Mixing behaviour of a mixture of equal amounts of substance of 1,1,1,2-tetrafluoroethane and 1,1-difluoroethane. II. Representation of thermal properties by equations of state

By Turk M.   Crone M.   Bier K.  

Journal of Chemical Thermodynamics, Vol. 29, Iss. 4, 1997-04 ,pp. : 369-383

Academic Press

Access to resources Recommend Favorite

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

Access to resources Recommend Favorite

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

Access to resources Recommend Favorite

High pressure phase equilibria in the system 1,1,1,2-tetrafluoroethane + heptylbenzene

By Poot W.   de Loos T.W.  

Fluid Phase Equilibria, Vol. 210, Iss. 1, 2003-07 ,pp. : 69-75

Elsevier

Access to resources Recommend Favorite

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

By Takagi T.   Sakura T.   Tsuji T.   Hongo M.  

Fluid Phase Equilibria, Vol. 162, Iss. 1, 1999-08 ,pp. : 171-179

Elsevier

Access to resources Recommend Favorite