11. José Aguado, María D. Romero, Araceli Rodríguez, José R. Ferrer, and Luis M. Marugán - J. Chem. Eng. Data, 1996, 41 (3), pp 440–442
Isobaric Vapor−Liquid Equilibria at 6.67 kPa for 1-Octene + 2-Butyl Propenoate
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http://dx.doi.org/10.1021/je950258iIsobaric Vapor−Liquid Equilibria at 6.67 kPa for 1-Octene + Propenoic Acid and 2-Butyl Propenoate + Propenoic Acid
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http://dx.doi.org/10.1021/je9601772Код: Выделить всё
http://dx.doi.org/10.1021/je034162xSolubility of Hydrogen, Carbon Monoxide, and 1-Octene in Various Solvents and Solvent Mixtures
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http://dx.doi.org/10.1021/je960024eBinary vapor-liquid equilibria of carbon dioxide with 2-methyl-1-pentene, 1-hexene, 1-heptene, and m-xylene at 303.15, 323.15, and 343.15 K
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http://dx.doi.org/10.1021/je00037a012Phase Equilibria of the Binary Systems 1-Hexene with o-Xylene, m-Xylene, p-Xylene, Toluene, and Ethylbenzene at 101.3 kPa
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http://dx.doi.org/10.1021/je010295bMeasurement of Activity Coefficients at Infinite Dilution Using Gas−Liquid Chromatography. 12. Results for Various Solutes with the Stationary fe6 Phases N-Ethylacetamide, N,N-Diethylacetamide, Diethylphthalate, and Glutaronitrile
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http://dx.doi.org/10.1021/je0000726Thermodynamics of Fuels with a Biosynthetic Component. II. Vapor–Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, 1-Hexene, and Cyclohexane at T = 313.15 K
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http://dx.doi.org/10.1021/je7005488Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor−Liquid Equilibrium of the Ternary Mixtures Methyl tert-Butyl Ether + Heptane + Benzene and Methyl tert-Butyl Ether + Benzene + 1-Hexene at 313.15 K
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http://dx.doi.org/10.1021/je980107qVapor−Liquid Equilibrium of Ternary Mixtures Containing Methyl tert-Butyl Ether and/or Substitution Hydrocarbons. Methyl tert-Butyl Ether + Heptane + Cyclohexane and Methyl tert-Butyl Ether + Cyclohexane + 1-Hexene at 313.15 K
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http://dx.doi.org/10.1021/je980108iPhase equilibriums in the n-pentane + pent-1-ene system. 1. Critical states
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http://dx.doi.org/10.1021/je00033a010