TERMOCAL
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Universidad de Burgos
Burgos, EspañaPublicaciones en colaboración con investigadores/as de Universidad de Burgos (21)
2017
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High Pressure Volumetric Properties of the Binary Mixtures Di-isopropyl Ether + 2,2,4-Trimethylpentane
Journal of Chemical and Engineering Data, Vol. 62, Núm. 10, pp. 3610-3619
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High pressure liquid densities and excess volumes of the (di-isopropyl ether + 1-hexanol) system
Journal of Chemical Thermodynamics, Vol. 113, pp. 213-218
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PVT properties of the binary system di-isopropyl ether + iso-octane for the development of new biofuels
30th International Conference on Efficiency, Cost, Optimization, Simulation and Environmental Impact of Energy Systems, ECOS 2017
2013
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Excess enthalpies of ternary mixtures of oxygenated additives + hydrocarbon mixtures in fuels and bio-fuels: Dibutyl ether (DBE) and 1-butanol and 1-hexene or cyclohexane or 2,2,4 trimethylpentane at 298.15 K and 313.15 K
Journal of Chemical Thermodynamics, Vol. 56, pp. 6-11
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Vapour-liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol with 2,2,4-trimethylpentane or n-heptane
Fluid Phase Equilibria, Vol. 338, pp. 95-99
2012
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Ether+alcohol+hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K
Fluid Phase Equilibria, Vol. 315, pp. 1-8
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Phase equilibrium properties of the ternary mixture dibutyl ether+toluene+heptane at 313.15K
Fluid Phase Equilibria, Vol. 317, pp. 84-88
2011
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Reply to "comment on 'excess enthalpies of binary and ternary mixtures containing dibutyl ether, cyclohexane, and 1-butanol at 298.15 K'"
Journal of Chemical and Engineering Data
2010
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Excess enthalpies of binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol, and heptane at T = 298.15 K and 313.15 K
Journal of Chemical Thermodynamics, Vol. 42, Núm. 1, pp. 28-37
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Excess enthalpies of oxygenated compounds + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and 2,2,4-trimethylpentane at 298.15 K
Fluid Phase Equilibria, Vol. 290, Núm. 1-2, pp. 15-20
2009
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Excess enthalpies of binary and ternary mixtures containing dibutyl ether, cyclohexane, and 1-butanol at 298.15 K
Journal of Chemical and Engineering Data, Vol. 54, Núm. 6, pp. 1672-1679
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Excess enthalpies of ether + alcohol + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and benzene at 298.15 K and 313.15 K
Fluid Phase Equilibria, Vol. 284, Núm. 2, pp. 106-113
2008
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Phase equilibrium properties of binary and ternary mixtures containing dibutyl ether, cyclohexane, and heptane or 1-hexene at T = 313.15 K
Journal of Chemical and Engineering Data, Vol. 53, Núm. 7, pp. 1486-1491
2006
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Experimental investigation of the vapour-liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15 K
Fluid Phase Equilibria, Vol. 245, Núm. 1, pp. 57-62
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Phase equilibrium properties of binary and ternary mixtures containing 1,1-dimethylethyl methyl ether, 1-propanol, and hexane at T = 313.15 K
Journal of Chemical and Engineering Data, Vol. 51, Núm. 6, pp. 2121-2125
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Vapour-liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15 K
Fluid Phase Equilibria, Vol. 245, Núm. 1, pp. 52-56
2004
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Excess enthalpies of binary and ternary mixtures containing tert-amyl methyl ether (TAME), tert-amyl alcohol (TAOH) and hexane at 298.15 and 313.15 K
Fluid Phase Equilibria
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Vapor-liquid equilibrium of octane-enhancing additives in gasolines: 6. Total pressure data and GE for binary and ternary mixtures containing 1,1-dimethylethyl methyl ether (MTBE), methanol and n-hexane at 313.15 K
Fluid Phase Equilibria