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    Rights statement: This document is the Accepted Manuscript version of a Published Work that appeared in final form in Journal of Chemical and Engineering Data, copyright ©2016 American Chemical Society after peer review and technical editing by the publisher. To access the final edited and published work see http://pubs.acs.org/doi/abs/10.1021/acs.jced.6b00595

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Experimental Determination and Modeling of the Phase Behavior of the CO2 + Propionic Anhydride Binary System at High Pressure

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Experimental Determination and Modeling of the Phase Behavior of the CO2 + Propionic Anhydride Binary System at High Pressure. / Rebocho, Sílvia ; V. M. Nunes, Ana; Najdanovic, Vesna; Barreiros, Susana; Paiva, Alexandre.

In: Journal of Chemical and Engineering Data, Vol. 62, No. 1, 12.01.2017.

Research output: Contribution to Journal/MagazineJournal articlepeer-review

Harvard

Rebocho, S, V. M. Nunes, A, Najdanovic, V, Barreiros, S & Paiva, A 2017, 'Experimental Determination and Modeling of the Phase Behavior of the CO2 + Propionic Anhydride Binary System at High Pressure', Journal of Chemical and Engineering Data, vol. 62, no. 1. https://doi.org/10.1021/acs.jced.6b00595

APA

Vancouver

Author

Rebocho, Sílvia ; V. M. Nunes, Ana ; Najdanovic, Vesna ; Barreiros, Susana ; Paiva, Alexandre. / Experimental Determination and Modeling of the Phase Behavior of the CO2 + Propionic Anhydride Binary System at High Pressure. In: Journal of Chemical and Engineering Data. 2017 ; Vol. 62, No. 1.

Bibtex

@article{4d48dbcddc8b450485bbd0b6fff2a81d,
title = "Experimental Determination and Modeling of the Phase Behavior of the CO2 + Propionic Anhydride Binary System at High Pressure",
abstract = "The phase equilibrium of the binary system (CO2 + propionic anhydride) was determined experimentally at temperatures of 308, 313, and 323 K and pressures up to 10 MPa. Measurements were carried out in a high-pressure visual cell with variable volume. The experimental data were modeled using the Peng–Robinson equation of state and the Mathias–Klotz–Prausnitz mixing rule. A good correlation was achieved with this model, with a total average absolute deviation of 0.21%.",
author = "S{\'i}lvia Rebocho and {V. M. Nunes}, Ana and Vesna Najdanovic and Susana Barreiros and Alexandre Paiva",
note = "This document is the Accepted Manuscript version of a Published Work that appeared in final form in Journal of Chemical and Engineering Data, copyright {\textcopyright}2016 American Chemical Society after peer review and technical editing by the publisher. To access the final edited and published work see http://pubs.acs.org/doi/abs/10.1021/acs.jced.6b00595",
year = "2017",
month = jan,
day = "12",
doi = "10.1021/acs.jced.6b00595",
language = "English",
volume = "62",
journal = "Journal of Chemical and Engineering Data",
issn = "0021-9568",
publisher = "American Chemical Society",
number = "1",

}

RIS

TY - JOUR

T1 - Experimental Determination and Modeling of the Phase Behavior of the CO2 + Propionic Anhydride Binary System at High Pressure

AU - Rebocho, Sílvia

AU - V. M. Nunes, Ana

AU - Najdanovic, Vesna

AU - Barreiros, Susana

AU - Paiva, Alexandre

N1 - This document is the Accepted Manuscript version of a Published Work that appeared in final form in Journal of Chemical and Engineering Data, copyright ©2016 American Chemical Society after peer review and technical editing by the publisher. To access the final edited and published work see http://pubs.acs.org/doi/abs/10.1021/acs.jced.6b00595

PY - 2017/1/12

Y1 - 2017/1/12

N2 - The phase equilibrium of the binary system (CO2 + propionic anhydride) was determined experimentally at temperatures of 308, 313, and 323 K and pressures up to 10 MPa. Measurements were carried out in a high-pressure visual cell with variable volume. The experimental data were modeled using the Peng–Robinson equation of state and the Mathias–Klotz–Prausnitz mixing rule. A good correlation was achieved with this model, with a total average absolute deviation of 0.21%.

AB - The phase equilibrium of the binary system (CO2 + propionic anhydride) was determined experimentally at temperatures of 308, 313, and 323 K and pressures up to 10 MPa. Measurements were carried out in a high-pressure visual cell with variable volume. The experimental data were modeled using the Peng–Robinson equation of state and the Mathias–Klotz–Prausnitz mixing rule. A good correlation was achieved with this model, with a total average absolute deviation of 0.21%.

U2 - 10.1021/acs.jced.6b00595

DO - 10.1021/acs.jced.6b00595

M3 - Journal article

VL - 62

JO - Journal of Chemical and Engineering Data

JF - Journal of Chemical and Engineering Data

SN - 0021-9568

IS - 1

ER -