Phase equilibrium properties of binary and ternary systems containing tert-amylmethyl ether (TAME) as oxygenate additive and gasoline substitution hydrocarbons at 313.15 K

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Vapour-liquid equilibrium of octane-enhancing additives in gasolines - 2. Total pressure data and g E for binary and ternary mixtures containing tert-amylmethyl ether (TAME), tert-amyl alcohol (TAOH) and n-hexane

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Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 5. Total pressure data and G E for binary and ternary mixtures containing 1,1-dimethylpropyl methyl ether (TAME), 1-propanol and n-hexane at 313.15 K

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Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 4. Total pressure data and G E for ternary mixtures containing isopropyl ether or benzene and n-heptane + 1-hexene at 313.15 K

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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

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