Publicaciones en las que colabora con JORGE GARCIA CANO (14)

2020

  1. Liquid-liquid, vapor-liquid and vapor-liquid-liquid experimental equilibrium of the system water + 1-butanol + 2-butanol at 101.3 kPa and data correlation

    Fluid Phase Equilibria, Vol. 517

  2. Use of Ultrasound in the Determination of Isobaric LLV, SLV, and SLLV Equilibrium Data. Application to the Determination of the Water + Na2SO4or K2SO4+ 2-Methylpropan-2-ol Systems at 101.3 kPa and Boiling Conditions

    Journal of Chemical and Engineering Data, Vol. 65, Núm. 7, pp. 3287-3296

2018

  1. Consistency of experimental data in SLLV equilibrium of ternary systems with electrolyte. Application to the water + NaCl + 2-propanol system at 101.3 kPa

    Journal of Chemical Thermodynamics, Vol. 124, pp. 79-89

  2. Experimental study of the LL, VL and VLL equilibria of water + 1-butanol + 2-octanol at 101.3 kPa

    Fluid Phase Equilibria, Vol. 475, pp. 111-117

  3. Phase equilibria of the water + 1-butanol + 2-pentanol ternary system at 101.3 kPa

    Journal of Chemical Thermodynamics, Vol. 123, pp. 38-45

  4. Study of the LLE, VLE, and VLLE of the Ternary System Water + 1-Butanol + Isoamyl Alcohol at 101.3 kPa

    Journal of Chemical and Engineering Data, Vol. 63, Núm. 10, pp. 3733-3743

2016

  1. Isobaric vapor-liquid-liquid-solid equilibrium of the water + NaCl + 1-butanol system at 101.3 kPa

    Journal of Chemical Thermodynamics, Vol. 100, pp. 53-59

2015

  1. Ethanol dehydration via azeotropic distillation with gasoline fraction mixtures as entrainers: A pilot-scale study with industrially produced bioethanol and naphta

    Fuel Processing Technology, Vol. 140, pp. 198-204

  2. Ethanol dehydration via azeotropic distillation with gasoline fractions as entrainers: A pilot-scale study of the manufacture of an ethanol-hydrocarbon fuel blend

    Fuel, Vol. 139, pp. 568-574

  3. Phase equilibria of the water+1-butanol+toluene ternary system at 101.3 kPa

    Fluid Phase Equilibria, Vol. 385, pp. 29-36

2014

  1. Isothermal (liquid + liquid) equilibrium data at T = 313.15 K and isobaric (vapor + liquid + liquid) equilibrium data at 101.3 kPa for the ternary system (water + 1-butanol + p-xylene)

    Journal of Chemical Thermodynamics, Vol. 79, pp. 242-247

2013

  1. CaSO4 solubility in water-ethanol mixtures in the presence of sodium chloride at 25°C. Application to a reverse osmosis process

    Fluid Phase Equilibria, Vol. 360, pp. 248-252

  2. Liquid-liquid, vapor-liquid, and vapor-liquid-liquid equilibrium data for the water- n-butanol-cyclohexane system at atmospheric pressure: Experimental determination and correlation

    Journal of Chemical and Engineering Data, Vol. 58, Núm. 12, pp. 3320-3326

2012

  1. LLE, VLE and VLLE data for the water-n-butanol-n-hexane system at atmospheric pressure

    Fluid Phase Equilibria, Vol. 316, pp. 135-140