Vapor-liquid equilibrium (VLE) data and thermodynamic modeling for binary systems containing perfluorobutane (R610) with carbon monoxide or nitric oxide at (293, 313, and 333) K

Mulamba M. Tshibangu; Alain Valtz; Caleb Narasigadu; Christophe Coquelet; Deresh Ramjugernath

doi:10.1021/je400822m

Vapor-liquid equilibrium (VLE) data and thermodynamic modeling for binary systems containing perfluorobutane (R610) with carbon monoxide or nitric oxide at (293, 313, and 333) K

Mulamba M. Tshibangu
, Alain Valtz
, Caleb Narasigadu
, Christophe Coquelet
, Deresh Ramjugernath

University of KwaZulu-Natal
CTP - Centre Thermodynamique des Procédés

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

9 Citations (Scopus)

Abstract

Isothermal vapor-liquid equilibrium data are presented for binary systems containing perfluorobutane with carbon monoxide or nitric oxide. The measurements were undertaken for both systems at three temperatures ranging from (293 to 333) K, with pressures ranging from (0.965 to 16.130) MPa. The measured data were successfully correlated via the direct method using the Peng-Robinson equation of state incorporating the Mathias-Copeman/Stryjek-Vera alpha function and the Wong-Sandler mixing rule utilizing the nonrandom two-liquid (NRTL) activity coefficient model.

Original language	English
Pages (from-to)	346-354
Number of pages	9
Journal	Journal of Chemical and Engineering Data
Volume	59
Issue number	2
DOIs	https://doi.org/10.1021/je400822m
Publication status	Published - 13 Feb 2014
Externally published	Yes

ASJC Scopus subject areas

General Chemistry
General Chemical Engineering

Access to Document

10.1021/je400822m

Cite this

@article{e502288def414640895542260d0cba24,

title = "Vapor-liquid equilibrium (VLE) data and thermodynamic modeling for binary systems containing perfluorobutane (R610) with carbon monoxide or nitric oxide at (293, 313, and 333) K",

abstract = "Isothermal vapor-liquid equilibrium data are presented for binary systems containing perfluorobutane with carbon monoxide or nitric oxide. The measurements were undertaken for both systems at three temperatures ranging from (293 to 333) K, with pressures ranging from (0.965 to 16.130) MPa. The measured data were successfully correlated via the direct method using the Peng-Robinson equation of state incorporating the Mathias-Copeman/Stryjek-Vera alpha function and the Wong-Sandler mixing rule utilizing the nonrandom two-liquid (NRTL) activity coefficient model.",

author = "Tshibangu, \{Mulamba M.\} and Alain Valtz and Caleb Narasigadu and Christophe Coquelet and Deresh Ramjugernath",

year = "2014",

month = feb,

day = "13",

doi = "10.1021/je400822m",

language = "English",

volume = "59",

pages = "346--354",

journal = "Journal of Chemical and Engineering Data",

issn = "0021-9568",

publisher = "American Chemical Society",

number = "2",

}

Vapor-liquid equilibrium (VLE) data and thermodynamic modeling for binary systems containing perfluorobutane (R610) with carbon monoxide or nitric oxide at (293, 313, and 333) K. / Tshibangu, Mulamba M.; Valtz, Alain; Narasigadu, Caleb et al.
In: Journal of Chemical and Engineering Data, Vol. 59, No. 2, 13.02.2014, p. 346-354.

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

TY - JOUR

T1 - Vapor-liquid equilibrium (VLE) data and thermodynamic modeling for binary systems containing perfluorobutane (R610) with carbon monoxide or nitric oxide at (293, 313, and 333) K

AU - Tshibangu, Mulamba M.

AU - Valtz, Alain

AU - Narasigadu, Caleb

AU - Coquelet, Christophe

AU - Ramjugernath, Deresh

PY - 2014/2/13

Y1 - 2014/2/13

N2 - Isothermal vapor-liquid equilibrium data are presented for binary systems containing perfluorobutane with carbon monoxide or nitric oxide. The measurements were undertaken for both systems at three temperatures ranging from (293 to 333) K, with pressures ranging from (0.965 to 16.130) MPa. The measured data were successfully correlated via the direct method using the Peng-Robinson equation of state incorporating the Mathias-Copeman/Stryjek-Vera alpha function and the Wong-Sandler mixing rule utilizing the nonrandom two-liquid (NRTL) activity coefficient model.

AB - Isothermal vapor-liquid equilibrium data are presented for binary systems containing perfluorobutane with carbon monoxide or nitric oxide. The measurements were undertaken for both systems at three temperatures ranging from (293 to 333) K, with pressures ranging from (0.965 to 16.130) MPa. The measured data were successfully correlated via the direct method using the Peng-Robinson equation of state incorporating the Mathias-Copeman/Stryjek-Vera alpha function and the Wong-Sandler mixing rule utilizing the nonrandom two-liquid (NRTL) activity coefficient model.

UR - https://www.scopus.com/pages/publications/84894066577

U2 - 10.1021/je400822m

DO - 10.1021/je400822m

M3 - Article

AN - SCOPUS:84894066577

SN - 0021-9568

VL - 59

SP - 346

EP - 354

JO - Journal of Chemical and Engineering Data

JF - Journal of Chemical and Engineering Data

IS - 2

ER -

Vapor-liquid equilibrium (VLE) data and thermodynamic modeling for binary systems containing perfluorobutane (R610) with carbon monoxide or nitric oxide at (293, 313, and 333) K

Abstract

ASJC Scopus subject areas

Access to Document

Other files and links

Fingerprint

Cite this