Solubility of carbon dioxide in eicosane, docosane, tetracosane, and octacosane at temperatures from 323 to 473 K and pressures up to 40 MPa

By Sato Y.   Tagashira Y.   Maruyama D.   Takishima S.   Masuoka H.  

Fluid Phase Equilibria, Vol. 147, Iss. 1, 1998-06 ,pp. : 181-193

Elsevier

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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

Elsevier

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Vapor-liquid equilibrium data for the CO 2 + 1,1,1,2,3,3,3,-heptafluoropropane (R227ea) system at temperatures from 276.01 to 367.30 K and pressures up to 7.4 MPa

By Valtz A.   Coquelet C.   Baba-Ahmed A.   Richon D.  

Fluid Phase Equilibria, Vol. 207, Iss. 1, 2003-05 ,pp. : 53-67

Elsevier

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Isothermal vapour-liquid equilibrium data for the binary propan-2-one+chloroalkanes mixtures at temperatures from 298.15 K to 313.15 K

By Dragoescu D.   Barhala A.   Vilcu R.  

Fluid Phase Equilibria, Vol. 157, Iss. 1, 1999-03 ,pp. : 41-51

Elsevier

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Excess molar enthalpies of (carbon dioxide+ethylene glycol dimethyl ether or 2-methoxyethyl ether) at the temperatures 298.15 K and 308.15 K and pressures from 7.5 MPa to 12.5 MPa

By Zhao J.P.   Tremaine P.R.  

Journal of Chemical Thermodynamics, Vol. 28, Iss. 6, 1996-06 ,pp. : 577-587

Academic Press

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