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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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High-pressure vapor-liquid equilibrium of binary systems with R236fa

By Bobbo S.   Camporese R.   Stryjek R.  

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