Solid-liquid phase equilibria in binary (benzene, cyclohexane + n-tetradecane, n-hexadecane) systems at temperatures 230-323 K and pressures up to 120 MPa

By Tanaka Y.   Kawakami M.  

Fluid Phase Equilibria, Vol. 125, Iss. 1, 1996-10 ,pp. : 103-114

Elsevier

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Vapor-liquid equilibria for the ternary system benzene+n-heptane+N,N-dimethylformamide at 101.33 kPa

By Blanco B.   Sanz M.T.   Beltran S.   Cabezas J.L.   Coca J.  

Fluid Phase Equilibria, Vol. 175, Iss. 1, 2000-10 ,pp. : 117-124

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The Bancroft point and vapor-liquid equilibria in the system benzene + isopropanol

By Elliott J.R.   Rainwater J.C.  

Fluid Phase Equilibria, Vol. 175, Iss. 1, 2000-10 ,pp. : 229-236

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Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 1. Total pressure data and g E for binary and ternary mixtures containing di-isopropyl ether (DIPE), n-heptane and benzene at 313.15 K

By Chamorro C.R.   Segovia J.J.   Martn M.C.   Villamanan M.A.  

Fluid Phase Equilibria, Vol. 182, Iss. 1, 2001-06 ,pp. : 229-239

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Vapor-liquid equilibria of the binary mixtures of tetrahydrofuran with 2,2,4-trimethylpentane, methylcyclohexane and n-heptane at 101.3 kPa

By Du T.-B.   Tang M.   Chen Y.-P.  

Fluid Phase Equilibria, Vol. 192, Iss. 1, 2001-12 ,pp. : 71-83

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