A fundamental equation of state for cis-1,3,3,3-tetrafluoropropene (R-1234ze(Z))

Akasaka, Ryo; Higashi, Yukihiro; Miyara, Akio; Koyama, Shigeru

doi:10.1016/j.ijrefrig.2013.12.018

Cited by 52 publications

(60 citation statements)

References 16 publications

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“…There is a large amount of scatter that is shown in Figure 117, and we estimate the uncertainty is 5 %. ______________________________________________________________________________________________________ Cis-1,3,3,3-tetrafluoropropene) The equation of state of Akasaka and Lemmon (R. Akasaka & Lemmon, 2018) was used to provide the density and the critical parameters. Lennard-Jones parameters were calculated by the method of Chung et al (Chung et al, 1988).…”

Section: Chlorobenzenementioning

confidence: 99%

“…The equation of state of Akasaka et al (R. Akasaka, Fukushima, & Lemmon, 2017) was used to provide the density and the critical parameters, and an acentric factor of 0.322. LennardJones parameters were calculated by the method of Chung et al (Chung et al, 1988); values are presented in Table 1 The dipole moment was estimated to be 4.903x10 -30 C·m (1.47 D) (Kazakov, 2017).…”

Section: R1224yd(z) ((Z)-1-chloro-2333-tetrafluoropropene)mentioning

confidence: 99%

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Models for viscosity, thermal conductivity, and surface tension of selected pure fluids as implemented in REFPROP v10.0

Huber¹

2018

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We describe models for the viscosity, thermal conductivity, and surface tension for selected fluids implemented in version 10.0 of the NIST computer program, NIST Standard Reference Database 23, also known as NIST Reference Fluid Thermodynamic and Transport Properties Database (REFPROP). These fluids do not presently have published reference fluid quality models in the open literature, so we provide preliminary models based on available data as an interim measure to allow calculations of these properties. Comparisons with available experimental data are given.

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Section: Chlorobenzenementioning

confidence: 99%

Section: R1224yd(z) ((Z)-1-chloro-2333-tetrafluoropropene)mentioning

confidence: 99%

Models for viscosity, thermal conductivity, and surface tension of selected pure fluids as implemented in REFPROP v10.0

Huber¹

2018

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“…The experimental data are used to develop a saturated liquid density (ρ s,f ) correlation and a compressed liquid density (ρ) correlation. The ρ s,f correlation is compared to the correlation of [7] and the experimental data of [2] and [3], and the ρ correlation is compared to the correlation of [7] and the experimental data of [2]. However, before discussing these correlations (Eqs.…”

Section: Experimental Compressed Liquid Densitymentioning

confidence: 99%

“…The PvT experimental data of Table 6 was used to develop a Martin-Hou EoS for the vapor phase for T < 375 K and P < P c , which is compared to the correlation of [7] and the experimental data of [3]:…”

Section: Vapor-phase Pvt Correlationmentioning

confidence: 99%

“…(3) Kayukawa et al [4] report P vap measurements for T s from 273 K to 410 K; ρ s,f measurements for T s from 310 K to 420 K; PvT data for T from 283 K to 420 K for P up to 5 MPa; and vapor sound speeds for T from 293 K to 318 K. (4) Fedele et al [5] report P vap measurements for T s from 238 K to 372 K. Two research groups have presented equations of state (EoS) for R1234ze(Z): (1) Brown et al [6] presented a Peng-Robinson EoS and (2) Akasaka et al [7] presented a fundamental Helmholtz EoS, and one research group [8] has presented molecular dynamics simulations.…”

Section: Introductionmentioning

confidence: 99%

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Measurements and Correlations of cis-1,3,3,3-Tetrafluoroprop-1-ene (R1234ze(Z)) Subcooled Liquid Density and Vapor-Phase PvT

et al. 2014

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22 182 compressed liquid density data and 98 vapor-phase PvT data for cis-1,3,3,3-tetrafluoroprop-1-ene (R1234ze(Z)) are presented. The compressed liquid density data are for nine isotherms evenly spaced approximately from 283 K to 363 K for pressures from close to saturation to 35 MPa, and the vapor-phase PvT data are for seven isochores for temperatures approximately from 303 K to 375 K for pressures approximately from 82 kPa to 436 kPa. In addition, a saturated liquid density correlation, a Tait correlation for the compressed liquid density data, and a Martin-Hou equation of state for the vapor-phase PvT data are presented.Keywords cis-1,3,3,3-Tetrafluoroprop-1-ene · CF 3 CH=CHF · CAS number 29118-25-0 · Martin-Hou equation of state · PvT behavior · Saturated liquid density · Subcooled liquid density · Tait correlation · Vapor phase Electronic supplementary material The online version of this article (

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Applications of Molecular Simulations to Studies on Working Fluids

Raabe

2017

Molecular Simulation Studies on Thermophysical Properties

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A fundamental equation of state for cis-1,3,3,3-tetrafluoropropene (R-1234ze(Z))

Cited by 52 publications

References 16 publications

Models for viscosity, thermal conductivity, and surface tension of selected pure fluids as implemented in REFPROP v10.0

Models for viscosity, thermal conductivity, and surface tension of selected pure fluids as implemented in REFPROP v10.0

Measurements and Correlations of cis-1,3,3,3-Tetrafluoroprop-1-ene (R1234ze(Z)) Subcooled Liquid Density and Vapor-Phase PvT

Applications of Molecular Simulations to Studies on Working Fluids

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