EDUARDO ATANASIO
MONTERO GARCIA
Investigador en el període 1988-1994
Publicacions en què col·labora amb EDUARDO ATANASIO MONTERO GARCIA (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
2012
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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Erratum: Excess enthalpies of binary and ternary mixtures containing dibutyl ether, cyclohexane and 1-butanol at 298.15 K (Journal of Chemical and Engineering Data (2009) 54 (1672-1679)
Journal of Chemical and Engineering Data
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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
2006
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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
2003
2001
1999
1998
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Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons. 2. Total-pressure data and G(E) for methyl tert-butyl ether/n-heptane/1-hexene at 313.15 K
Fluid Phase Equilibria, Vol. 152, Núm. 2, pp. 265-276
1997
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Isothermal vapor-liquid equilibria of binary mixtures containing methyl tert-butyl ether (MTBE) and/or substitution hydrocarbons
Fluid Phase Equilibria, Vol. 133, Núm. 1-2, pp. 155-162