New models for the binary interaction parameters of nitrogen-alkanes mixtures based on the cubic equations of state

被引:3
作者
Haghbakhsh, Reza [1 ]
Parvaneh, Khalil [1 ]
Esmaeilzadeh, Feridun [1 ,2 ]
机构
[1] Shiraz Univ, Oil & Gas Thermodynam Res Lab, Sch Chem & Petr Engn, Shiraz, Iran
[2] Shiraz Univ, Adv Res Grp Gas Condensate Recovery, Enhanced Oil & Gas Recovery Inst, Dept Chem & Petr Engn,Sch Chem & Petr Engn, Shiraz 7134851154, Iran
关键词
Binary interaction parameters; ER EoS; Halgren HHG model; high-pressure vapor-liquid equilibria; Lorentz-Berthelot model; PR EoS; VAPOR-LIQUID-EQUILIBRIA; PENG-ROBINSON EQUATION; MIXING RULES; OF-STATE; PHASE-EQUILIBRIA; CARBON-DIOXIDE; INTERACTION COEFFICIENTS; HYDROCARBON SYSTEMS; PREDICTIVE; 1978; ALPHA-FUNCTION;
D O I
10.1080/00986445.2017.1423475
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, the goal was to derive a new purely predictive model to obtain binary interaction parameters based on intermolecular theories. The Lorentz-Berthelot and Halgren HHG molecular combining rules were coupled with the vdw1 mixing rule to derive the new equations for binary interaction parameters. These equations were used with the PR and ER EoSs to calculate the vapor-liquid equilibria of 14 binary mixtures of nitrogen with either methane, ethane, propane, iso-butane, n-butane, iso-pentane, n-pentane, n-hexane, n-heptane, n-octane, n-nonae, n-decane, n-dodecane, or n-tetradecane over wide ranges of temperature and pressure. To increase the accuracy for all of the investigated systems, we have additionally suggested a new correlative mode for the proposed equations. For some of the systems, the proposed predictive equations enhance the accuracy of vapor-liquid equilibria predictions up to three times in comparison to the case where binary interaction parameters are set to zero.
引用
收藏
页码:914 / 928
页数:15
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