Saturated liquid density and pressure measurements for HFC134a + HC290 by a compact single-sinker densimeter

Huiya Li; Xueqiang Dong; Haiyang Zhang; Quan Zhong; Hao Guo; Yanxing Zhao; Jun Shen; Maoqiong Gong

doi:10.1016/j.ijrefrig.2017.10.013

Saturated liquid density and pressure measurements for HFC134a + HC290 by a compact single-sinker densimeter

Huiya Li^*, Xueqiang Dong, Haiyang Zhang, Quan Zhong, Hao Guo, Yanxing Zhao, Jun Shen, Maoqiong Gong

^*Corresponding author for this work

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

4 Citations (Scopus)

Abstract

Saturated liquid densities and bubble point pressures for binary mixtures of 1,1,1,2-tetrafluoroethane (HFC134a) + propane (HC290) were measured using a compact single-sinker densimeter. The temperature range was from 253 to 293 K and mole fractions of HFC134a were 0.105, 0.197, 0.331, 0.387, 0.536 and 0.557. The standard uncertainties were estimated to be less than 5 mK for temperature, 1 kPa for pressure, 0.003 for mole fraction, and 0.02% for density. The experimental results were reproduced by VNDS equation and our modified Rackett equation. The saturated pressures data were correlated by the PR-Soave-vdW equation. Good agreement between values of calculation and experiment were found.

Original language	English
Pages (from-to)	376-382
Number of pages	7
Journal	International Journal of Refrigeration
Volume	85
DOIs	https://doi.org/10.1016/j.ijrefrig.2017.10.013
Publication status	Published - Jan 2018
Externally published	Yes

Keywords

Equation of state
HFC134a + HC290
Saturated liquid density
Saturated pressure

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10.1016/j.ijrefrig.2017.10.013

Cite this

@article{264d96ca8a6449058c2af561e971ff91,

title = "Saturated liquid density and pressure measurements for HFC134a + HC290 by a compact single-sinker densimeter",

abstract = "Saturated liquid densities and bubble point pressures for binary mixtures of 1,1,1,2-tetrafluoroethane (HFC134a) + propane (HC290) were measured using a compact single-sinker densimeter. The temperature range was from 253 to 293 K and mole fractions of HFC134a were 0.105, 0.197, 0.331, 0.387, 0.536 and 0.557. The standard uncertainties were estimated to be less than 5 mK for temperature, 1 kPa for pressure, 0.003 for mole fraction, and 0.02% for density. The experimental results were reproduced by VNDS equation and our modified Rackett equation. The saturated pressures data were correlated by the PR-Soave-vdW equation. Good agreement between values of calculation and experiment were found.",

keywords = "Equation of state, HFC134a + HC290, Saturated liquid density, Saturated pressure",

author = "Huiya Li and Xueqiang Dong and Haiyang Zhang and Quan Zhong and Hao Guo and Yanxing Zhao and Jun Shen and Maoqiong Gong",

note = "Publisher Copyright: {\textcopyright} 2017 Elsevier Ltd and IIR",

year = "2018",

month = jan,

doi = "10.1016/j.ijrefrig.2017.10.013",

language = "English",

volume = "85",

pages = "376--382",

journal = "International Journal of Refrigeration",

issn = "0140-7007",

publisher = "Elsevier Ltd.",

}

TY - JOUR

T1 - Saturated liquid density and pressure measurements for HFC134a + HC290 by a compact single-sinker densimeter

AU - Li, Huiya

AU - Dong, Xueqiang

AU - Zhang, Haiyang

AU - Zhong, Quan

AU - Guo, Hao

AU - Zhao, Yanxing

AU - Shen, Jun

AU - Gong, Maoqiong

PY - 2018/1

Y1 - 2018/1

N2 - Saturated liquid densities and bubble point pressures for binary mixtures of 1,1,1,2-tetrafluoroethane (HFC134a) + propane (HC290) were measured using a compact single-sinker densimeter. The temperature range was from 253 to 293 K and mole fractions of HFC134a were 0.105, 0.197, 0.331, 0.387, 0.536 and 0.557. The standard uncertainties were estimated to be less than 5 mK for temperature, 1 kPa for pressure, 0.003 for mole fraction, and 0.02% for density. The experimental results were reproduced by VNDS equation and our modified Rackett equation. The saturated pressures data were correlated by the PR-Soave-vdW equation. Good agreement between values of calculation and experiment were found.

AB - Saturated liquid densities and bubble point pressures for binary mixtures of 1,1,1,2-tetrafluoroethane (HFC134a) + propane (HC290) were measured using a compact single-sinker densimeter. The temperature range was from 253 to 293 K and mole fractions of HFC134a were 0.105, 0.197, 0.331, 0.387, 0.536 and 0.557. The standard uncertainties were estimated to be less than 5 mK for temperature, 1 kPa for pressure, 0.003 for mole fraction, and 0.02% for density. The experimental results were reproduced by VNDS equation and our modified Rackett equation. The saturated pressures data were correlated by the PR-Soave-vdW equation. Good agreement between values of calculation and experiment were found.

KW - Equation of state

KW - HFC134a + HC290

KW - Saturated liquid density

KW - Saturated pressure

UR - http://www.scopus.com/inward/record.url?scp=85035045765&partnerID=8YFLogxK

U2 - 10.1016/j.ijrefrig.2017.10.013

DO - 10.1016/j.ijrefrig.2017.10.013

M3 - Article

AN - SCOPUS:85035045765

SN - 0140-7007

VL - 85

SP - 376

EP - 382

JO - International Journal of Refrigeration

JF - International Journal of Refrigeration

ER -

Saturated liquid density and pressure measurements for HFC134a + HC290 by a compact single-sinker densimeter

Abstract

Keywords

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