Dehydration for a solid coordination network based on CuII-(py)2C(OH)2 trimers

Abstract de congreso: Póster presentado en 12th International Conference on Materials Chemistry (MC12), 20 - 23 July 2015, York, United Kingdom

Modelos de empresa multinacional democrática o cooperativa

[ES] En este trabajo analizamos las posibles vías de desarrollar otro modelo de empresa multinacional desde tres puntos de vista. En primer lugar, analizaremos el papel que pueden desempeñar los códigos de conducta como instrumentos complementarios para diseñar una política social internacional. En segundo lugar, realizamos una breve reflexión sobre la cooperativa multinacional, o la cooperativa global, como alternativa cooperativa al modelo de empresa multinacional imperante. Por último, en tercer lugar, desde un punto de vista más amplio, nos referimos a las posibilidades de desarrollar un modelo de empresa multinacional más democrática. En este sentido, estudiamos algunos condicionantes que afectan al funcionamiento y a los procesos de decisión de las empresas multinacionales, en concreto nos referimos a los mecanismos de coordinación entre las diferentes unidades de la estructura multinacional y a las características de las filiales, en cuanto a su fortaleza o calidad.

La fiscalidad de las cooperativas. Un modelo que fortalece los fondos propios

[ES] Las cooperativas son un modelo de empresa que tiene unas características particulares, entre las que destacan la distribución y el ejercicio del poder, la manera particular de distribución de resultados, la existencia de unos fondos obligatorios, la autoregulación del régimen de trabajo, el procedimiento de atribución de fondos económicos en el momento de la baja de un socio, y la participación de los asalariados en los resultados económicos positivos.

Sociedades Cooperativas. Aspectos Contables Singulares

[ES] Las sociedades cooperativas han visto recientemente reforzada su normativa contable con la aprobación de la ORDEN ECO/3614/2003 que tiene por objeto la adaptación de las Normas de valoración y elaboración de cuentas anuales aprobada en el Plan General de Contabilidad a las características de estas entidades.

Las sociedades cooperativas de vivienda. Especial referencia al País Vasco

[ES] Son muy diversos los sectores en los que ejercen su actividad las sociedades cooperativas. La sociedad cooperativa de viviendas es una clase específica de dentro de las de consumidores, regulada como una «clase» diferenciada en las leyes, que presenta particularidades que es preciso conocer. Constituyen entidades con un lugar propio dentro del sector inmobiliario con una nada despreciable contribución a la promoción de vivienda. En el País Vasco son en cuantía las más importantes después de las de trabajo asociado. La sociedad cooperativa de viviendas se caracteriza como empresa de participación dentro del sector inmobiliario, en la medida que son los propios usuarios de las viviendas los responsables de la toma de decisiones en la promoción inmobiliaria.

Los Modelos Implícitos de Valoración de Opciones

[ES] Los modelos implícitos constituyen uno de los enfoques de valoración de opciones alternativos al modelo de Black-Scholes que ha conocido un mayor desarrollo en los últimos años. Dentro de este planteamiento existen diferentes alternativas: los árboles implícitos, los modelos con función de volatilidad determinista y los modelos con función de volatilidad implícita. Todos ellos se construyen a partir de una estimación de la distribución de probabilidades riesgo-neutral del precio futuro del activo subyacente, congruente con los precios de mercado de las opciones negociadas. En consecuencia, los modelos implícitos proporcionan buenos resultados en la valoración de opciones dentro de la muestra. Sin embargo, su comportamiento como instrumento de predicción para opciones fuera de muestra no resulta satisfactorio. En este artículo se analiza la medida en la que este enfoque contribuye a la mejora de la valoración de opciones, tanto desde un punto de vista teórico como práctico.

Evaluación del proyecto de Madrid 2012 bajo un enfoque de mercado. Una exploración de posibilidades y mejoras

[ES] Desde que el 24 de abril de 1966 Madrid perdiera frente a Munich la votación para ser elegida como ciudad organizadora de los Juegos Olímpicos de 1972, la ciudad nunca había estado tan cerca de la organización de unas Olimpiadas.

La gestión del conocimiento en la gestión pública. Compartir, cooperar y competir

Hasta no hace demasiado tiempo se ha entendido que la gestión de la cosa pública era diferente a la de la empresa privada y que, por tanto, las teorías y técnicas que se aplicaban en ésta nada tenían que ver con aquélla. Sin embargo, de un tiempo a esta parte, empiezan a verse señales que apuntan al lado contrario. Al parecer, en la gestión pública, también hay consumidores de servicios (en este mercado se les llama ciudadanos), y también existe la competencia: ciudades, regiones o naciones que compiten por ofrecer mejores servicios a sus consumidores-ciudadanos, o que compiten para conseguir más localizaciones de empresas en su territorio, o para atraer más eventos, o más turistas, sean estos de ocio o de negocios.

Los inicios de la vascología en Holanda: El Essai de grammaire de la langue basque de Willem J. van Eys (1865, 1867)

Ed. by Xabier Artiagoitia, Patxi Goenaga & Joseba A. Lakarra.

X Seminario sobre Aspectos Jurídicos de la Gestión Universitaria

Índice: Bloque I (coordinadora: María Isabel Bonachera Ledro): - A. Evolución histórica del doctorado (Daniel Pastor Javaloyes). - B. Análisis de las principales novedades del RD 99/2011, de 28 de enero, por el que se regulan las enseñanzas oficiales de Doctorado (Araceli García Sánchez). - C. Análisis de la adaptación normativa en materia de estudios de Doctorado llevada a cabo por las universidades tras el Real Decreto 99/2011, de 28 de enero (Amaya Rosa Ruiz-Alejos). - D. Las escuelas de Doctorado. Nueva estructura de soporte de los estudios de doctorado (María Isabel Bonachera Ledro). - E. Aproximación a la organización de los estudios de Doctorado en el entorno EEES (Manuel Fabián Martín-Arroyo). - Anexo I. Reglamento de régimen interno de la Escuela de Doctorado de la Universidad de Cantabria (EDUC). Bloque II. Educación y formación superior: puntos de encuentro (coordinadora: Ana I. Caro Muñoz): - 1. Encuadre normativo de la correspondencia de enseñanzas: educación superior, formación profesional y enseñanzas artísticas superiores (Elena de la Fuente García). - 2. Convergencias en la consecución del EEES, el EEI y el Proceso de Copenhague (José Plana Plana). - 3. Realidades y perspectivas de los entornos de formación superior (Juan Cayón Peña). - 4. Análisis de una experiencia: universidad privada y formación profesional (Fernando Lostao Crespo). - 5. Diseño y evaluación de competencias: definición, clasificación y perfiles competenciales (David Martínez Victorio). - 6. Envejecimiento activo: educación a lo largo de la vida (Ana I. Caro Muñoz). Bloque III. La gestión de recursos humanos en las universidades y sus implicaciones jurídicas (coordinador: Fernando Palencia Herrejón): - Introducción (Fernando Palencia Herrejón). - 1. Incidencia de los Decretos leyes 20/2011 y 3/2012 en la gestión de personal de las universidades (Beatriz Vozmediano Ares). - 2. Tres aspectos de la aplicación del EBEP a las universidades (Elena Martínez Nieto). - 3. El régimen jurídico del personal directivo profesional (Juan Eduardo González González). - 4. Sobre la negociación colectiva (María de Rivera Parga). 5. La evaluación del desempeño (Jesús Lobato de Ruiloba). 6. El desarrollo legislativo del EBEP en las Comunidades Autónomas (M.ª Mercedes Sánchez Castillo). Bloque IV. Propiedad intelectual e industrial: desafíos (coordinador: Emiliano Garmendia Ferrer): - 1. Propiedad intelectual, propiedad industrial, conocimiento y su protección: - 1.1. Notas sobre la propiedad intelectual, la propiedad industrial, el conocimiento científico y su protección (Emiliano Garmendia Ferrer). - 1.2. Normativa específica de protección de determinadas invenciones (Elena Meaños Melón). - 1.3. La gestión colectiva en el sector del libro: entidades de gestión colectiva de derechos de autor y las universidades (Miguel Ángel Davara F. de Marcos). - 2. Algunas producciones en el ámbito universitario: - 2.1. La actividad del Personal de Administración y Servicios: programas de ordenador y bases de datos (Soledad Béthencourt Zamora). - 2.2. Tesis Doctorales y Propiedad Intelectual (Isabel-Cecilia del Castillo). - 3. Ejemplos a partir de las nuevas tecnologías: - 3.1. El e-book. Implicaciones jurídicas para las universidades de un nuevo modelo de aprendizaje (Soledad Béthencourt Zamora). - 3.2. La difusión de obras de la propiedad intelectual» Susana Martínez Fernández). - 4. Los Agentes de la creación del conocimiento en la Universidad: - 4.1. Los agentes universitarios de la creación del conocimiento (Elena Meaños Melón). - 4.2. La incidencia de la Ley de Economía Sostenible y de la Ley de la Ciencia en el tratamiento de autor en las universidades públicas (Jerónimo D. Reynés Vives). - 5. La transferencia de los resultados de la investigación: - 5.1. El tratamiento de la transferencia en las Leyes de Economía Sostenible y de la Ciencia (Carlos A. Gómez Otero). - 5.2. La transferencia inversa (Javier Such Martínez). - 5.3. Naturaleza jurídica de los negocios relativos a la propiedad intelectual e industrial. La problemática de los sistemas de adjudicación al amparo de la Ley de Economía Sostenible y de la Ley de la Ciencia, la Tecnología y la Innovación (Carlos A. Gómez Otero). - 5.4. La valorización y gestión de la transferencia. El caso UNIVALUE (Jerónimo D. Reynés Vives). - Ponencia final: La reforma laboral de 2012. RDL 3/2012, de 10 de febrero, de medidas urgentes para la reforma del mercado laboral (Garbiñe Biurrun Mancisidor). - Comunicación: El nuevo marco normativo de las prácticas académicas externas de los estudiantes universitarios (Josep Moreno Gené).

Advanced Reaction Systems for Hydrogen Production

[EN] This PhD work started in March 2010 with the support of the University of the Basque Country (UPV/EHU) under the program named “Formación de Personal Investigador” at the Chemical and Environmental Engineering Department in the Faculty of Engineering of Bilbao. The major part of the Thesis work was carried out in the mentioned department, as a member of the Sustainable Process Engineering (SuPrEn) research group. In addition, this PhD Thesis includes the research work developed during a period of 6 months at the Institut für Mikrotechnik Mainz GmbH, IMM, in Germany. During the four years of the Thesis, conventional and microreactor systems were tested for several feedstocks renewable and non-renewable, gases and liquids through several reforming processes in order to produce hydrogen. For this purpose, new catalytic formulations which showed high activity, selectivity and stability were design. As a consequence, the PhD work performed allowed the publication of seven scientific articles in peer-reviewed journals. This PhD Thesis is divided into the following six chapters described below. The opportunity of this work is established on the basis of the transition period needed for moving from a petroleum based energy system to a renewable based new one. Consequently, the present global energy scenario was detailed in Chapter 1, and the role of hydrogen as a real alternative in the future energy system was justified based on several outlooks. Therefore, renewable and non-renewable hydrogen production routes were presented, explaining the corresponding benefits and drawbacks. Then, the raw materials used in this Thesis work were described and the most important issues regarding the processes and the characteristics of the catalytic formulations were explained. The introduction chapter finishes by introducing the concepts of decentralized production and process intensification with the use of microreactors. In addition, a small description of these innovative reaction systems and the benefits that entailed their use were also mentioned. In Chapter 2 the main objectives of this Thesis work are summarized. The development of advanced reaction systems for hydrogen rich mixtures production is the main objective. In addition, the use and comparison between two different reaction systems, (fixed bed reactor (FBR) and microreactor), the processing of renewable raw materials, the development of new, active, selective and stable catalytic formulations, and the optimization of the operating conditions were also established as additional partial objectives. Methane and natural gas (NG) steam reforming experimental results obtained when operated with microreactor and FBR systems are presented in Chapter 3. For these experiments nickel-based (Ni/Al2O3 and Ni/MgO) and noble metal-based (Pd/Al2O3 and Pt/Al2O3) catalysts were prepared by wet impregnation and their catalytic activity was measured at several temperatures, from 973 to 1073 K, different S/C ratios, from 1.0 to 2.0, and atmospheric pressure. The Weight Hourly Space Velocity (WHSV) was maintained constant in order to compare the catalytic activity in both reaction systems. The results obtained showed a better performance of the catalysts operating in microreactors. The Ni/MgO catalyst reached the highest hydrogen production yield at 1073 K and steam-to-carbon ratio (S/C) of 1.5 under Steam methane Reforming (SMR) conditions. In addition, this catalyst also showed good activity and stability under NG reforming at S/C=1.0 and 2.0. The Ni/Al2O3 catalyst also showed high activity and good stability and it was the catalyst reaching the highest methane conversion (72.9 %) and H2out/CH4in ratio (2.4) under SMR conditions at 1073 K and S/C=1.0. However, this catalyst suffered from deactivation when it was tested under NG reforming conditions. Regarding the activity measurements carried out with the noble metal-based catalysts in the microreactor systems, they suffered a very quick deactivation, probably because of the effects attributed to carbon deposition, which was detected by Scanning Electron Microscope (SEM). When the FBR was used no catalytic activity was measured with the catalysts under investigation, probably because they were operated at the same WHSV than the microreactors and these WHSVs were too high for FBR system. In Chapter 4 biogas reforming processes were studied. This chapter starts with an introduction explaining the properties of the biogas and the main production routes. Then, the experimental procedure carried out is detailed giving concrete information about the experimental set-up, defining the parameters measured, specifying the characteristics of the reactors used and describing the characterization techniques utilized. Each following section describes the results obtained from activity testing with the different catalysts prepared, which is subsequently summarized: Section 4.3: Biogas reforming processes using γ-Al2O3 based catalysts The activity results obtained by several Ni-based catalysts and a bimetallic Rh-Ni catalyst supported on magnesia or alumina modified with oxides like CeO2 and ZrO2 are presented in this section. In addition, an alumina-based commercial catalyst was tested in order to compare the activity results measured. Four different biogas reforming processes were studied using a FBR: dry reforming (DR), biogas steam reforming (BSR), biogas oxidative reforming (BOR) and tri-reforming (TR). For the BSR process different steam to carbon ratios (S/C) from 1.0 to 3.0, were tested. In the case of BOR process the oxygen-to-methane (O2/CH4) ratio was varied from 0.125 to 0.50. Finally, for TR processes different S/C ratios from 1.0 to 3.0, and O2/CH4 ratios of 0.25 and 0.50 were studied. Then, the catalysts which achieved high activity and stability were impregnated in a microreactor to explore the viability of process intensification. The operation with microreactors was carried out under the best experimental conditions measured in the FBR. In addition, the physicochemical characterization of the fresh and spent catalysts was carried out by Inductively Coupled Plasma Atomic Emission Spectroscopy (ICP-AES), N2 physisorption, H2 chemisorption, Temperature Programmed Reduction (TPR), SEM, X-ray Photoelectron Spectroscopy (XPS) and X-ray powder Diffraction (XRD). Operating with the FBR, conversions close to the ones predicted by thermodynamic calculations were obtained by most of the catalysts tested. The Rh-Ni/Ce-Al2O3 catalyst obtained the highest hydrogen production yield in DR. In BSR process, the Ni/Ce-Al2O3 catalyst achieved the best activity results operating at S/C=1.0. In the case of BOR process, the Ni/Ce-Zr-Al2O3 catalyst showed the highest reactants conversion values operating at O2/CH4=0.25. Finally, in the TR process the Rh-Ni/Ce-Al2O3 catalyst obtained the best results operating at S/C=1.0 and O2/CH4=0.25. Therefore, these three catalysts were selected to be coated onto microchannels in order to test its performance under BOR and TR processes conditions. Although the operation using microreactors was carried out under considerably higher WHSV, similar conversions and yields as the ones measured in FBR were measured. Furthermore, attending to other measurements like Turnover Frequency (TOF) and Hydrogen Productivity (PROD), the values calculated for the catalysts tested in microreactors were one order of magnitude higher. Thus, due to the low dispersion degree measured by H2-chemisorption, the Ni/Ce-Al2O3 catalyst reached the highest TOF and PROD values. Section 4.4: Biogas reforming processes using Zeolites L based catalysts In this section three type of L zeolites, with different morphology and size, were synthesized and used as catalyst support. Then, for each type of L zeolite three nickel monometallic and their homologous Rh-Ni bimetallic catalysts were prepared by the wetness impregnation method. These catalysts were tested using the FBR under DR process and different conditions of BSR (S/C ratio of 1.0 and 2.0), BOR (O2/CH4 ratio of 0.25 and 0.50) and TR processes (at S/C=1.0 and O2/CH4=0.25). The characterization of these catalysts was also carried out by using the same techniques mentioned in the previous section. Very high methane and carbon dioxide conversion values were measured for almost all the catalysts under investigation. The experimental results evidenced the better catalytic behavior of the bimetallic catalysts as compared to the monometallic ones. Comparing the catalysts behavior with regards to their morphology, for the BSR process the Disc catalysts were the most active ones at the lowest S/C ratio tested. On the contrary, the Cylindrical (30–60 nm) catalysts were more active under BOR conditions at O2/CH4=0.25 and TR processes. By the contrary, the Cylindrical (1–3 µm) catalysts showed the worst activity results for both processes. Section 4.5: Biogas reforming processes using Na+ and Cs+ doped Zeolites LTL based catalysts A method for the synthesis of Linde Type L (LTL) zeolite under microwave-assisted hydrothermal conditions and its behavior as a support for heterogeneously catalyzed hydrogen production is described in this section. Then, rhodium and nickel-based bimetallic catalysts were prepared in order to be tested by DR process and BOR process at O2/CH4=0.25. Moreover, the characterization of the catalysts under investigation was also carried out. Higher activities were achieved by the catalysts prepared from the non-doped zeolites, Rh-Ni/D and Rh-Ni/N, as compared to the ones supported on Na+ and Cs+ exchanged supports. However, the differences between them were not very significant. In addition, the Na+ and Cs+ incorporation affected mainly to the Disc catalysts. Comparing the results obtained by these catalysts with the ones studied in the section 4.4, in general worst results were achieved under DR conditions and almost the same results when operated under BOR conditions. In Chapter 5 the ethylene glycol (EG) as feed for syngas production by steam reforming (SR) and oxidative steam reforming (OSR) was studied by using microchannel reactors. The product composition was determined at a S/C of 4.0, reaction temperatures between 625°C and 725°C, atmospheric pressure and Volume Hourly Space Velocities (VHSV) between 100 and 300 NL/(gcath). This work was divided in two sections. The first one corresponds to the introduction of the main and most promising EG production routes. Then, the new experimental procedure is detailed and the information about the experimental set-up and the measured parameters is described. The characterization was carried out using the same techniques as for the previous chapter. Then, the next sections correspond to the catalytic activity and catalysts characterization results. Section 5.3: xRh-cm and xRh-np catalysts for ethylene glycol reforming Initially, catalysts with different rhodium loading, from 1.0 to 5.0 wt. %, and supported on α-Al2O3 were prepared by two different preparation methods (conventional impregnation and separate nanoparticle synthesis). Then, the catalysts were compared regarding their measured activity and selectivity, as well as the characterization results obtained before and after the activity tests carried out. The samples prepared by a conventional impregnation method showed generally higher activity compared to catalysts prepared from Rh nanoparticles. By-product formation of species such as acetaldehyde, ethane and ethylene was detected, regardless if oxygen was added to the feed or not. Among the catalysts tested, the 2.5Rh-cm catalyst was considered the best one. Section 5.4: 2.5Rh-cm catalyst support modification with CeO2 and La2O3 In this part of the Chapter 5, the catalyst showing the best performance in the previous section, the 2.5Rh-Al2O3 catalyst, was selected in order to be improved. Therefore, new Rh based catalysts were designed using α-Al2O3 and being modified this support with different contents of CeO2 or La2O3 oxides. All the catalysts containing additives showed complete conversion and selectivities close to the equilibrium in both SR and OSR processes. In addition, for these catalysts the concentrations measured for the C2H4, CH4, CH3CHO and C2H6 by-products were very low. Finally, the 2.5Rh-20Ce catalyst was selected according to its catalytic activity and characterization results in order to run a stability test, which lasted more than 115 hours under stable operation. The last chapter, Chapter 6, summarizes the main conclusions achieved throughout this Thesis work. Although very high reactant conversions and rich hydrogen mixtures were obtained using a fixed bed reaction system, the use of microreactors improves the key issues, heat and mass transfer limitations, through which the reforming reactions are intensified. Therefore, they seem to be a very interesting and promising alternative for process intensification and decentralized production for remote application.

Increased antiparkinson efficacy of the combined administration of VEGF- and GDNF-loaded nanospheres in a partial lesion model of Parkinson's disease

Current research efforts are focused on the application of growth factors, such as glial cell line-derived neurotrophic factor (GDNF) and vascular endothelial growth factor (VEGF), as neuroregenerative approaches that will prevent the neurodegenerative process in Parkinson's disease. Continuing a previous work published by our research group, and with the aim to overcome different limitations related to growth factor administration, VEGF and GDNF were encapsulated in poly(lactic-co-glycolic acid) nanospheres (NS). This strategy facilitates the combined administration of the VEGF and GDNF into the brain of 6-hydroxydopamine (6-OHDA) partially lesioned rats, resulting in a continuous and simultaneous drug release. The NS particle size was about 200 nm and the simultaneous addition of VEGF NS and GDNF NS resulted in significant protection of the PC-12 cell line against 6-OHDA in vitro. Once the poly(lactic-co-glycolic acid) NS were implanted into the striatum of 6-OHDA partially lesioned rats, the amphetamine rotation behavior test was carried out over 10 weeks, in order to check for in vivo efficacy. The results showed that VEGF NS and GDNF NS significantly decreased the number of amphetamine-induced rotations at the end of the study. In addition, tyrosine hydroxylase immunohistochemical analysis in the striatum and the external substantia nigra confirmed a significant enhancement of neurons in the VEGF NS and GDNF NS treatment group. The synergistic effect of VEGF NS and GDNF NS allows for a reduction of the dose by half, and may be a valuable neurogenerative/neuroreparative approach for treating Parkinson's disease.

Órdenes generales del Cuerpo de Ejército nº 1 del Ejército del Norte, dadas entre los días 14 de julio y 5 de agosto de 1937, firmadas por el Jefe del Estado Mayor

Orden nº 24 (14 de julio). Unidad de instalación: Carpeta Rectorado G-2. 2 hojas. Orden nº 26 (16 de julio). Unidad de instalación: Carpeta Rectorado G-3. 1 hoja. Orden nº 27 (17 de julio). Unidad de instalación: Carpeta Rectorado G-4. 2 hojas. Orden nº 28 (18 de julio). Unidad de instalación: Carpeta Rectorado G-5. 3 hojas. Orden nº 32 (22 de julio). Unidad de instalación: Carpeta Rectorado G-6. 3 hojas + 1 h. de anexo. Orden nº 40 (31 de julio). Unidad de instalación: Carpeta Rectorado G-7. 1 hoja. Orden nº 41 (1 de agosto). Unidad de instalación: Carpeta Rectorado G-8. 1 hoja. Orden nº 44 (4 de agosto). Unidad de instalación: Carpeta Rectorado G-9. 2 hojas. Orden nº 46 (5 de agosto). Unidad de instalación: Carpeta Rectorado G-10. 1 hoja. Mecanografiadas

Postantifungal Effect of Micafungin against the Species Complexes of Candida albicans and Candida parapsilosis

Micafungin is an effective antifungal agent useful for the therapy of invasive candidiasis. Candida albicans is the most common cause of invasive candidiasis; however, infections due to non-C. albicans species, such as Candida parapsilosis, are rising. Killing and postantifungal effects (PAFE) are important factors in both dose interval choice and infection outcome. The aim of this study was to determinate the micafungin PAFE against 7 C. albicans strains, 5 Candida dubliniensis, 2 Candida Africana, 3 C. parapsilosis, 2 Candida metapsilosis and 2 Candida orthopsilosis. For PAFE studies, cells were exposed to micafungin for 1 h at concentrations ranging from 0.12 to 8 mu g/ml. Time-kill experiments (TK) were conducted at the same concentrations. Samples were removed at each time point (0-48 h) and viable counts determined. Micafungin (2 mu g/ml) was fungicidal (>= 3 log(10) reduction) in TK against 5 out of 14 (36%) strains of C. albicans complex. In PAFE experiments, fungicidal endpoint was achieved against 2 out of 14 strains (14%). In TK against C. parapsilosis, 8 mu g/ml of micafungin turned out to be fungicidal against 4 out 7 (57%) strains. Conversely, fungicidal endpoint was not achieved in PAFE studies. PAFE results for C. albicans complex (41.83 +/- 2.18 h) differed from C. parapsilosis complex (8.07 +/- 4.2 h) at the highest tested concentration of micafungin. In conclusion, micafungin showed significant differences in PAFE against C. albicans and C. parapsilosis complexes, being PAFE for the C. albicans complex longer than for the C. parapsilosis complex.