Experimental measurement of vapor-liquid equilibrium for (trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) + propane (R290))

Xueqiang Dong; Maoqiong Gong; Jun Shen; Jianfeng Wu

doi:10.1016/j.ijrefrig.2011.03.007

Experimental measurement of vapor-liquid equilibrium for (trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) + propane (R290))

Xueqiang Dong, Maoqiong Gong^*, Jun Shen, Jianfeng Wu

^*Corresponding author for this work

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

64 Citations (Scopus)

Abstract

The VLE data for the binary system of R1234ze(E) + R290 were measured with a recirculation method at four temperatures (258.150, 263.150, 273.150 and 283.150 K). The measured uncertainties of the temperature, pressure, and compositions are ±5 mK, ±0.0005 MPa, and ±0.005, respectively. All the experimental data were correlated by the Peng-Robinson (PR) EoS with the Huron-Vidal (HV) mixing rule involving the non-random two-liquid (NRTL) activity coefficient (PR-HV-NRTL) model. Azeotropic behavior can be found at the measured temperature range.

Original language	English
Pages (from-to)	1238-1243
Number of pages	6
Journal	International Journal of Refrigeration
Volume	34
Issue number	5
DOIs	https://doi.org/10.1016/j.ijrefrig.2011.03.007
Publication status	Published - Aug 2011
Externally published	Yes

Keywords

Azeotropic mixtures
Equilibrium
R290
Refrigerant

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10.1016/j.ijrefrig.2011.03.007

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title = "Experimental measurement of vapor-liquid equilibrium for (trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) + propane (R290))",

abstract = "The VLE data for the binary system of R1234ze(E) + R290 were measured with a recirculation method at four temperatures (258.150, 263.150, 273.150 and 283.150 K). The measured uncertainties of the temperature, pressure, and compositions are ±5 mK, ±0.0005 MPa, and ±0.005, respectively. All the experimental data were correlated by the Peng-Robinson (PR) EoS with the Huron-Vidal (HV) mixing rule involving the non-random two-liquid (NRTL) activity coefficient (PR-HV-NRTL) model. Azeotropic behavior can be found at the measured temperature range.",

keywords = "Azeotropic mixtures, Equilibrium, R290, Refrigerant",

author = "Xueqiang Dong and Maoqiong Gong and Jun Shen and Jianfeng Wu",

year = "2011",

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doi = "10.1016/j.ijrefrig.2011.03.007",

language = "English",

volume = "34",

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T1 - Experimental measurement of vapor-liquid equilibrium for (trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) + propane (R290))

AU - Dong, Xueqiang

AU - Gong, Maoqiong

AU - Shen, Jun

AU - Wu, Jianfeng

PY - 2011/8

Y1 - 2011/8

N2 - The VLE data for the binary system of R1234ze(E) + R290 were measured with a recirculation method at four temperatures (258.150, 263.150, 273.150 and 283.150 K). The measured uncertainties of the temperature, pressure, and compositions are ±5 mK, ±0.0005 MPa, and ±0.005, respectively. All the experimental data were correlated by the Peng-Robinson (PR) EoS with the Huron-Vidal (HV) mixing rule involving the non-random two-liquid (NRTL) activity coefficient (PR-HV-NRTL) model. Azeotropic behavior can be found at the measured temperature range.

AB - The VLE data for the binary system of R1234ze(E) + R290 were measured with a recirculation method at four temperatures (258.150, 263.150, 273.150 and 283.150 K). The measured uncertainties of the temperature, pressure, and compositions are ±5 mK, ±0.0005 MPa, and ±0.005, respectively. All the experimental data were correlated by the Peng-Robinson (PR) EoS with the Huron-Vidal (HV) mixing rule involving the non-random two-liquid (NRTL) activity coefficient (PR-HV-NRTL) model. Azeotropic behavior can be found at the measured temperature range.

KW - Azeotropic mixtures

KW - Equilibrium

KW - R290

KW - Refrigerant

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DO - 10.1016/j.ijrefrig.2011.03.007

M3 - Article

AN - SCOPUS:79958745833

SN - 0140-7007

VL - 34

SP - 1238

EP - 1243

JO - International Journal of Refrigeration

JF - International Journal of Refrigeration

IS - 5

ER -

Experimental measurement of vapor-liquid equilibrium for (trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) + propane (R290))

Abstract

Keywords

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