Thermal conductivity measurements and correlations of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf

Thermal conductivity measurements of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf were conducted in the homogeneous liquid and vapour phases with a transient hot-wire technique. The mole fractions of R32 are 0.25, 0.50, and 0.75 in both binary systems. The temperature range of...

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Main Authors: Kim, D., Liu, H., Yang, X., Yang, F., Morfitt, J., Arami-Niya, Arash, Ryu, M., Duan, Y., May, E.F.
Format: Journal Article
Published: 2021
Online Access:http://purl.org/au-research/grants/arc/IC150100019
http://hdl.handle.net/20.500.11937/87785
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author Kim, D.
Liu, H.
Yang, X.
Yang, F.
Morfitt, J.
Arami-Niya, Arash
Ryu, M.
Duan, Y.
May, E.F.
author_facet Kim, D.
Liu, H.
Yang, X.
Yang, F.
Morfitt, J.
Arami-Niya, Arash
Ryu, M.
Duan, Y.
May, E.F.
author_sort Kim, D.
building Curtin Institutional Repository
collection Online Access
description Thermal conductivity measurements of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf were conducted in the homogeneous liquid and vapour phases with a transient hot-wire technique. The mole fractions of R32 are 0.25, 0.50, and 0.75 in both binary systems. The temperature range of the measurements was from (264.1 to 405.6) K with pressures ranging between (0.9 and 6.1) MPa. The transient hot-wire apparatus was validated with measurements of pure CO2 in both the liquid and vapour regions. The relative combined expanded uncertainty (k = 2) in the experimental thermal conductivity was approximately 2.0 %. The relative deviations of the measured thermal conductivities from those calculated using the extended corresponding states (ECS) model as implemented in the software REFPROP 10 were between (−13 and 10) % in the vapour phase, and between (−14 and 1) % in the liquid phase. Additionally, the performance of a new approach to predicting fluid transport properties, the residual entropy scaling model incorporating the cubic-plus-association equation of state (RES-CPA model) was tested for these mixtures by first determining the scaling parameter of pure R1243zf. The RES-CPA model was then able to predict the mixture thermal conductivities generally within 10 %, which is similar to the ECS model; however no additional parameters were introduced to the RES-CPA model to describe binary interactions.
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institution Curtin University Malaysia
institution_category Local University
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publishDate 2021
recordtype eprints
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spelling curtin-20.500.11937-877852023-08-01T00:32:36Z Thermal conductivity measurements and correlations of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf Kim, D. Liu, H. Yang, X. Yang, F. Morfitt, J. Arami-Niya, Arash Ryu, M. Duan, Y. May, E.F. Thermal conductivity measurements of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf were conducted in the homogeneous liquid and vapour phases with a transient hot-wire technique. The mole fractions of R32 are 0.25, 0.50, and 0.75 in both binary systems. The temperature range of the measurements was from (264.1 to 405.6) K with pressures ranging between (0.9 and 6.1) MPa. The transient hot-wire apparatus was validated with measurements of pure CO2 in both the liquid and vapour regions. The relative combined expanded uncertainty (k = 2) in the experimental thermal conductivity was approximately 2.0 %. The relative deviations of the measured thermal conductivities from those calculated using the extended corresponding states (ECS) model as implemented in the software REFPROP 10 were between (−13 and 10) % in the vapour phase, and between (−14 and 1) % in the liquid phase. Additionally, the performance of a new approach to predicting fluid transport properties, the residual entropy scaling model incorporating the cubic-plus-association equation of state (RES-CPA model) was tested for these mixtures by first determining the scaling parameter of pure R1243zf. The RES-CPA model was then able to predict the mixture thermal conductivities generally within 10 %, which is similar to the ECS model; however no additional parameters were introduced to the RES-CPA model to describe binary interactions. 2021 Journal Article http://hdl.handle.net/20.500.11937/87785 10.1016/j.ijrefrig.2021.07.019 http://purl.org/au-research/grants/arc/IC150100019 http://creativecommons.org/licenses/by-nc-nd/4.0/ fulltext
spellingShingle Kim, D.
Liu, H.
Yang, X.
Yang, F.
Morfitt, J.
Arami-Niya, Arash
Ryu, M.
Duan, Y.
May, E.F.
Thermal conductivity measurements and correlations of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf
title Thermal conductivity measurements and correlations of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf
title_full Thermal conductivity measurements and correlations of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf
title_fullStr Thermal conductivity measurements and correlations of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf
title_full_unstemmed Thermal conductivity measurements and correlations of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf
title_short Thermal conductivity measurements and correlations of pure R1243zf and binary mixtures of R32 + R1243zf and R32 + R1234yf
title_sort thermal conductivity measurements and correlations of pure r1243zf and binary mixtures of r32 + r1243zf and r32 + r1234yf
url http://purl.org/au-research/grants/arc/IC150100019
http://hdl.handle.net/20.500.11937/87785