Liquid and Vapor Viscosities of Binary Refrigerant Mixtures Containing R1234yf or R1234ze(E)

Masoumeh Akhfash; Saif Z.S. Al Ghafri; Darren Rowland; Thomas J. Hughes; Tomoya Tsuji; Yukio Tanaka; Yoshio Seiki; Eric F. May

doi:10.1021/acs.jced.8b01039

Liquid and Vapor Viscosities of Binary Refrigerant Mixtures Containing R1234yf or R1234ze(E)

Masoumeh Akhfash, Saif Z.S. Al Ghafri, Darren Rowland, Thomas J. Hughes, Tomoya Tsuji, Yukio Tanaka, Yoshio Seiki, Eric F. May

Research output: Contribution to journal › Article

5 Citations (Scopus)

Abstract

Liquid and vapor viscosities are reported for the binary refrigerant mixtures (R125 + R152a), (R125 + R1234ze(E)), (R143a + R1234ze(E)), (R143a + R1234yf), and (R1234ze(E) + R1234yf). The measurements were made with a vibrating wire viscometer and span temperatures from (252 to 403) K and pressures from (0.9 to 4.0) MPa. The performance of the vibrating-wire apparatus was validated by measuring the viscosity of pure R152a in both the vapor and liquid regions. These measurements and previously published data were used to tune binary interaction parameters in the extended corresponding states equation model for viscosity implemented in the NIST software REFPROP 9.1. After tuning, deviations between the model and reported viscosities were reduced from between (-4 and 8)% to within ±2%.

Original language	English
Pages (from-to)	1122-1130
Journal	Journal of Chemical and Engineering Data
Volume	64
Issue number	3
DOIs	https://doi.org/10.1021/acs.jced.8b01039
Publication status	Published - 14 Mar 2019

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@article{23fadb6182cb45908086f0f328dbf724,

title = "Liquid and Vapor Viscosities of Binary Refrigerant Mixtures Containing R1234yf or R1234ze(E)",

abstract = "Liquid and vapor viscosities are reported for the binary refrigerant mixtures (R125 + R152a), (R125 + R1234ze(E)), (R143a + R1234ze(E)), (R143a + R1234yf), and (R1234ze(E) + R1234yf). The measurements were made with a vibrating wire viscometer and span temperatures from (252 to 403) K and pressures from (0.9 to 4.0) MPa. The performance of the vibrating-wire apparatus was validated by measuring the viscosity of pure R152a in both the vapor and liquid regions. These measurements and previously published data were used to tune binary interaction parameters in the extended corresponding states equation model for viscosity implemented in the NIST software REFPROP 9.1. After tuning, deviations between the model and reported viscosities were reduced from between (-4 and 8)% to within ±2%.",

author = "Masoumeh Akhfash and {Al Ghafri}, {Saif Z.S.} and Darren Rowland and Hughes, {Thomas J.} and Tomoya Tsuji and Yukio Tanaka and Yoshio Seiki and May, {Eric F.}",

year = "2019",

month = mar,

day = "14",

doi = "10.1021/acs.jced.8b01039",

language = "English",

volume = "64",

pages = "1122--1130",

journal = "Journal of Chemical & Engineering Data",

issn = "0021-9568",

publisher = "American Chemical Society",

number = "3",

}

Liquid and Vapor Viscosities of Binary Refrigerant Mixtures Containing R1234yf or R1234ze(E). / Akhfash, Masoumeh; Al Ghafri, Saif Z.S.; Rowland, Darren; Hughes, Thomas J.; Tsuji, Tomoya; Tanaka, Yukio; Seiki, Yoshio; May, Eric F.

In: Journal of Chemical and Engineering Data, Vol. 64, No. 3, 14.03.2019, p. 1122-1130.

Research output: Contribution to journal › Article

TY - JOUR

T1 - Liquid and Vapor Viscosities of Binary Refrigerant Mixtures Containing R1234yf or R1234ze(E)

AU - Akhfash, Masoumeh

AU - Al Ghafri, Saif Z.S.

AU - Rowland, Darren

AU - Hughes, Thomas J.

AU - Tsuji, Tomoya

AU - Tanaka, Yukio

AU - Seiki, Yoshio

AU - May, Eric F.

PY - 2019/3/14

Y1 - 2019/3/14

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AB - Liquid and vapor viscosities are reported for the binary refrigerant mixtures (R125 + R152a), (R125 + R1234ze(E)), (R143a + R1234ze(E)), (R143a + R1234yf), and (R1234ze(E) + R1234yf). The measurements were made with a vibrating wire viscometer and span temperatures from (252 to 403) K and pressures from (0.9 to 4.0) MPa. The performance of the vibrating-wire apparatus was validated by measuring the viscosity of pure R152a in both the vapor and liquid regions. These measurements and previously published data were used to tune binary interaction parameters in the extended corresponding states equation model for viscosity implemented in the NIST software REFPROP 9.1. After tuning, deviations between the model and reported viscosities were reduced from between (-4 and 8)% to within ±2%.

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