Viscosity of gaseous mixtures of HFC-125 (pentafluoroethane) + HFC-134a (1,1,1,2-tetrafluoroethane) under pressure

By Yokoyama C.   Nishino T.   Takahashi M.  

Fluid Phase Equilibria, Vol. 174, Iss. 1, 2000-09 ,pp. : 231-240

Elsevier

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Thermodynamic properties of 1,1,1,2-tetrafluoroethane + polyether mixtures up to 60 MPa

By Comuñas M J.   Boned C   Baylaucq A   López E R   Fernández J  

Canadian Journal of Chemistry, Vol. 82, Iss. 8, 2004-08 ,pp. : 1271-1279

NRC Research Press

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Phase equilibria of 1,1,1-trifluoroethane (HFC-143a) + 1,1,1,2-tetrafluoroethane (HFC-134a), and + 1,1-difluoroethane (HFC-152a) at 273.15, 293.15, 303.15, and 313.15 K

By Lim J.S.   Park J.-Y.   Lee B.-G.   Lee Y.-W.  

Fluid Phase Equilibria, Vol. 193, Iss. 1, 2002-01 ,pp. : 29-39

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A facile synthetic method for 2-fluoroindolizines from 1-chloro-2,2,2-trifluoroethane (HCFC-133a) and 1,1,1,2-tetrafluoroethane (HFC-134a)

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Journal of Fluorine Chemistry, Vol. 122, Iss. 2, 2003-08 ,pp. : 171-174

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Vapor-liquid equilibria for carbon dioxide + 1,1,1,2-tetrafluoroethane (R-134a) systems at temperatures from 329 to 354 K and pressures upto 7.37 MPa

By Silva-Oliver G.   Galicia-Luna L.A.  

Fluid Phase Equilibria, Vol. 199, Iss. 1, 2002-06 ,pp. : 213-222

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