Ethane, 1,1,1,2-tetrafluoro-

Synonym: 1,1,1,2-tetrafluoroethane

Molecular formula:	C₂H₂F₄
Molar mass:	102.03 g·mol^-1
CAS registry number:	811-97-2

W. Ren and A. M. Scurto
Phase equilibria of imidazolium ionic liquids and the refrigerant gas, 1,1,1,2-tetrafluoroethane (R-134a)
Fluid Phase Equilib. • Year: 2009 • Volume: 286 • Pages: 1-7.
Keywords: Imidazolium ionic liquids, Mixture critical points, 1,1,1,2-Tetrafluoroethane (R-134a), Vapor liquid equilibrium, Vapor liquid liquid equilibrium
DOI: 10.1016/j.fluid.2009.07.007
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2009.07.007.xml

J. Liu, D. Li, H. S. Byun and M. A. McHugh
Impact of fluorine on the phase behavior of bis-p-tolyl propane in supercritical CO2, 1,1-difluoroethane, and 1,1,1,2-tetrafluoroethane
Fluid Phase Equilib. • Year: 2008 • Volume: 267 • Pages: 39-46.
DOI: 10.1016/j.fluid.2008.02.016
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2008.02.016.xml

Chaudhari, S. K., Salavera, D., Esteve, X., Coronas, A.
Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
Fluid Phase Equilib. • Year: 2008 • Volume: 271 • Pages: 28-33.
DOI: 10.1016/j.fluid.2008.07.003
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2008.07.003.xml

L. Fedele, S. Bobbo, R. Camporese and M. Scattolini
Isothermal vapour + liquid equilibrium measurements and correlation for the pentafluoroethane + cyclopropane and the cyclopropane + 1,1,1,2-tetrafluoroethane binary systems
Fluid Phase Equilib. • Year: 2007 • Volume: 251 • Pages: 41-46.
Keywords: (Vapour + liquid) equilibria, Cyclopropane (RC270), Pentafluoroethane (R125), 1,1,1,2-Tetrafluoroethane (R134a)
DOI: 10.1016/j.fluid.2006.10.023
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.10.023.xml

Monsalvo, M. A., Baylaucq, A., Reghem, P.[Patrick], Quinones-Cisneros, S. E., Boned, C.
Viscosity measurements and correlations of binary mixtures: 1,1,1,2-tetrafluoroethane (HFC-134a) + tetraethylene glycol dimethylether (TEGDME)
Fluid Phase Equilib. • Year: 2005 • Volume: 233 • Pages: 1-8.
Keywords: Viscosity, Measurements, Modeling, Refrigerant, Lubricant, Mixtures
DOI: 10.1016/j.fluid.2005.03.030
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2005.03.030.xml

Q. Chen, Y. Tong, R.-h. Hong and G.-m. Chen
Gas phase PVTx properties for binary mixtures of HFC-161 and HFC-134a
Fluid Phase Equilib. • Year: 2011 • Volume: 304 • Pages: 61-63.
Keywords: Gas phase, PVTx properties, Equation of state, HFC-161/134a mixtures
DOI: 10.1016/j.fluid.2011.02.012
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2011.02.012.xml

A. Valtz, L. Gicquel, C. Coquelet and D. Richon
Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
Fluid Phase Equilib. • Year: 2005 • Volume: 230 • Pages: 184-191.
Keywords: VLE data, High pressures, Refrigerants, Modelling, Azeotrope, 1,1,1,2 Tetrafluoroethane (R134a), Dimethyl ether (DME)
ThermoML: http://trc.nist.gov/journals/fpe/2005v230/i01/2005valgic0.xml

M. A. Monsalvo, A. Baylaucq, S. E. Quinones-Cisneros and C. Boned
High-pressure viscosity behavior of x 1,1,1,2-tetrafluoroethane (HFC-134a) + (1-x) triethylene glycol dimethylether (TriEGDME) mixtures: Measurements and modeling
Fluid Phase Equilib. • Year: 2006 • Volume: 247 • Pages: 70-79.
Keywords: Viscosity, Measurements, Refrigerants, Lubricants, Modeling
DOI: 10.1016/j.fluid.2006.06.015
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.06.015.xml

J. S. Lim, J. -Y. Park, j. W. Kang and B. G. Lee
Measurement of vapor liquid equilibria for the binary systems of propane + 1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane + propane at various temperatures
Fluid Phase Equilib. • Year: 2006 • Volume: 243 • Pages: 57-63.
Keywords: Propane (R-290), HFC-134a, HFC-143a, Azeotropic mixture, Vapor liquid equilibria (VLE), Carnahan Starling De Santis equation of state (CSD EOS)
DOI: 10.1016/j.fluid.2006.02.016
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.02.016.xml

X.-l. Cui, G.-m. Chen, X.-h. Han and Q. Wang
Experimental vapor pressure data and a vapor pressure equation for fluoroethane (HFC-161)
Fluid Phase Equilib. • Year: 2006 • Volume: 245 • Pages: 155-157.
Keywords: Vapor pressure, Fluoroethane, Vapor pressure equation, Alternatives
DOI: 10.1016/j.fluid.2006.04.014
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.04.014.xml

R. Kato and H. Nishiumi
Vapor liquid equilibria and critical loci of binary and ternary systems composed of CH2F2, C2HF5 and C2H2F4
Fluid Phase Equilib. • Year: 2006 • Volume: 249 • Pages: 140-146.
Keywords: Vapor liquid equilibria, Critical locus, Binary system, Ternary system, CH2F2, C2HF5, C2H2F4, Peng Robinson equation state
DOI: 10.1016/j.fluid.2006.07.017
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.07.017.xml

X. Cui, G. Chen, C. Li and X. Han
Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
Fluid Phase Equilib. • Year: 2006 • Volume: 249 • Pages: 97-103.
DOI: 10.1016/j.fluid.2006.09.017
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.09.017.xml

A. Laesecke and S. Bair
High-Pressure Viscosity Measurements of 1,1,1,2-Tetrafluoroethane
Int. J. Thermophys. • Year: 2011 • Volume: 32 • Pages: 925-941.
Keywords: 1,1,1,2-tetrafluoroethane, Compressed liquid, Falling-body viscometer, High pressure, n-octane, R134a, Supercritical, Viscosity
DOI: 10.1016/s10765-011-0978-y
ThermoML: http://trc.nist.gov/ThermoML/10.1007/s10765-011-0978-y.xml

G. Di Nicola, G. Santori and R. Stryjek
Solid-Liquid Equilibria for the Carbon Dioxide + 1,1-Tetrafluoroethane and Nitrous Oxide + 1,1-Tetrafluoroethane Systems
J. Chem. Eng. Data • Year: 2008 • Volume: 53 • Pages: 1980-1983.
DOI: 10.1021/je800285k
ThermoML: http://trc.nist.gov/journals/jced/2008v53/i08/je800285k.xml

X. Dong, M. Gong, Y. Zhang and J. Wu
Vapor-Liquid Equilibria of the Fluoroethane (R161) + 1,1,1,2-Tetrafluoroethane (R134a) System at Various Temperatures from (253.15 to 292.92) K
J. Chem. Eng. Data • Year: 2008 • Volume: 53 • Pages: 2193-2196.
DOI: 10.1021/je800505y
ThermoML: http://trc.nist.gov/journals/jced/2008v53/i09/je800505y.xml

Neindre, B. L., Garrabos, Y., Gumerov, F., Sabirzianov, A.
Measurements of the Thermal Conductivity of HFC-134a in the Supercritical Region
J. Chem. Eng. Data • Year: 2009 • Volume: 54 • Pages: 2678-2688.
DOI: 10.1021/je900210h
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je900210h.xml

E. R. Lopez, A. M. Mainar, J. S. Urieta and J. Fernandez
Solubility of HFC134a (1,1,1,2-Tetrafluoroethane) in Two Dialkyl Carbonates
J. Chem. Eng. Data • Year: 2009 • Volume: 54 • Pages: 2609-2615.
DOI: 10.1021/je900138j
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je900138j.xml

L. Liu, Z. Li, Z.-W. Liu and Z.-T. Liu
Solubilities of L-Proline in Subcritical HFC-134a and Supercritical CO2 Fluids
J. Chem. Eng. Data • Year: 2009 • Volume: 54 • Pages: 2780-2784.
DOI: 10.1021/je801009z
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je801009z.xml

Shiflett, M. B.[Mark B.], Yokozeki, A.
Vapor-Liquid-Liquid Equilibria of Hydrofluorocarbons + 1-Butyl-3-methylimidazolium Hexafluorophosphate
J. Chem. Eng. Data • Year: 2006 • Volume: 51 • Pages: 1931-1939.
DOI: 10.1021/je060275f
ThermoML: http://trc.nist.gov/journals/jced/2006v51/i05/je060275f.xml

X.-l. Cui, G.-m. Chen, X.-h. Han and C. S. Li
Vapor-Liquid Equilibria for the Trifluoromethane + 1,1,1,2-Tetrafluoroethane System
J. Chem. Eng. Data • Year: 2006 • Volume: 51 • Pages: 1927-1930.
DOI: 10.1021/je0602622
ThermoML: http://trc.nist.gov/journals/jced/2006v51/i05/je0602622.xml

Z.-T. Liu, L. Liu, J. Wu, L. Song, Z. Gao, W. Dong and J. Lu
Solubility and Phase Behaviors of AOT Analogue Surfactants in 1,1,1,2-Tetrafluoroethane and Supercritical Carbon Dioxide
J. Chem. Eng. Data • Year: 2006 • Volume: 51 • Pages: 2045-2050.
DOI: 10.1021/je060152v
ThermoML: http://trc.nist.gov/journals/jced/2006v51/i06/je060152v.xml

H. Hong, M. Gong and J. Wu
Solubility Measurements of 1,1,1,2-Tetrafluoroethane (R134a) and of Propane in Squalane at Temperatures from (325 to 400) K and Pressures from (0.1 to 1) MPa
J. Chem. Eng. Data • Year: 2006 • Volume: 51 • Pages: 2270-2273.
DOI: 10.1021/je060330k
ThermoML: http://trc.nist.gov/journals/jced/2006v51/i06/je060330k.xml

D. Yuan-yuan and L. Hong
Surface Tension Measurements of Difluoromethane(R-32) and the Binary Mixture Difluoromethane(R-32) + 1,1,1,2-tetrafluoroethane(R-134a) from (253 to 333) K
J. Chem. Eng. Data • Year: 2003 • Volume: 48 • Pages: 1068-1072.
Keywords: Surface tension, DCRM, Mixture, Difluoromethane(R-32), 1, 1, 1, 2-tetrafluoroethane(R-134a)
DOI: 10.1021/je030137f
ThermoML: http://trc.nist.gov/journals/jced/2003v48/i04/je030137f.xml

M. Yasumoto, Y. Yamada, J. Murata, S. Urata and K. Otake
Critical Parameters and Vapor Pressures Measurements of Hydrofluoroethers at High Temperatures
J. Chem. Eng. Data • Year: 2003 • Volume: 48 • Pages: 1368-1379.
Keywords: Critical Properties, vapor pressure, hydrofluoroether, Antoine parameter, Wagner parameter
DOI: 10.1021/je0201976
ThermoML: http://trc.nist.gov/journals/jced/2003v48/i06/je0201976.xml

Im, J.[Jihoon], Kim, M., Lee, B.-G., Hwayong, K.[Kim]
Vapor-Liquid Equilibria of the Binary n-Butane (HC-600) + Difluoromethane (HFC-32), + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a) Mixture Systems
J. Chem. Eng. Data • Year: 2005 • Volume: 50 • Pages: 359-363.
Keywords: Binary vapor liquid equilibriua, n-butane, difluoromethane, pentafluoroethane, 1,1,1,2-tetrafluoroethane
DOI: 10.1021/je049817o
ThermoML: http://trc.nist.gov/journals/jced/2005v50/i02/je049817o.xml

B. Saleh and M. Wendland
Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
J. Chem. Eng. Data • Year: 2005 • Volume: 50 • Pages: 429-437.
Keywords: vapor-liquid equilibria, new apparatus, pure fluids, saturated liquid densities
DOI: 10.1021/je0497496
ThermoML: http://trc.nist.gov/journals/jced/2005v50/i02/je0497496.xml

H. Lin and Y. -Y. Duan
Surface Tension for the 1,1,1-Trifluoroethane (R-143a) + 1,1,1,2-Tetrafluoroethane (R-134a) System
J. Chem. Eng. Data • Year: 2004 • Volume: 49 • Pages: 372-375.
Keywords: Surface tension, DCRM, mixture, R-143a+R-134a
DOI: 10.1021/je0342163
ThermoML: http://trc.nist.gov/journals/jced/2004v49/i02/je0342163.xml

Y. Uchida, M. Yasumoto, Y. Yamada, K. Ochi, T. Furuya and K. Otake
Critical Properties of Four HFE + HFC Binary Systems: Trifluoromethoxymethane (HFE-143m) + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a), + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea), and + 1,1,1,2,3,3-Hexafluoropropane (HFC-236ea)
J. Chem. Eng. Data • Year: 2004 • Volume: 49 • Pages: 1615-1621.
Keywords: critical properties
DOI: 10.1021/je0499723
ThermoML: http://trc.nist.gov/journals/jced/2004v49/i06/je0499723.xml

K. Otake, Y. Uchida, M. Yasumoto, Y. Yamada, T. Furuya and K. Ochi
Critical Parameters Measurements of Four HFE + HFC Binary Systems: Pentafluoromethoxyethane (HFE-245Mc) + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a), + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea), and + 1,1,1,2,3,3-Hexafluoropropane (HFC-236ea)
J. Chem. Eng. Data • Year: 2004 • Volume: 49 • Pages: 1643-1647.
Keywords: critical properties
DOI: 10.1021/je0499420
ThermoML: http://trc.nist.gov/journals/jced/2004v49/i06/je0499420.xml

G. Di Nicola, F. Polonara and G. Santori
Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf)
J. Chem. Eng. Data • Year: 2010 • Volume: 55 • Pages: 201-204.
DOI: 10.1021/je900306v
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je900306v.xml

R. Zehioua, C. Coquelet, A. H. Meniai and D. Richon
Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
J. Chem. Eng. Data • Year: 2010 • Volume: 55 • Pages: 985-988.
DOI: 10.1021/je900440t
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je900440t.xml

Y. Zhang and M. He
Kinematic Viscosity of R410A and R407C Refrigerant-Oil Mixtures in the Saturated Liquid Phase with Lubricant Mass Fraction in the Range of (0 to 0.0001)
J. Chem. Eng. Data • Year: 2010 • Volume: 55 • Pages: 2886-2889.
DOI: 10.1021/je9009442
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je9009442.xml

R. Zehioua, C. Coquelet, A. H. Meniai and D. Richon
p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
J. Chem. Eng. Data • Year: 2010 • Volume: 55 • Pages: 2769-2775.
DOI: 10.1021/je9009915
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je9009915.xml

C. D. Nicola, G. D. Nicola, M. Pacetti, F. Polonara and G. Santori
P-V-T Behavior of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf) in the Vapor Phase from (243 to 373) K
J. Chem. Eng. Data • Year: 2010 • Volume: 55 • Pages: 3302-3306.
DOI: 10.1021/je100102q
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je100102q.xml

X. Han, Z. Gao, Y. Xu, Y. Qiu, X. Min, X. Cui and G. Chen
Solubility of Refrigerant 1,1,1,2-Tetrafluoroethane in the N,N-Dimethyl Formamide in the Temperature Range from (263.15 to 363.15) K
J. Chem. Eng. Data • Year: 2011 • Volume: 56 • Pages: 1821-1826.
DOI: 10.1021/je100975b
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je100975b.xml

Fedele, L.[Laura], Bobbo, S.[Sergio], Groppo, F.[Fabio], Brown, J. S., Zilio, C.[Claudio]
Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) for Reduced Temperatures Ranging from 0.67 to 0.93
J. Chem. Eng. Data • Year: 2011 • Volume: 56 • Pages: 2608-2612.
Keywords: 1,1,1,2-tetrafluoroethane (R134a), 2,3,3,3-tetrafluoroprop-1-ene (R1234yf),, experimental method, extended Antoine-type equation, normal boiling temperature, saturated, pressure, Wagner-type equation.
DOI: 10.1021/je2000952
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je2000952.xml

Shiflett, M. B.[Mark B.], Yokozeki, A.
Solubility Differences of Halocarbon Isomers in Ionic Liquid [emim][Tf2N]
J. Chem. Eng. Data • Year: 2007 • Volume: 52 • Pages: 2007-2015.
DOI: 10.1021/je700295e
ThermoML: http://trc.nist.gov/journals/jced/2007v52/i05/je700295e.xml

M. Mukoubayashi, K. Ichikura and Y. Kano
PVT Property Measurements for R143a, R125, and R32 in the Gaseous Phase
J. Chem. Eng. Data • Year: 2007 • Volume: 52 • Pages: 1925-1929.
DOI: 10.1021/je700236c
ThermoML: http://trc.nist.gov/journals/jced/2007v52/i05/je700236c.xml

J. S. Lim, G. Seong and H.-K. Roh
Vapor-Liquid Equilibria for the 1,1,1,2-Tetrafluoroethane (HFC-134a) + n-Butane (R-600) System
J. Chem. Eng. Data • Year: 2007 • Volume: 52 • Pages: 1313-1318.
DOI: 10.1021/je700041v
ThermoML: http://trc.nist.gov/journals/jced/2007v52/i04/je700041v.xml

Marchi, P.[Paolo], Scalabrin, G.[Giancarlo], Ihmels, E. C., Fischer, K.[Kai], Gmehling, J.[Juergen]
Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
J. Chem. Thermodyn. • Year: 2006 • Volume: 38 • Pages: 1247-1253.
Keywords: R134a, (Refrigerant + lubricant), Solubility, TriEGDME, VLE measurements
DOI: 10.1016/2006marsca2
ThermoML: http://trc.nist.gov/ThermoML/jct/2006marsca2.xml

X. Dong, M. Gong, J. Liu and J. Wu
Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
J. Chem. Thermodyn. • Year: 2011 • Volume: 43 • Pages: 505-510.
Keywords: Saturated vapor pressures, (Vapor + liquid) equilibrium, 1,1,1,2-Tetrafluoroethane, Propane
DOI: 10.1016/j.jct.2010.11.001
ThermoML: http://trc.nist.gov/ThermoML/10.1016/j.jct.2010.11.001.xml