Abstract

Alcohols/hydrocarbons blends represent important products in the industry and remarkable systems from the thermodynamic standpoint, especially in presence of traces of water. In automotive applications, ethanol is incorporated in increasing proportions into car fuel formulations for environmental and economic reasons. From a thermodynamic viewpoint, the strongly polar nature of ethanol versus the rather apolar character of hydrocarbons makes the study of such blends particularly interesting in terms of vapor pressure and miscibility behavior. A long term collaboration between GE EnergyEurope (Belfort, France) and the Thermodynamics Team of the LRGP laboratory (Nancy, France) has been conducted to improve the knowledge of these systems, using the UNIFAC thermodynamic theory. First, blends of anhydrous ethanol and naphtha class hydrocarbons have been studied in terms of volatility: a strong liquid/vapor non-ideality effect has been put in evidence and numerically characterized. In a further step, blends of hydrated ethanol and hydrocarbons featuring diverse compositions have been the matter of a thermodynamic modeling that confirmed the paramount role played by the moisture content of ethanol on the miscibility, using the Maximum Miscibility Temperature (“TMM”) concept; this study also pointed out the non-negligible influence of the PONA data and sulfur species of the hydrocarbon cut. Later on, other alcohols namely methanol, isopropanol and n-butanol, that may play an important role in future “green fuel” formulations, were included in this study that showed an interesting chain length effect. Recently, the team has started a study of the effect of biodiesel additions on the TMM of hydrated alcoholhydrocarbon mixtures. This paper summarizes the methodology and the results of the multi-step, collaborative modeling study developed in the field of ethanol/hydrocarbon thermodynamics.

Highlights

  • In recent years, the quest for sustainable primary energies has increased the potential interest of biogenic/fossil fuels mixes

  • This figure demonstrates the highly non-ideal behavior of these blends: for instance, for a blend containing 17% ethanol, a calculation assuming an ideal behaviour (Raoult’s law) would lead to undervalue the vapour pressure by 51%. These results are very important from a safety standpoint since the Lower and Upper Flammability Limits depend on the vapour pressure; they are relevant for the selection of the right naphtha cuts when one wishes to prepare ethanol/gasolines blends having suitable volatility for cars (e.g. “E10”)

  • One observes that: - the Miscibility Temperature (MMT) systematically increases with the proportion of water in the alcohol - the heavier the alcohol, the stronger this increase; when the water percent goes from 1 to 10 %, the MMT is multiplied by: 1.3 for the methanol; 2.1 for the ethanol; 2.7 for the isopropanol and for 1butanol

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Summary

Vapor pressure of ethanol-naphtha blends

The theoretical approach is based on the 1978 version of the Peng and Robinson equation of state [1], noted “PR78” in this paper.

Introduction
Alcohol-gasoil miscibility study
General aspects
Outlines of the UNIFAC method
Liquid-liquid phase diagrams for multicomponent systems
Direct calculation of the saturation curve
Flash calculation
Addition of four different industrial alcohols in gasoil GO1
Addition of four different industrial alcohols in gasoil GO2
Addition of four different industrial alcohols in gasoil GO3
Addition of different industrial alcohols in gasoil GO4
Findings
Conclusion
Full Text
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