Fluoroethane

Molecular formula: C2H5F
Molar mass: 48.06 g·mol-1
CAS registry number: 353-36-6

Han, X. H., Gao, Z. J., Xu, Y. J., Qiu, Y., Ming, X. W., Wang, Q., Chen, G. M.
Isothermal vapor-liquid equilibrium data for the binary mixture difluoromethane (HFC-32)+ ethyl fluoride (HFC-161) over a temperature range from 253.15 to 303.15 K
Fluid Phase Equilib.Year: 2010Volume: 299Pages: 116-121.
Keywords: Alternative refrigerants, HFC-161, Vapor-liquid equilibrium, Mixing rule, Equation of state
DOI: 10.1016/j.fluid.2010.09.016
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2010.09.016.xml
Q. Chen, R.-h. Hong and G.-m. Chen
PVTx measurements in the gas phase for binary mixtures of HFC-161 and HFC-227ea
Fluid Phase Equilib.Year: 2008Volume: 269Pages: 113-116.
DOI: 10.1016/j.fluid.2008.04.022
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2008.04.022.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: 2011Volume: 304Pages: 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
Q. Wang, Y.-J. Xu, Z.-J. Gao, Y. Qiu, X.-W. Min, X.-h. Han and G.-m. Chen
Isothermal vapor-liquid equilibrium data for the binary mixture ethyl fluoride (HFC-161) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) over a temperature range from 253.15 K to 313.15 K
Fluid Phase Equilib.Year: 2010Volume: 297Pages: 67-71.
Keywords: HFC-227ea, HFC-161, Vapor liquid equilibrium, Mixing rule, Equation of state
DOI: 10.1016/j.fluid.2010.06.006
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2010.06.006.xml
Q. Chen, R.-h. Hong and G.-m. Chen
An experimental study of PVTx properties in the gas phase for binary mixtures of HFC-161 and HFC-32
Fluid Phase Equilib.Year: 2006Volume: 243Pages: 156-160.
Keywords: Gas phase, PVTx properties, Equation of state, HFC-161/32 mixtures
DOI: 10.1016/j.fluid.2006.03.003
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.03.003.xml
Q. Chen, R.-h. Hong and G.-m. Chen
PVTx properties in the gas phase for binary HFC-161/125 system
Fluid Phase Equilib.Year: 2006Volume: 240Pages: 63-66.
Keywords: PVTx properties, Mixture, Equation of state, HFC-161/125
DOI: 10.1016/j.fluid.2005.12.005
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2005.12.005.xml
Chen, Q., Hong, R. H., Chen, G. M.
Gaseous PVT properties of ethyl fluoride
Fluid Phase Equilib.Year: 2005Volume: 237Pages: 111-116.
Keywords: PVT properties, Vapor pressure, Equation of state, HFC-161
DOI: 10.1016/j.fluid.2005.08.011
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2005.08.011.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: 2006Volume: 245Pages: 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
Q. Chen, R.-h. Hong and G.-m. Chen
Measurements of gas phase PVTx properties for the ternary HFC-161/125/32 system
Fluid Phase Equilib.Year: 2006Volume: 249Pages: 92-96.
Keywords: Gas phase, PVTx property, Virial equation, HFC-161/125/32 mixture
DOI: 10.1016/j.fluid.2006.09.008
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.09.008.xml
R.-h. Hong, Q. Chen and G.-m. Chen
Gas phase PVTx properties for binary mixtures of HFC-161 and HFC-143a
Fluid Phase Equilib.Year: 2007Volume: 259Pages: 153-156.
Keywords: Gas phase, PVTx properties, Equation of state, HFC-161/143a mixtures
DOI: 10.1016/j.fluid.2007.06.022
ThermoML: http://trc.nist.gov/ThermoML/fpe/j.fluid.2007.06.022.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. DataYear: 2008Volume: 53Pages: 2193-2196.
DOI: 10.1021/je800505y
ThermoML: http://trc.nist.gov/journals/jced/2008v53/i09/je800505y.xml
Shiflett, M. B.[Mark B.], Yokozeki, A.
Vapor-Liquid-Liquid Equilibria of Hydrofluorocarbons + 1-Butyl-3-methylimidazolium Hexafluorophosphate
J. Chem. Eng. DataYear: 2006Volume: 51Pages: 1931-1939.
DOI: 10.1021/je060275f
ThermoML: http://trc.nist.gov/journals/jced/2006v51/i05/je060275f.xml
Han, X. H., Chen, G. M., Li, C. S., Qiao, X. G., Cui, X. L., Wang, Q.
Isothermal Vapor-Liquid Equilibrium of (Pentafluoroethane + Fluoroethane) at Temperatures between (265.15 and 303.15) K Obtained with a Recirculating Still
J.Chem.Eng.DataYear: 2006Volume: 51Pages: 1232-1235.
DOI: 10.1021/je050539i
ThermoML: http://trc.nist.gov/journals/jced/2006v51/i04/je050539i.xml
Q. Chen, R.-h. Hong and G.-m. Chen
Vapor Pressure Measurements of Ethyl Fluoride
J. Chem. Eng. DataYear: 2005Volume: 50Pages: 1586-1588.
Keywords: vapor pressure
DOI: 10.1021/je050054u
ThermoML: http://trc.nist.gov/journals/jced/2005v50/i05/je050054u.xml
Q. Wang, Z. J. Gao, Y. J. Xu, X. H. Han and G. M. Chen
Isothermal Vapor-Liquid Equilibrium Data for the Binary Mixture Trifluoroethane (HFC-143a) + Ethyl Fluoride (HFC-161) over the Temperature Range (253.15 to 303.15) K
J. Chem. Eng. DataYear: 2010Volume: 55Pages: 2990-2993.
DOI: 10.1021/je100160d
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je100160d.xml
X. Dong, M. Gong, J. Liu and J. Wu
Vapor-Liquid Equilibria for 1,1,2,2-Tetrafluoroethane (R134) + Fluoroethane (R161) at Temperatures between (263.15 and 288.15) K
J. Chem. Eng. DataYear: 2010Volume: 55Pages: 3383-3386.
DOI: 10.1021/je100143k
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je100143k.xml
X. H. Han, Y. J. Xu, X. W. Min, Z. J. Gao, Q. Wang and G. M. Chen
Density Data for the Refrigerant Ethyl Fluoride (HFC-161) over a Temperature Range from (230 to 344) K
J. Chem. Eng. DataYear: 2011Volume: 56Pages: 3038-3042.
DOI: 10.1021/je2000827
ThermoML: http://trc.nist.gov/ThermoML/10.1021/je2000827.xml


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