Trabajos de seguimiento de la lapa ferruginosa Patella ferruginea Gmelin, 1791 en Andalucía en el marco de la Estrategia Nacional de Conservación de la especie

El gasterópodo marino Patella ferruginea se encuentra incluido en los Catálogos Español y Andaluz de Especies Amenazadas en la categoría “En peligro de extinción”. En 2008 fue aprobada la Estrategia de Conservación Nacional de la especie que establece la realización de un seguimiento de la población cada cuatro años. En Andalucía se ha realizado en 2010 el seguimiento de la especie empleando dos tipos de metodología: los “Controles de crecimiento”, mediante marcaje de ejemplares, y los “Censos exhaustivos” en “Tramos” de costa, para intentar detectar todos los individuos presentes. En el censo de 2010 se han muestreado unos 21 km de costa en 34 localidades, un 5% del litoral andaluz con presencia de la especie, lo que constituye un esfuerzo considerable, pero asumible para el control periódico de la misma. La densidad media detectada es muy baja, de 0,048 ind./m. El mayor número de individuos se encuentra en Cádiz y la población mejor estructurada en la isla de Alborán. Se estima que el tamaño actual de la población en Andalucía ronda los 1.800 ejemplares, lo que constituye un aumento con respecto a inventarios anteriores. Sin embargo, el contingente es muy reducido para garantizar la supervivencia de la especie. La categoría de protección propuesta por el Libro Rojo de los Invertebrados de Andalucía, “En peligro crítico” (MORENO y ARROYO, 2008), debe considerarse, por lo tanto, la más adecuada para la lapa ferruginosa siguiendo los criterios de valoración de la UICN (2001).

Correlation of the liquid–liquid equilibrium data for specific ternary systems with one or two partially miscible binary subsystems

This paper presents the results of a liquid–liquid equilibrium data correlation for 11 ternary systems which have not been previously fitted using the NRTL model or, when they have, the results presented in the literature are inconsistent with the experimental behavior of the system. These ternary systems include mixtures with one or two partially miscible pairs. During the correlation process, new restrictions were imposed on the values for the NRTL binary parameters to ensure correct prediction of the total or partial miscibility for the binary pairs involved. In addition, topological concepts related to the Gibbs stability test have been applied in order to validate the results in the whole range of compositions.

Modelling liquid–liquid equilibria for island type ternary systems

Closed miscibility gaps in ternary liquid mixtures, at constant temperature and pressure, are obtained if phase separations occur only in the ternary region, whilst all binary mixtures involved in the system are completely miscible. This type of behaviour, although not very frequent, has been observed for a certain number of systems. Nevertheless, we have found no information about the applicability of the common activity coefficient models, as NRTL and UNIQUAC, for these types of ternary systems. Moreover, any of the island type systems published in the most common liquid–liquid equilibrium data collections, are correlated with any model. In this paper, the applicability of the NRTL equation to model the LLE of island type systems is assessed using topological concepts related to the Gibbs stability test. A first attempt to correlate experimental LLE data for two island type ternary systems is also presented.

Pitfalls on computing liquid-liquid phase equilibria using the k-value method

Poster presented in the 11th Mediterranean Congress of Chemical Engineering, Barcelona, October 21-24, 2008.

Liquid–Liquid, Vapor–Liquid, and Vapor–Liquid–Liquid Equilibrium Data for the Water–n-Butanol–Cyclohexane System at Atmospheric Pressure: Experimental Determination and Correlation

The temperature and the composition of the vapor–liquid–liquid equilibrium (VLLE) and the vapor–liquid equilibrium (VLE) of a ternary mixture of water–n-butanol–cyclohexane were measured at atmospheric pressure (101.32 kPa) in a modified dynamic recirculating still. As found in the literature, the experimental data obtained reveal a ternary azeotrope at 341.86 K with a mole fraction composition of 0.281, 0.034, and 0.685 water, n-butanol, and cyclohexane, respectively. The liquid–liquid equilibrium (LLE) compositions were measured at a constant temperature of 313.15 K and compared with data in the literature collected at other temperatures. Thermodynamic consistency of all the experimental data was demonstrated. The universal quasichemical (UNIQUAC) and the nonrandom two-liquid (NRTL) thermodynamic models were used to correlate the VLE and LLE data, while the original universal functional (UNIFAC) model was used to compare the predicted data.

Gibbs Energy of Mixing Function: Topological Analysis in Azeotropic Systems

ESAT 2014. 27th European Symposium on Applied Thermodynamics, Eindhoven University of Technology, July 6-9, 2014.

Liquid–Liquid Equilibria of Water + Ethanol + 1-Butyl-3-methylimidazolium Bis(trifluoromethanesulfonyl)imide Ternary System: Measurements and Correlation at Different Temperatures

In this work authors present the experimental liquid–liquid equilibria (LLE) data of water + ethanol + 1-butyl-3-methylimidazolium bis(trifluoromethanesulfonyl)imide ([bmim][Tf2N]) system at different temperatures. The LLE of the system was obtained in the temperature range from 283.2 to 323.2 K. The nonrandom two liquid (NRTL) and universal quasichemical (UNIQUAC) models were used to correlate ternary systems. The equilibrium compositions were successfully correlated by the interaction parameters from both models, however UNIQUAC gave a more accurate correlation. Finally, a study about the solvent capability of ionic liquid was made in order to evaluate the possibility of separating the mixture formed by ethanol and water using that ionic liquid.