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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Bubble point pressure for binary mixtures of difluoromethane with pentafluoroethane and 1,1,1,2-tetrafluoroethane

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

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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

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High-Pressure Fluid-Phase Equilibria: Experimental Methods and Systems Investigated (1988-1993)

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