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

Elsevier

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Viscosity measurements and correlations for 1,1,1,2-tetrafluoroethane (HFC-134a) up to 140 MPa

By Comunas M.J.P.   Baylaucq A.   Quinones-Cisneros S.E.   Zeberg-Mikkelssen C.K.   Boned C.   Fernandez J.  

Fluid Phase Equilibria, Vol. 210, Iss. 1, 2003-07 ,pp. : 21-32

Elsevier

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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

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Desorption Behaviour of HF,HCFC-133a and HFC-134a on a Catalyst Supported on γ-AlF₃

By Quan H.   Ge Z.   Li Z.   Yin C.   Zhong K.   Hao Z.   Li H.   Ji F.  

Journal of Thermal Analysis and Calorimetry, Vol. 55, Iss. 1, 1999-01 ,pp. : 213-220

Springer Publishing Company

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Sodium dithionite initiated reactions of 1-bromo-1-chloro-2,2,2-trifluoroethane with enol ethers of cyclic ketones

By Dmowski W.   Ignatowska J.  

Journal of Fluorine Chemistry, Vol. 123, Iss. 1, 2003-09 ,pp. : 37-42

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