Vapor-liquid equilibria and critical points for the carbon dioxide +1-pentanol and carbon dioxide +2-pentanol systems at temperatures from 332 to 432 K

By Silva-Oliver G.   Galicia-Luna L.A.   Sandler S.I.  

Fluid Phase Equilibria, Vol. 200, Iss. 1, 2002-07 ,pp. : 161-172

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

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Vapour-liquid equilibrium in the carbon dioxide-ethyl propanoate system at pressures from 2 to 9 MPa and temperatures from 303 to 323 K

By Wagner Z.  

Fluid Phase Equilibria, Vol. 112, Iss. 1, 1995-11 ,pp. : 125-129

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High pressure vapor-liquid and vapor-liquid-liquid equilibria for systems containing supercritical carbon dioxide, water and furfural

By Sako T.   Sugeta T.   Nakazawa N.   Otake K.   Sato M.   Ishihara K.   Kato M.  

Fluid Phase Equilibria, Vol. 108, Iss. 1, 1995-07 ,pp. : 293-303

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Corrigendum to ''Solubility of carbon dioxide in aqueous solutions containing sodium acetate or ammonium acetate at temperatures from 313 to 433 K and pressures up to 10 MPa'' [Fluid Phase Equilibria 155 (1999) 107-125]

By Xia J.   Rumpf B.   Maurer G.  

Fluid Phase Equilibria, Vol. 168, Iss. 2, 2000-02 ,pp. : 283-284

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