Modeling of interfacial tension in binary mixtures of CH4, CO2, and N2- alkanes using gene expression programming and equation of state

被引:29
作者
Mirzaie, Mohsen [1 ]
Tatar, Afshin [2 ]
机构
[1] Islamic Azad Univ, South Tehran Branch, Tehran, Iran
[2] Islamic Azad Univ, North Tehran Branch, Young Researchers & Elite Club, Tehran, Iran
关键词
Interfacial tension; Alkalies; EOR; Genetic expression programming (GEP); Equation of state (EoS); EQUILIBRIUM PHASE COMPOSITIONS; MINIMUM MISCIBILITY PRESSURE; PLUS N-ALKANE; SURFACE-TENSION; CARBON-DIOXIDE; CORRESPONDING-STATES; GRADIENT THEORY; THERMODYNAMIC ANALYSIS; ELEVATED PRESSURES; OIL-RECOVERY;
D O I
10.1016/j.molliq.2020.114454
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Interfacial tension (IFT) plays a key role in enhanced oil recovery (EOR) processes that involve the injection of light hydrocarbon and non-hydrocarbon gases into oil reservoirs. Crude oil is a complex mixture of different hydrocarbons, its phase behavior is unknown in presence of miscible gas under reservoir conditions: therefore, most of the LIT measurement experiments are done using a certain fluid, such as n-alkanes. CO2 is a common gas used for EOR purposes. Since N-2 and CH4 impurities in the injected CO2 stream substantially influence the IFTs and the MMP of the system, several experimental studies conducted on (N-2 + n-alkanc) and (CH4 n-alkane) systems over a wide range of temperature and pressure to provide a comprehensive III database. Accurate prediction of this property under the thermodynamic conditions encountered in petroleum reservoirs is of paramount importance for achieving the highest amount of oil recovery. In this study, two different models are developed for prediction of IFT in binary mixtures containing (CO2 + n-alkane), (N-2 + n-alkane), and (CH4 + nalkane). These models include the thermodynamic-based model of Weinaug and Katz 1943 [1] combined with PR-EoS, and the mathematical-based model of Gene Expression Programming (GEP). A preprocessing based on Z score method is applied on the assembled dataset to remove the outliers and duplicates from the data. The GEP and EoS models were able to predict accurate IFT results in all three systems with the EOS providing slightly inferior results in systems containing N-2 gas. For some experimental observations the EoS model failed to provide any IFT results. In addition, to have a better understanding of the performance of the developed models, they were compared for IFT values less and greater than or equal to 1 mNim for all the systems. The average squared coefficient of determination (R-2) for the GEP model in CH4, CO2, and N-2 - alkanes systems were 0.92, 0.94, and 0.91, and for EoS model were 0.94,0.87, and 0.66, respectively. The findings of this study can help fora better understanding of interfacial tension under the thermodynamic conditions encountered in petroleum reservoirs is of paramount importance for achieving the highest amount of oil recovery. (C) 2020 Elsevier B.V. All rights reserved.
引用
收藏
页数:15
相关论文
共 88 条
[11]   High-pressure densities and interfacial tensions of binary systems containing carbon dioxide plus n-alkanes: (n-Dodecane, n-tridecane, n-tettadecane) [J].
Cumicheo, Constanza ;
Cartes, Marcela ;
Segura, Hugo ;
Mueller, Erich A. ;
Mejia, Andres .
FLUID PHASE EQUILIBRIA, 2014, 380 :82-92
[12]   INTERFACIAL TENSION IN HYDROCARBON SYSTEMS [J].
DEAM, JR ;
MADDOX, RN .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1970, 15 (02) :216-&
[13]  
Dechoz J, 2004, APPL SURF SCI, V229, P175, DOI [10.1016/j.apsusc.2004.01.057, 10.1016/j.apsuse.2004.01.057]
[14]   A comparison of CO2 minimum miscibility pressure determinations for Weyburn crude oil [J].
Dong, MZ ;
Huang, S ;
Dyer, SB ;
Mourits, FM .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2001, 31 (01) :13-22
[15]  
Ferreira C., 2001, Complex Systems, V13, P87
[16]   EQUILIBRIUM PHASE COMPOSITIONS, PHASE DENSITIES, AND INTERFACIAL-TENSIONS FOR CO2 + HYDROCARBON SYSTEMS .5. CO2 + N-TETRADECANE [J].
GASEM, KAM ;
DICKSON, KB ;
DULCAMARA, PB ;
NAGARAJAN, N ;
ROBINSON, RL .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1989, 34 (02) :191-195
[17]   Interfacial tension measurements and modelling of (carbon dioxide plus n-alkane) and (carbon dioxide plus water) binary mixtures at elevated pressures and temperatures [J].
Georgiadis, Apostolos ;
Llovell, Felix ;
Bismarck, Alexander ;
Blas, Felipe J. ;
Galindo, Amparo ;
Maitland, Geoffrey C. ;
Trusler, J. P. Martin ;
Jackson, George .
JOURNAL OF SUPERCRITICAL FLUIDS, 2010, 55 (02) :743-754
[18]  
Grigg R.B., 1997, SPE ANN TECHN C EXH, P7
[19]   THE PRINCIPLE OF CORRESPONDING STATES [J].
GUGGENHEIM, EA .
JOURNAL OF CHEMICAL PHYSICS, 1945, 13 (07) :253-261
[20]   Modeling interfacial tension and minimum miscibility pressure in paraffin-nitrogen systems: Application to gas injection processes [J].
Hemmati-Sarapardeh, Abdolhossein ;
Mohagheghian, Erfan .
FUEL, 2017, 205 :80-89