme reproduce vapor pressures and liquid density with the same accuracy of PC-SAFT original parameters but show a better representation of the LLE data. In addition to using pure component PC-SAFT parameters derived from the standard method of fitting to liquid density and saturated vapor pressure, the new PC-SAFT parameters set for methanol and ethanol are determined from experimental association energy. The new association energy parameter of methanol and ethanol shows better agreement with the experimental results at approximately 298 K compared to all previously published PC-SAFT parameters. Different binary methanol + hydrocarbon and ethanol + hydrocarbon systems at high pressure up to 150 Mpa were tested using the PC-SAFT. LLE calculations and prediction show good agreement with experimental data for almost considered systems. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:206 / 214
页数:9
相关论文
共 51 条
[21]  
HRADETZKY G., 1986, Int. DATA Ser., Sel. Data Mixtures, P216
[22]   Phase equilibrium properties of ethane plus methanol system at 298.15 K [J].
Ishihara, K ;
Tanaka, H ;
Kato, M .
FLUID PHASE EQUILIBRIA, 1998, 144 (1-2) :131-136
[23]   Evaluation of the truncated perturbed chain-polar statistical associating fluid theory for complex mixture fluid phase equilibria [J].
Karakatsani, Eirini K. ;
Kontogeorgis, Georgios M. ;
Economou, Ioannis G. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (17) :6063-6074
[24]   Modeling of polar systems using PCP-SAFT: An approach to account for induced-association interactions [J].
Kleiner, Matthias ;
Sadowski, Gabriele .
JOURNAL OF PHYSICAL CHEMISTRY C, 2007, 111 (43) :15544-15553
[25]   Liquid-Liquid Equilibrium of Associating Fluid Mixtures Using Perturbed-Hard-Sphere-Chain Equation of State Combined with the Association Model [J].
Lee, Bong-Seop ;
Kim, Ki-Chang .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2015, 54 (01) :540-549
[26]   Modeling Water Containing Systems with the Simplified PC-SAFT and CPA Equations of State [J].
Liang, Xiaodong ;
Tsivintzelis, Ioannis ;
Kontogeorgis, Georgios M. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (37) :14493-14507
[27]   Prediction of the vapor-liquid equilibria and speed of sound in binary systems of 1-alkanols and n-alkanes with the simplified PC-SAFT equation of state [J].
Liang, Xiaodong ;
Thomsen, Kaj ;
Yan, Wei ;
Kontogeorgis, Georgios M. .
FLUID PHASE EQUILIBRIA, 2013, 360 :222-232
[28]   Prediction of liquid-liquid equilibria at high pressure for binary systems using EOS-GE models:: methanol plus hydrocarbon systems [J].
Matsuda, H ;
Kurihara, K ;
Ochi, K ;
Kojima, K .
FLUID PHASE EQUILIBRIA, 2002, 203 (1-2) :269-284
[29]   Liquid-liquid equilibrium data for binary alcohol plus n-alkane (C10-C16) systems:: methanol plus decane, ethanol plus tetradecane, and ethanol plus hexadecane [J].
Matsuda, H ;
Ochi, K .
FLUID PHASE EQUILIBRIA, 2004, 224 (01) :31-37
[30]   Modelling LLE and VLE of methanol plus n-alkane series using GC-PC-SAFT with a group contribution kij [J].
Mourah, M. ;
NguyenHuynh, D. ;
Passarello, J. P. ;
de Hemptinne, J. C. ;
Tobaly, P. .
FLUID PHASE EQUILIBRIA, 2010, 298 (01) :154-168