Investigation of liquid-liquid equilibrium of the ternary system (water+1,6-diaminohexane+2-methyl-1-propanol or 3-methyl-1-butanol) at different temperatures
Chemical Engineering Thermodynamics|Updated:2026-01-06
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Investigation of liquid-liquid equilibrium of the ternary system (water+1,6-diaminohexane+2-methyl-1-propanol or 3-methyl-1-butanol) at different temperatures
Chinese Journal of Chemical EngineeringVol. 28, Issue 1, Pages: 191-197(2020)
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School of Chemical Engineering and Energy, Zhengzhou University,Zhengzhou,China,450001
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Published:2020
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Yonghui Dou, Huanxin Li, Xiaoqiang Gao, Guoji Liu, Li Xu. Investigation of liquid-liquid equilibrium of the ternary system (water+1,6-diaminohexane+2-methyl-1-propanol or 3-methyl-1-butanol) at different temperatures[J]. Chinese Journal of Chemical Engineering, 2020, 28(1): 191-197.
DOI:
Yonghui Dou, Huanxin Li, Xiaoqiang Gao, Guoji Liu, Li Xu. Investigation of liquid-liquid equilibrium of the ternary system (water+1,6-diaminohexane+2-methyl-1-propanol or 3-methyl-1-butanol) at different temperatures[J]. Chinese Journal of Chemical Engineering, 2020, 28(1): 191-197.DOI:
Investigation of liquid-liquid equilibrium of the ternary system (water+1,6-diaminohexane+2-methyl-1-propanol or 3-methyl-1-butanol) at different temperatures
6-diaminohexane+3-methyl-1-butanol) were measured at 293.15
303.15 and 313.15 K under atmospheric pressure. Reliability of the experimental tie-line data was checked by empirical Hand
Othmer-Tobias and Bachman equations. Distribution coefficient (
D
) and selectivity (
S
) were calculated in order to investigate capability of the studied organic solvents for 1
6-diaminohexane extraction. The high values of separation factors demonstrated that 2-methyl-1-propanol and 3-methyl-1-butanol were applicable for this purpose. The experimental data were correlated by nonrandom two-liquid (NRTL) and universal quasi-chemical (UNIQUAC) models. The percent-root-mean-square deviation (RMSD) values for NRTL and UNIQUAC models were less than 0.15
which indicated that the experimental data have been sufficiently correlated.
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Measurement and Correlation of Vapor-Liquid Equilibrium for Binary System 1,2-Epoxycyclohexane+1,2-Dichloroethane
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