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Featured researches published by César R. Chamorro.


Fluid Phase Equilibria | 1997

Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons. 1. Total-pressure data and GE for methyl tert-butyl etherbenzenecyclohexane at 313.15 K

JoséJ. Segovia; Maria C. Martin; César R. Chamorro; Miguel A. Villamañán

Abstract Experimental isothermal P–x–y data for the ternary system (methyl tert-butyl ether (MTBE)+n-heptane+1-hexene) and for its corresponding binaries at 313.15 K are reported. Data reduction by Barkers method provides correlations for GE using the Margules equation for the binary systems, the Wohl expansion for the ternary system and Wilson, NRTL and UNIQUAC models for both binary and the ternary mixtures.


Fluid Phase Equilibria | 1999

Phase equilibrium properties of binary and ternary systems containing tert-amylmethyl ether (TAME) as oxygenate additive and gasoline substitution hydrocarbons at 313.15 K

César R. Chamorro; José J. Segovia; Maria C. Martin; Eduardo A. Montero; Miguel A. Villamañán

Abstract Experimental isothermal P – x – y data for the binary systems ( tert -amylmethyl ether (TAME)+the hydrocarbons n -heptane, cyclohexane, benzene and 1-hexene) and the ternary system ( tert -amylmethyl ether (TAME)+1-hexene+cyclohexane) at 313.15 K are reported. Data reduction by Barkers method provides correlations for G E using the Margules equation for the binary systems and the Wohl expansion for the ternary system. Wilson, NRTL and UNIQUAC models have been applied successfully to both the binary and the ternary systems presented here and they have been used for predicting the behaviour of the other ternary systems involving TAME+hydrocarbon+hydrocarbon, where the four types of substitution hydrocarbons have been used.


Fluid Phase Equilibria | 1999

Experimental investigation of the vapor–liquid equilibrium at 313.15 K of the ternary system tert-amylmethyl ether (TAME)+n-heptane+methanol

César R. Chamorro; José J. Segovia; Maria C. Martin; Miguel A. Villamañán

Abstract Experimental isothermal P–x data at 313.15 K for the ternary system (tert-amylmethyl ether (TAME)+n-heptane+methanol) and for one of the unmeasured constituent binary systems, (tert-amylmethyl ether (TAME)+methanol) are reported. Data reduction by Barkers method provides correlations for gE using the Margules equation for the binary systems and the Wohl expansion for the ternary system. Wilson, NRTL and UNIQUAC models have been applied successfully to both the binary and the ternary systems. The presence of azeotropes in the ternary system and constituent binaries are studied as well as the presence of immiscible zones.


Archive | 2017

Geothermal Power Technologies

Maria E. Mondejar; César R. Chamorro

Although geothermal energy has been widely deployed for direct use in locations with especial geologic manifestations, its potential for power generation has been traditionally underestimated. Recent technology developments in drilling techniques and power conversion technologies from low-temperature heat resources are bringing geothermal energy to the spotlight as a renewable baseload energy option for a sustainable energy mix. Although the environmental impact and economic viability of geothermal exploitation must be carefully evaluated for each case, the use of deep low-temperature geothermal reservoirs could soon become an important contributor to the energy generation around the world.


Energy | 2012

World geothermal power production status: Energy, environmental and economic study of high enthalpy technologies

César R. Chamorro; Maria E. Mondejar; Roberto Ramos; José J. Segovia; Maria C. Martin; Miguel A. Villamañán


Energy | 2006

Low-grade coal and biomass co-combustion on fluidized bed: exergy analysis

Carmen Martín; Miguel A. Villamañán; César R. Chamorro; Juan Otero; Andrés Cabanillas; José J. Segovia


Energy | 2014

Enhanced geothermal systems in Europe: An estimation and comparison of the technical and sustainable potentials

César R. Chamorro; José L. García-Cuesta; Maria E. Mondejar; Alfonso Pérez-Madrazo


Journal of Chemical & Engineering Data | 1998

Vapor−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†

José J. Segovia; Maria C. Martin; César R. Chamorro; Miguel A. Villamañán


Fluid Phase Equilibria | 1998

Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons

José J. Segovia; Maria C. Martin; César R. Chamorro; Eduardo A. Montero; Miguel A. Villamañán


Fluid Phase Equilibria | 2004

Characterization and modelling of a gasoline containing 1,1-dimethylethyl methyl ether (MTBE), diisopropyl ether (DIPE) or 1,1-dimethylpropyl methyl ether (TAME) as fuel oxygenate based on new isothermal binary vapour–liquid data

César R. Chamorro; Maria C. Martin; Miguel A. Villamañán; José J. Segovia

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M.C. Martín

University of Valladolid

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