Isobaric low-pressure vapor-liquid equilibrium data of the system monochloroacetic acid + dichloroacetic acid + diethylene glycol dipentyl ether and the constituent binary systems

M.T.G. Jongmans; A. Londono; B. Schuur; A.B. Haan, de

doi:10.1016/j.fluid.2012.07.027

Isobaric low-pressure vapor-liquid equilibrium data of the system monochloroacetic acid + dichloroacetic acid + diethylene glycol dipentyl ether and the constituent binary systems

M.T.G. Jongmans, A. Londono, B. Schuur, A.B. Haan, de

Proces Systems Engineering

Research output: Contribution to journal › Article › Academic › peer-review

3 Citations (Scopus)

1 Downloads (Pure)

Abstract

In this study, binary and ternary VLE data have been determined at 5, 7.5, and 10 kPa for the system monochloracetic acid (MCA) + dichloroacetic acid (DCA) + diethylene glycol dipentyl ether (DGDP). The extractant DGDP enhances the relative volatility of the MCA/DCA system from 1.2 without extractant up to 4. The non-ideal behavior in the liquid and vapor phase was reasonably well correlated with the NRTL and Hayden–O’Connell (HOC) model, respectively. The binary and ternary VLE data were correlated separately to obtain a better description of both datasets

Original language	English
Pages (from-to)	15-21
Number of pages	7
Journal	Fluid Phase Equilibria
Volume	334
DOIs	https://doi.org/10.1016/j.fluid.2012.07.027
Publication status	Published - 2012

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title = "Isobaric low-pressure vapor-liquid equilibrium data of the system monochloroacetic acid + dichloroacetic acid + diethylene glycol dipentyl ether and the constituent binary systems",

abstract = "In this study, binary and ternary VLE data have been determined at 5, 7.5, and 10 kPa for the system monochloracetic acid (MCA) + dichloroacetic acid (DCA) + diethylene glycol dipentyl ether (DGDP). The extractant DGDP enhances the relative volatility of the MCA/DCA system from 1.2 without extractant up to 4. The non-ideal behavior in the liquid and vapor phase was reasonably well correlated with the NRTL and Hayden–O{\textquoteright}Connell (HOC) model, respectively. The binary and ternary VLE data were correlated separately to obtain a better description of both datasets",

author = "M.T.G. Jongmans and A. Londono and B. Schuur and {Haan, de}, A.B.",

year = "2012",

doi = "10.1016/j.fluid.2012.07.027",

language = "English",

volume = "334",

pages = "15--21",

journal = "Fluid Phase Equilibria",

issn = "0378-3812",

publisher = "Elsevier",

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Isobaric low-pressure vapor-liquid equilibrium data of the system monochloroacetic acid + dichloroacetic acid + diethylene glycol dipentyl ether and the constituent binary systems. / Jongmans, M.T.G.; Londono, A.; Schuur, B.; Haan, de, A.B.

In: Fluid Phase Equilibria, Vol. 334, 2012, p. 15-21.

Research output: Contribution to journal › Article › Academic › peer-review

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T1 - Isobaric low-pressure vapor-liquid equilibrium data of the system monochloroacetic acid + dichloroacetic acid + diethylene glycol dipentyl ether and the constituent binary systems

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AU - Schuur, B.

AU - Haan, de, A.B.

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AB - In this study, binary and ternary VLE data have been determined at 5, 7.5, and 10 kPa for the system monochloracetic acid (MCA) + dichloroacetic acid (DCA) + diethylene glycol dipentyl ether (DGDP). The extractant DGDP enhances the relative volatility of the MCA/DCA system from 1.2 without extractant up to 4. The non-ideal behavior in the liquid and vapor phase was reasonably well correlated with the NRTL and Hayden–O’Connell (HOC) model, respectively. The binary and ternary VLE data were correlated separately to obtain a better description of both datasets

U2 - 10.1016/j.fluid.2012.07.027

DO - 10.1016/j.fluid.2012.07.027

M3 - Article

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EP - 21

JO - Fluid Phase Equilibria

JF - Fluid Phase Equilibria

SN - 0378-3812

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