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Ao Yang et al.
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Yichun Dong et al.
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Xinqiang You et al.
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Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
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Dongmei Xu et al.
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B. J. Zhang et al.
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INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH (2012)
(Liquid plus liquid) equilibrium data of (water plus phosphoric acid plus solvents) systems at T = (308.2 and 318.2) K
H. Ghanadzadeh Gilani et al.
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Alfonsina E. Andreatta et al.
FLUID PHASE EQUILIBRIA (2010)
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Qunsheng Li et al.
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Effect of pressure and the capability of 2-methoxyethanol as a solvent in the behaviour of a diisopropyl ether-isopropyl alcohol azeotropic mixture
Estela Lladosa et al.
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Correlation of vapor-liquid equilibrium data for acetic acid-isopropanol-water-isopropyl acetate mixtures
BA Mandagaran et al.
BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING (2006)
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WX Chang et al.
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A Arce et al.
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Experimental determination of the vapor-liquid equilibrium at 101.32 kPa of the ternary system 1-butanol plus methanol plus TAME
A Arce et al.
JOURNAL OF CHEMICAL AND ENGINEERING DATA (2000)