Influencia de la adición de nanosílice y microsílice en el comportamiento mecánico, microestructural y durable de un hormigón autocompactante

Desde mediados de la década de los 80 se está investigando sobre el hormigón autocompactante. Cada día, su uso en el mundo de la construcción es más común debido a sus numerosas ventajas como su excelente fluidez ya que puede fluir bajo su propio peso y llenar encofrados con formas complicadas y muy armados sin necesidad de compactaciones internas o externas. Por otra parte, la búsqueda de materiales más resistentes y duraderos, ha dado lugar a la incorporación de adiciones en materiales a base de cemento. En las últimas dos décadas, los ensayos con los nanomateriales, ha experimentado un gran aumento. Los resultados hasta ahora obtenidos pueden asumir no sólo un aumento en la resistencia de estos materiales, pero un cambio es su funcionalidad. Estas nanopartículas, concretamente la nanosílice, no sólo mejoran sus propiedades mecánicas y especialmente sus propiedades durables, sino que pueden implicar un cambio sustancial en las condiciones de uso y en su ciclo de vida. Este trabajo tiene como principal objetivo el estudio de las propiedades mecánicas, características microestructurales y durables de un hormigón autocompactante cuando se le agrega como adición nanosílice, microsílice y mezcla binarias de ambas, como adición al cemento. Para ello se han realizado 10 mezclas de hormigón. Se utilizó como referencia un hormigón autocompactante obtenido con cemento, caliza, árido, aditivo modificador de viscosidad Se han fabricado tres hormigones con la misma dosificación pero con diferentes contenidos de nanosílice. 2,5%, 5% y 7,5% Tres dosificaciones con adición de microsílice 2,5%, 5% y 7,5% y las tres restantes con mezclas binarias de nanosílice y microsílice con respectivamente2,5%-2,5%, 5%-2,5% y 2,5%-5%, sobre el peso del cemento. El contenido de superplastificante se modificó para conseguir las características de autocompactabilidad. Para observar los efectos de las adiciones añadidas al hormigón, se realiza una extensa campaña experimental. En ella se evaluaron en primer lugar, las características de autocompactabilidad del material en estado fresco, mediante los ensayos prescritos en la Instrucción Española del hormigón estructural EHE 08. Las propiedades mecánicas fueron evaluadas con ensayos de resistencia a compresión, resistencia a tracción indirecta y módulo de elasticidad. Las características microestructurales fueron analizadas mediante porosimetría por intrusión de mercurio, el análisis termogravimétrico y la microscopía electrónica de barrido. Para el estudio de la capacidad durable de las mezclas se realizaron ensayos de resistividad eléctrica, migración de cloruros, difusión de cloruros, carbonatación acelerada, absorción capilar y resistencia al hielo-deshielo. Los resultados ponen de manifiesto que la acción de las adiciones genera mejoras en las propiedades resistentes del material. Así, la adición de nanosílice proporciona mayores resistencias a compresión que la microsílice, sin embargo las mezclas binarias con bajas proporciones de adición producen mayores resistencias. Por otra parte, se observó mediante la determinación de las relaciones de gel/portlandita, que las mezclas que contienen nanosílice tienen una mayor actividad puzolánica que las que contienen microsílice. En las mezclas binarias se obtuvo como resultado que mientras mayor es el contenido de nanosílice en la mezcla mayor es la actividad puzolánica. Unido a lo anteriormente expuesto, el estudio de la porosidad da como resultado que la adición de nanosílice genera un refinamiento del tamaño de los poros mientras que la adición de microsílice disminuye la cantidad de los mismos sin variar el tamaño de poro medio. Por su parte, en las micrografías, se visualizó la formación de cristales procedentes de la hidratación del cemento. En ellas, se pudo observar, que al adicionar nanosílice, la velocidad de hidratación aumenta al aumentar la formación de monosulfoaluminatos con escasa presencia de etringita. Mientras que en las mezclas con adición de microsílice se observan mayor cantidad de cristales de etringita, lo que confirma que la velocidad de hidratación en estos últimos fue menor. Mediante el estudio de los resultados de las pruebas de durabilidad, se observó que no hay diferencias significativas entre el coeficiente de migración de cloruros y el coeficiente de difusión de cloruros en hormigones con adición de nano o microsílice. Aunque este coeficiente es ligeramente menor en mezclas con adición de microsílice. Sin embargo, en las mezclas binarias de ambas adiciones se obtuvo valores de los coeficientes de difusión o migración de cloruros inferiores a los obtenidos en mezclas con una única adición. Esto se evidencia en los resultados de las pruebas de resistividad eléctrica, de difusión de cloruros y de migración de cloruros. Esto puede ser debido a la suma de los efectos que producen el nano y micro adiciones en la porosidad. El resultado mostró que nanosílice tiene un papel importante en la reducción de los poros y la microsílice disminuye el volumen total de ellos. Esto permite definir la vida útil de estos hormigones a valores muy superiores a los exigidos por la EHE-08, por lo que es posible reducir, de forma notable, el recubrimiento exigido en ambiente de alta agresividad asegurando un buen comportamiento en servicio. Por otra parte, la pérdida de masa debido a los ciclos de congelación-descongelación es significativamente menor en los hormigones que contienen nanosílice que los que contienen microsílice. Este resultado está de acuerdo con el ensayo de absorción capilar. De manera general, se puede concluir que son las mezclas binarias y más concretamente la mezcla con un 5% de nanosílice y 2,5% de microsílice la que presenta los mejores resultados tanto en su comportamiento resistente con en su comportamiento durable. Esto puede ser debido a que en estas mezclas la nanosílice se comporta como un núcleo de activación de las reacciones puzolánicas rodeado de partículas de mayor tamaño. Además, el extraordinario comportamiento durable puede deberse también a la continuidad en la curva granulométrica por la existencia de la microsílice, el filler calizo, el cemento, la arena y la gravilla con tamaños de partículas que garantice mezclas muy compactas que presentan elevadas prestaciones. Since the middle of the decade of the 80 is being investigated about self-consolidating concrete. Every day, its use in the world of construction is more common due to their numerous advantages as its excellent fluidity such that it can flow under its own weight and fill formworks with complicated shapes and congested reinforcement without need for internal or external compactions. Moreover, the search for more resistant and durable materials, has led to the incorporation of additions to cement-based materials. In the last two decades, trials with nanomaterials, has experienced a large increase. The results so far obtained can assume not only an increase in the resistance of these materials but a change is its functionality. These nano particles, particularly the nano silica, not only improve their mechanical properties and especially its durable properties, but that may imply a substantial change in the conditions of use and in their life cycle. This work has as its main objective the study of the mechanical properties, the microstructural characteristics and durability capacity in one self-compacting concrete, when added as addition to cement: nano silica, micro silica o binary mixtures of both. To this effect, 10 concrete mixes have been made. As reference one with a certain amount of cement, limestone filler, viscosity modifying additive and water/binder relation. Furthermore they were manufactured with the same dosage three mix with addition of 2.5%, 5% and 7.5% of nano silica by weight of cement. Other three with 2.5%, 5% and 7.5% of micro silica and the remaining three with binary mixtures of 2.5%-2.5%, 5%-2.5% and 2.5%-5% of silica nano-micro silica respectively, b weight of cement, varying only the amount of superplasticizer to obtain concrete with characteristics of self-compactability. To observe the effects of the additions added to the concrete, an extensive experimental campaign was performed. It assessed, first, the characteristics of self-compactability of fresh material through the tests prescribed in the Spanish Structural Instruction Concrete EHE 08. The mechanical properties were evaluated by compression strength tests, indirect tensile strength and modulus of elasticity. The microstructural properties were analyzed by mercury intrusion porosimetry, thermogravimetric analysis and scanning electron microscopy. To study the durability, were performed electrical resistivity tests, migration and diffusion of chlorides, accelerated carbonation, capillary suction and resistance to freeze-thaw cycles. The results show that the action of the additions generates improvements in the strength properties of the material. Specifically, the addition of nano silica provides greater resistance to compression that the mix with micro silica, however binary mixtures with low addition rates generate higher strengths. Moreover, it was observed by determining relationships gel/portlandite, that the pozzolanic activity in the mixtures with nano silica was higher than in the mixtures with micro silica. In binary mixtures it was found that the highest content of nano silica in the mix is the one with the highest pozzolanic activity. Together with the foregoing, the study of the porosity results in the mixture with addition of nano silica generates a refinement of pore size while adding micro silica decreases the amount thereof without changing the average pore size. On the other hand, in the micrographs, the formation of crystals of cement hydration was visualized. In them, it was observed that by adding nano silica, the speed of hydration increases with increasing formation monosulfoaluminatos with scarce presence of ettringite. While in mixtures with addition of micro silica, ettringite crystals are observed, confirming that the hydration speed was lower in these mixtures. By studying the results of durability testing, it observed that no significant differences between the coefficient of migration of chlorides and coefficient of diffusion of chlorides in concretes with addition of nano or micro silica. Although this coefficient is slightly lower in mixtures with addition of micro silica. However, in binary mixtures of both additions was obtained values of coefficients of difusion o migration of chlorides lower than those obtained in mixtures with one of the additions. This is evidenced by the results of the tests electrical resistivity, diffusion of chlorides and migration of chlorides. This may be due to the sum of the effects that produced the nano and micro additions in the porosity. The result showed that nano silica has an important role in the pores refining and the micro silica decreases the total volume of them. This allows defining the life of these concretes in values to far exceed those required by the EHE-08, making it possible to reduce, significantly, the coating required in highly aggressive environment and to guarantee good behavior in service. Moreover, the mass loss due to freeze-thaw cycles is significantly lower in concretes containing nano silica than those containing micro silica. This result agrees with the capillary absorption test. In general, one can conclude that the binary mixture and more specifically the mixture with 5% of nano silica and 2.5% silica fume is which presents the best results in its durable behavior. This may be because in these mixtures, the nano silica behaves as cores activation of pozzolanic reactions. In addition, the durable extraordinary behavior may also be due to the continuity of the grading curve due to existence of micro silica, limestone filler, cement, sand and gravel with particle sizes that guarantees very compact mixtures which have high performance.

Interactions métaboliques entre le bisphénol A et le naproxène dans un modèle de foie de rat isolé et perfusé

L'exposition aux mélanges de contaminants (environnementaux, alimentaires ou thérapeutiques) soulève de nombreuses interrogations et inquiétudes vis-à-vis des probabilités d'interactions toxicocinétiques et toxicodynamiques. Une telle coexposition peut influencer le mode d’action des composants du cocktail et donc de leur toxicité, suite à un accroissement de leurs concentrations internes. Le bisphénol A (4 dihydroxy-2,2-diphenylpropane) est un contaminant chimique répandu de manière ubiquitaire dans notre environnement, largement utilisé dans la fabrication des plastiques avec l’un des plus grands volumes de production à l’échelle mondiale. Il est un perturbateur endocrinien par excellence de type œstrogèno-mimétique. Cette molécule est biotransformée en métabolites non toxiques par un processus de glucuronidation. L'exposition concomitante à plusieurs xénobiotiques peut induire à la baisse le taux de glucuronidation du polluant chimique d'intérêt, entre autres la co-exposition avec des médicaments. Puisque la consommation de produits thérapeutiques est un phénomène grandissant dans la population, la possibilité d’une exposition simultanée est d’autant plus grande et forte. Sachant que l'inhibition métabolique est le mécanisme d'interaction le plus plausible pouvant aboutir à une hausse des niveaux internes ainsi qu’à une modulation de la toxicité prévue, la présente étude visait d'abord à confirmer et caractériser ce type d'interactions métaboliques entre le bisphénol A et le naproxène, qui est un anti-inflammatoire non stéroïdiennes (AINS), sur l'ensemble d'un organe intact en utilisant le système de foie de rat isolé et perfusé (IPRL). Elle visait ensuite à déterminer la cinétique enzymatique de chacune de ces deux substances, seule puis en mélange binaire. Dans un second temps, nous avons évalué aussi l’influence de la présence d'albumine sur la cinétique métabolique et le comportement de ces deux substances étudiées en suivant le même modèle de perfusion in vivo au niveau du foie de rat. Les constantes métaboliques ont été déterminées par régression non linéaire. Les métabolismes du BPA et du NAP seuls ont montré une cinétique saturable avec une vélocité maximale (Vmax) de 8.9 nmol/min/ mg prot de foie et une constante d'affinité de l'enzyme pour le substrat (Km) de 51.6 μM pour le BPA et de 3 nmol/min/mg prot de foie et 149.2 μM pour le NAP. L'analyse des expositions combinées suggère une inhibition compétitive partielle du métabolisme du BPA par le NAP avec une valeur de Ki estimée à 0.3542 μM. Les résultats obtenus montrent que l’analyse de risque pour les polluants environnementaux doit donc prendre en considération la consommation des produits pharmaceutiques comme facteur pouvant accroitre le niveau interne lors d’une exposition donnée. Ces données in vivo sur les interactions métaboliques pourraient être intégrées dans un modèle pharmacocinétique à base physiologique (PBPK) pour prédire les conséquences toxicococinétique (TK) de l'exposition d'un individu à ces mélanges chimiques.

Interactions métaboliques entre le bisphénol A et le naproxène dans un modèle de foie de rat isolé et perfusé

L'exposition aux mélanges de contaminants (environnementaux, alimentaires ou thérapeutiques) soulève de nombreuses interrogations et inquiétudes vis-à-vis des probabilités d'interactions toxicocinétiques et toxicodynamiques. Une telle coexposition peut influencer le mode d’action des composants du cocktail et donc de leur toxicité, suite à un accroissement de leurs concentrations internes. Le bisphénol A (4 dihydroxy-2,2-diphenylpropane) est un contaminant chimique répandu de manière ubiquitaire dans notre environnement, largement utilisé dans la fabrication des plastiques avec l’un des plus grands volumes de production à l’échelle mondiale. Il est un perturbateur endocrinien par excellence de type œstrogèno-mimétique. Cette molécule est biotransformée en métabolites non toxiques par un processus de glucuronidation. L'exposition concomitante à plusieurs xénobiotiques peut induire à la baisse le taux de glucuronidation du polluant chimique d'intérêt, entre autres la co-exposition avec des médicaments. Puisque la consommation de produits thérapeutiques est un phénomène grandissant dans la population, la possibilité d’une exposition simultanée est d’autant plus grande et forte. Sachant que l'inhibition métabolique est le mécanisme d'interaction le plus plausible pouvant aboutir à une hausse des niveaux internes ainsi qu’à une modulation de la toxicité prévue, la présente étude visait d'abord à confirmer et caractériser ce type d'interactions métaboliques entre le bisphénol A et le naproxène, qui est un anti-inflammatoire non stéroïdiennes (AINS), sur l'ensemble d'un organe intact en utilisant le système de foie de rat isolé et perfusé (IPRL). Elle visait ensuite à déterminer la cinétique enzymatique de chacune de ces deux substances, seule puis en mélange binaire. Dans un second temps, nous avons évalué aussi l’influence de la présence d'albumine sur la cinétique métabolique et le comportement de ces deux substances étudiées en suivant le même modèle de perfusion in vivo au niveau du foie de rat. Les constantes métaboliques ont été déterminées par régression non linéaire. Les métabolismes du BPA et du NAP seuls ont montré une cinétique saturable avec une vélocité maximale (Vmax) de 8.9 nmol/min/ mg prot de foie et une constante d'affinité de l'enzyme pour le substrat (Km) de 51.6 μM pour le BPA et de 3 nmol/min/mg prot de foie et 149.2 μM pour le NAP. L'analyse des expositions combinées suggère une inhibition compétitive partielle du métabolisme du BPA par le NAP avec une valeur de Ki estimée à 0.3542 μM. Les résultats obtenus montrent que l’analyse de risque pour les polluants environnementaux doit donc prendre en considération la consommation des produits pharmaceutiques comme facteur pouvant accroitre le niveau interne lors d’une exposition donnée. Ces données in vivo sur les interactions métaboliques pourraient être intégrées dans un modèle pharmacocinétique à base physiologique (PBPK) pour prédire les conséquences toxicococinétique (TK) de l'exposition d'un individu à ces mélanges chimiques.

Multicomponent adsorption on activated carbons under supercritical conditions

Adsorption of binary mixtures onto activated carbon Norit R1 for the system nitrogen-methane-carbon dioxide was investigated over the pressure range up to 15 MPa. A new model is proposed to describe the experimental data. It is based on the assumption that an activated carbon can be characterized by the distribution function of elements of adsorption volume (EAV) over the solid-fluid potential. This function may be evaluated from pure component isotherms using the equality of the chemical potentials in the adsorbed phase and in the bulk phase for each EAV. In the case of mixture adsorption a simple combining rule is proposed, which allows determining the adsorbed phase density and its composition in the EAV at given pressure and compositions of the bulk phase. The adsorbed concentration of each adsorbate is the integral of its density over the set of EAV. The comparison with experimental data on binary mixtures has shown that the approach works reasonably well. In the case of high-pressure binary mixture adsorption, when only total amount adsorbed was measured, the proposed model allows reliably determining partial amounts of the adsorbed components. (C) 2004 Elsevier Inc. All rights reserved.

Gelatinization of starch in mixed sugar systems

Sugars affect the gelatinization of starch, with the effect varying significantly between sugars. Since many food products contain a mixture of sugar sources, it is important to understand how their mixtures affect starch gelatinization. In a Rapid Visco Analyser study of maize starch gelatinization, changing proportions in binary mixtures of refined sugars saw a largely proportionate change in starch gelatinization properties. However, binary mixture of pure sugars and honey, or a model honey system (the main sugars in honey) and honey responded differently. Generally, replacing 25% or 50% of the refined sugar or model honey system with honey gave a large change in starch gelatinization properties, while further increases in honey level had little further effect. Differences between honey and buffered model honey system (either gluconic acid, or a mixture of citric acid and di-sodium phosphate) showed the sensitivity of starch gelatinization to the composition of the nonsaccharide component. (c) 2004 Swiss Society of Food Science and Technology. Published by Elsevier Ltd. All rights reserved.

Modelling and simulation of biomass gasification in a circulating fluidized bed reactor

Computational Fluid Dynamics (CFD) has found great acceptance among the engineering community as a tool for research and design of processes that are practically difficult or expensive to study experimentally. One of these processes is the biomass gasification in a Circulating Fluidized Bed (CFB). Biomass gasification is the thermo-chemical conversion of biomass at a high temperature and a controlled oxygen amount into fuel gas, also sometime referred to as syngas. Circulating fluidized bed is a type of reactor in which it is possible to maintain a stable and continuous circulation of solids in a gas-solid system. The main objectives of this thesis are four folds: (i) Develop a three-dimensional predictive model of biomass gasification in a CFB riser using advanced Computational Fluid Dynamic (CFD) (ii) Experimentally validate the developed hydrodynamic model using conventional and advanced measuring techniques (iii) Study the complex hydrodynamics, heat transfer and reaction kinetics through modelling and simulation (iv) Study the CFB gasifier performance through parametric analysis and identify the optimum operating condition to maximize the product gas quality. Two different and complimentary experimental techniques were used to validate the hydrodynamic model, namely pressure measurement and particle tracking. The pressure measurement is a very common and widely used technique in fluidized bed studies, while, particle tracking using PEPT, which was originally developed for medical imaging, is a relatively new technique in the engineering field. It is relatively expensive and only available at few research centres around the world. This study started with a simple poly-dispersed single solid phase then moved to binary solid phases. The single solid phase was used for primary validations and eliminating unnecessary options and steps in building the hydrodynamic model. Then the outcomes from the primary validations were applied to the secondary validations of the binary mixture to avoid time consuming computations. Studies on binary solid mixture hydrodynamics is rarely reported in the literature. In this study the binary solid mixture was modelled and validated using experimental data from the both techniques mentioned above. Good agreement was achieved with the both techniques. According to the general gasification steps the developed model has been separated into three main gasification stages; drying, devolatilization and tar cracking, and partial combustion and gasification. The drying was modelled as a mass transfer from the solid phase to the gas phase. The devolatilization and tar cracking model consist of two steps; the devolatilization of the biomass which is used as a single reaction to generate the biomass gases from the volatile materials and tar cracking. The latter is also modelled as one reaction to generate gases with fixed mass fractions. The first reaction was classified as a heterogeneous reaction while the second reaction was classified as homogenous reaction. The partial combustion and gasification model consisted of carbon combustion reactions and carbon and gas phase reactions. The partial combustion considered was for C, CO, H2 and CH4. The carbon gasification reactions used in this study is the Boudouard reaction with CO2, the reaction with H2O and Methanation (Methane forming reaction) reaction to generate methane. The other gas phase reactions considered in this study are the water gas shift reaction, which is modelled as a reversible reaction and the methane steam reforming reaction. The developed gasification model was validated using different experimental data from the literature and for a wide range of operating conditions. Good agreement was observed, thus confirming the capability of the model in predicting biomass gasification in a CFB to a great accuracy. The developed model has been successfully used to carry out sensitivity and parametric analysis. The sensitivity analysis included: study of the effect of inclusion of various combustion reaction; and the effect of radiation in the gasification reaction. The developed model was also used to carry out parametric analysis by changing the following gasifier operating conditions: fuel/air ratio; biomass flow rates; sand (heat carrier) temperatures; sand flow rates; sand and biomass particle sizes; gasifying agent (pure air or pure steam); pyrolysis models used; steam/biomass ratio. Finally, based on these parametric and sensitivity analysis a final model was recommended for the simulation of biomass gasification in a CFB riser.

Systematic screening of compressed ODT excipients:cellulosic versus non-cellulosic

The successful development of compressed ODTs utilises low compression forces to create a porous structure whereby excipients are added to enhance wicking/swelling action or provide strength to the fragile tablet framework. In this work, a systematic investigation comparing materials from two different categories was employed to understand their functionality in binary mixture tablets of the most commonly used diluent mannitol. Cellulose based excipients such as HPC (SSL-SFP), L-HPC (NBD-022) and MCC (Avicel PH-102) were compared with non-cellulosic materials such as PEO (POLYOX WSR N-10) and Crospovidone (XL-10). Pure excipient properties were studied using Heckel Plot, compressibility profile, SEM and XRPD, whereas the prepared binary mixture compacts were studied for hardness, disintegration time and friability. Results from our investigation provide insight into differences encountered in product performance of ODT upon inclusion of additional materials. For example, non-cellulosic excipients Polyox and Crospovidone showed higher plasticity (Py values 588 and 450MPa) in pure form but not in binary mixtures of mannitol. Cellulosic excipients, nonetheless, offer faster disintegration (<30 sec) specifically L-HPC and MCC tablets. Disintegration time for tablets with fully substituted-HPC was prolonged (200-500 sec) upon increasing concentration between 1-10% due to gelation/matrix formation. It can be concluded that despite the reasonably good plasticity of both cellulosic and non-cellulosic excipients in pure form, the mechanical strength in binary mixtures is negatively impacted by the fragmentation/fracture effect of mannitol. © 2014 Bentham Science Publishers.

Systematic screening of compressed ODT excipients : cellulosic versus non-cellulosic

The successful development of c ompressed ODTs utilises low compression force s to create a porous structure whereby excipients are added to enhance wicking/swelling action or p rovide strength to the fragile tablet framework. In this work, a systematic investigation comparing materials from two different categories was employed to understand their functionality in binary mixture tablets of the most commonly used diluent mannitol. Cellulose based excipients such as HPC (SSL-SFP), L-HPC (NBD -022) and MCC (Avicel PH -102 ) were compared with non -cellulosic materials such as PEO (POLYOX WSR N -10) and Crospovidone (XL -10). P ure excipient properties were studied using Heckel Plot, compre ssibility profile, SEM and XR PD, w hereas the prepared binary mixture compacts were studied for hardness, disintegration time and friability. Results from our investigation provide insight into differences encountered in product performance of ODT upon inclusion of additional materials. For example, non -cellulosic excipients Polyox and Crospovidone showed higher plasticity (Py values 588 and 450 MPa) in pure form but not in binary mixtures of mannitol . Cellulosic excipients, nonetheless, offer faster disintegration (

Methyl chloride purification for the silicone industry

This study experimentally investigated methyl chloride (MeCl) purification method using an inhouse designed and built volumetric adsorption/desorption rig. MeCl is an essential raw material in the manufacture of silicone however all technical grades of MeCl contain concentrations (0.2 - 1.0 % wt) of dimethyl ether (DME) which poison the process. The project industrial partner had previously exhausted numerous separation methods, which all have been deemed not suitable for various reasons. Therefore, adsorption/desorption separation was proposed in this study as a potential solution with less economic and environmental impact. Pure component adsorption/desorption was carried out for DME and MeCl on six different adsorbents namely: zeolite molecular sieves (types 4 Å and 5 Å); silica gels (35-70 mesh, amorphous precipitated, and 35-60 mesh) and granular activated carbon (type 8-12 mesh). Subsequent binary gas mixture adsorption in batch and continuous mode was carried out on both zeolites and all three silica gels following thermal pre-treatment in vacuum. The adsorbents were tested as received and after being subjected to different thermal and vacuum pre-treatment conditions. The various adsorption studies were carried out at low pressure and temperature ranges of 0.5 - 3.5 atm and 20 - 100 °C. All adsorbents were characterised using Brunauer Emmett Teller (BET), thermogravimetric analysis (TGA), scanning electron microscopy (SEM) and energy dispersive x-ray analysis (EDXA) to investigate their physical and chemical properties. The well-known helium (He) expansion method was used to determine the empty manifold and adsorption cell (AC) regions and respective void volumes for the different adsorbents. The amounts adsorbed were determined using Ideal gas laws via the differential pressure method. The heat of adsorption for the various adsorbate-adsorbent (A-S) interactions was calculated using a new calorimetric method based on direct temperature measurements inside the AC. Further adsorption analysis included use of various empirical and kinetic models to determine and understand the behaviour of the respective interactions. The gas purification behaviour was investigated using gas chromatography and mass spectroscopy (GC-MC) analysis. Binary gas mixture samples were syringed from the manifold iii and AC outlet before and after adsorption/desorption analysis through manual sample injections into the GC-MS to detect and quantify the presence of DME and ultimately observe for methyl chloride purification. Convincing gas purification behaviour was confirmed using two different GC columns, thus giving more confidence on the measurement reliability. From the single pure component adsorption of DME and MeCl on the as received zeolite 4A subjected to 1 h vacuum pre-treatment, both gases exhibited pseudo second order adsorption kinetics with DME exhibiting a rate constant nearly double that of MeCl thus suggesting a faster rate of adsorption. From the adsorption isotherm classification both DME and MeCl exhibited Type II and I adsorption isotherm classifications, respectively. The strength of bonding was confirmed by the differential heat of adsorption measurement, which was found to be 23.30 and 10.21 kJ mol-1 for DME and MeCl, respectively. The former is believed to adsorb heterogeneously through hydrogen bonding whilst MeCl adsorbs homogenously via van der Waal’s (VDW) forces. Single pure component adsorption on as received zeolite 5A, silica gels (35-70, amorphous precipitated and 35-60) resulted in similar adsorption/desorption behaviour in similar quantities (mol kg-1). The adsorption isotherms for DME and MeCl on zeolite 5A, silica gels (35-70, amorphous precipitated and 35-60) and activated carbon 8-12 exhibited Type I classifications, respectively. Experiments on zeolite 5A indicated that DME adsorbed stronger, faster and with a slightly stronger strength of interaction than MeCl but in lesser quantities. On the silica gels adsorbents, DME exhibited a slightly greater adsorption capacity whilst adsorbing at a similar rate and strength of interaction compared to MeCl. On the activated carbon adsorbent, MeCl exhibited the greater adsorption capacity at a faster rate but with similar heats of adsorption. The effect of prolonged vacuum (15 h), thermal pre-treatment (150 °C) and extended equilibrium time (15 min) were investigated for the adsorption behaviour of DME and MeCl on both zeolites 4A and 5A, respectively. Compared to adsorption on as received adsorbents subjected to 1 h vacuum the adsorption capacities for DME and MeCl were found to increase by 1.95 % and 20.37 % on zeolite 4A and by 4.52 % and 6.69 % on zeolite 5A, respectively. In addition the empirical and kinetic models and differential heats of adsorption resulted in more definitive fitting curves and trends due to the true equilibrium position of the adsorbate with the adsorbent. Batch binary mixture adsorption on thermally and vacuum pre-treated zeolite 4A demonstrated purification behaviour of all adsorbents used for MeCl streams containing DME impurities, with a concentration as low as 0.66 vol. %. The GC-MS analysis showed no DME detection for the tested concentration mixtures at the AC outlet after 15 or 30 min, whereas MeCl was detectable in measurable amounts. Similar behaviour was also observed when carrying out adsorption in continuous mode. On the other hand, similar studies on the other adsorbents did not show such favourable MeCl purification behaviour. Overall this study investigated a wide range of adsorbents (zeolites, silica gels and activated carbon) and demonstrated for the first time potential to purify MeCl streams containing DME impurities using adsorption/desorption separation under different adsorbent pre-treatment and adsorption operating conditions. The study also revealed for the first time the adsorption isotherms, empirical and kinetic models and heats of adsorption for the respective adsorbentsurface (A-S) interactions. In conclusion, this study has shown strong evidence to propose zeolite 4A for adsorptive purification of MeCl. It is believed that with a technical grade MeCl stream competitive yet simultaneous co-adsorption of DME and MeCl occurs with evidence of molecular sieiving effects whereby the larger DME molecules are unable to penetrate through the adsorbent bed whereas the smaller MeCl molecules diffuse through resulting in a purified MeCl stream at the AC outlet. Ultimately, further studies are recommended for increased adsorption capacities by considering wider operating conditions, e.g. different adsorbent thermal and vacuum pre-treatment and adsorbing at temperatures closer to the boiling point of the gases and different conditions of pressure and temperature.

Trissoralen um medicamento de baixa dosagem: estudos termoanalíticos da compatibilidade do fármaco-excipientes e determinação de parâmetros de qualidade para cápsulas magistrais

The trioxsalen (Tri) is a low-dose drug used in the treatment of psoriasis and other skin diseases. The aim of the study was applying the thermal analysis and complementary techniques for characterization, evaluation of the trioxsalen stability and components of manipulated pharmaceutical formulations. The thermal behavior of the Tri by TG/DTG-DTA in dynamic atmosphere of synthetic air and nitrogen showed the same profile with a melting peak followed by a volatilization-related event. From the curves TG / DTG is observed a single stage of mass loss. By heating the drug in the stove at temperatures of 80, 240 and 260 °C, it had no change in chemical structure through the techniques of XRD, HPLC, MIR, OM and SEM. From the non-isothermal and isothermal TG kinetic studies was possible to calculate the activation energy and reaction order for the Tri. The drug showed good thermal stability. Studies on drug-excipient compatibility showed interaction of trissoralen with sodium lauryl sulfate 1:1. There was no interaction with aerosol, pregelatinized starch, sodium starch glycolate, cellulose, croscarmellose sodium, magnesium stearate, lactose and mannitol.The characterization of three trioxsalen formulations at concentrations of 2.5, 5, 7.5, 10, 12.5 and 15 mg was performed by DSC, TG / DTG, XRD, NIR and MIR. The PCA classification method based on spectral data from the NIR and MIR of trissoralen formulations allows successful differentiation into three groups. The formulation 3 was the one that best showed analytical profile with the following composition of aerosil excipients, pre-gelatinized starch and cellulose. The activation energy of the volatilization process of the drug was determined in binary mixtures and formulation 3 through fitting and isoconversional methods. The binary mixture with sodium starch glycolate and lactose showed differences in kinetic parameters compared to the drug isolated. The thermoanalytical techniques (DSC and TG / DTG) were shown to be promising methodologies for quantifying trioxsalen obtained by the linearity, selectivity, no use solvents, without sample preparation, speed and practicality.

Radiogenic Hf isotopic composition of continental eolian dust in Pacific Ocean sediments

The inorganic silicate fraction extracted from bulk pelagic sediments from the North Pacific Ocean is eolian dust. It monitors the composition of continental crust exposed to erosion in Asia. 176Lu/177Hf ratios of modern dust are subchondritic between 0.011 and 0.016 but slightly elevated with respect to immature sediments. Modern dust samples display a large range in Hf isotopic composition (IC), -4.70 < epsilon-Hf < +16.45, which encompasses that observed for the time series of DSDP cores 885/886 and piston core LL44-GPC3 extending back to the late Cretaceous. Hafnium and neodymium isotopic results are consistent with a dominantly binary mixture of dust contributed from island arc volcanic material and dust from central Asia. The Hf-Nd isotopic correlation for all modern dust samples, epsilon-Hf= =0.78 epsilon-Nd = +5.66 (n =22, R**2 =0.79), is flatter than those reported so far for terrestrial reservoirs. Moreover, the variability in epsilon-Hf of Asian dust exceeds that predicted on the basis of corresponding epsilon-Nd values (34.76 epsilon-Hf < +2.5; -10.96< epsilon-Nd <-10.1). This is attributed to: (1) the fixing of an important unradiogenic fraction of Hf in zircons, balanced by radiogenic Hf that is mobile in the erosional cycle, (2) the elevated Lu/Hf ratio in chemical sediments which, given time, results in a Hf signature that is radiogenic compared with Hf expected from its corresponding Nd isotopic components, and (3) the possibility that diagenetic resetting of marine sediments may incorporate a significant radiogenic Hf component into diagenetically grown minerals such as illite. Together, these processes may explain the variability and more radiogenic character of Hf isotopes when compared to the Nd isotopic signatures of Asian dust. The Hf-Nd isotope time series of eolian dust are consistent with the results of modern dust except two samples that have extremely radiogenic Hf for their Nd (epsilon-Hf =+8.6 and +10.3, epsilon-Nd =39.5 and 39.8). These data may point to a source contribution of dust unresolved by Nd and Pb isotopes. The Hf IC of eolian dust input to the oceans may be more variable and more radiogenic than previously anticipated. The Hf signature of Pacific seawater, however, has varied little over the past 20 Myr, especially across the drastic increase of eolian dust flux from Asia around 3.5 Ma. Therefore, continental contributions to seawater Hf appear to be riverine rather than eolian. Current predictions regarding the relative proportions of source components to seawater Hf must account for the presence of a variable and radiogenic continental component. Data on the IC and flux of river-dissolved Hf to the oceans are urgently required to better estimate contributions to seawater Hf. This then would permit the use of Hf isotopes as a monitor of past changes in erosion.

Dynamical collapse in a degenerate binary fermion mixture using a hydrodynamic model

We use a time-dependent dynamical hydrodynamic model to study a collapse in a degenerate fermion-fermion mixture ( DFFM) of different atoms. Due to a strong Pauli-blocking repulsion among identical spin-polarized fermions at short distances, there cannot be a collapse for repulsive interspecies fermion fermion interaction. However, there can be a collapse for a sufficiently attractive interspecies fermion-fermion interaction in a DFFM of different atoms. Using a variational analysis and numerical solution of the hydrodynamic model, we study different aspects of collapse in such a DFFM initiated by a jump in the interspecies fermion-fermion interaction ( scattering length) to a large negative ( attractive) value using a Feshbach resonance. Suggestion for experiments of collapse in a DFFM of distinct atoms is made.

Hidden vorticity in binary Bose-Einstein condensates

We consider a binary Bose-Einstein condensate (BEC) described by a system of two-dimensional (2D) Gross-Pitaevskii equations with the harmonic-oscillator trapping potential. The intraspecies interactions are attractive, while the interaction between the species may have either sign. The same model applies to the copropagation of bimodal beams in photonic-crystal fibers. We consider a family of trapped hidden-vorticity (HV) modes in the form of bound states of two components with opposite vorticities S(1,2) = +/- 1, the total angular momentum being zero. A challenging problem is the stability of the HV modes. By means of a linear-stability analysis and direct simulations, stability domains are identified in a relevant parameter plane. In direct simulations, stable HV modes feature robustness against large perturbations, while unstable ones split into fragments whose number is identical to the azimuthal index of the fastest growing perturbation eigenmode. Conditions allowing for the creation of the HV modes in the experiment are discussed too. For comparison, a similar but simpler problem is studied in an analytical form, viz., the modulational instability of an HV state in a one-dimensional (1D) system with periodic boundary conditions (this system models a counterflow in a binary BEC mixture loaded into a toroidal trap or a bimodal optical beam coupled into a cylindrical shell). We demonstrate that the stabilization of the 1D HV modes is impossible, which stresses the significance of the stabilization of the HV modes in the 2D setting.

Surface miscibility of EPC/DOTAP/DOPE in binary and ternary mixed monolayers

Surface pressure (pi)-molecular area (A) curves were used to characterize the packing of pseudo-ternary mixed Langmuir monolayers of egg phosphatidylcholine (EPC), 1,2-dioleoyl-3-trimethylammonium propane (DOTAP) and L-alpha-dioleoyl phosphatidylethanolamine (DOPE). This pseudo-ternary mixture EPC/DOPE/DOTAP has been successfully employed in liposome formulations designed for DNA non-viral vectors. Pseudo-binary mixtures were also studied as a control. Miscibility behavior was inferred from pi-A curves applying the additivity rule by calculating the excess free energy of mixture (Delta G(Exc)). The interaction between the lipids was also deduced from the surface compressional modulus (C(s)(-1)). The deviation from ideality shows dependence on the lipid polar head type and monolayer composition. For lower DOPE concentrations, the forces are predominantly attractive. However, if the monolayer is DOPE rich, the DOTAP presence disturbs the PE-PE intermolecular interaction and the net interaction is then repulsive. The ternary monolayer EPC/DOPE/DOTAP presented itself in two configurations, modulated by the DOPE content, in a similar behavior to the DOPE/DOTAP monolayers. These results contribute to the understanding of the lipid interactions and packing in self-assembled systems associated with the in vitro and in vivo stability of liposomes. (C) 2010 Elsevier B.V. All rights reserved.

Segregation in binary and ternary liquid fluidized beds

The mechanism underlying segregation in liquid fluidized beds is investigated in this paper, A binary fluidized bed system not at a stable equilibrium condition. is modelled in the literature as forming a mixed part-corresponding to stable mixture-at the bottom of the bed and a pure layer of excess components always floating on the mixed part. On the basis of this model: (0 comprehensive criteria for binary particles of any type to mix/segregate, and (ii) mixing, segregation regime map in terms of size ratio and density ratio of the particles for a given fluidizing medium, are established in this work. Therefore, knowing the properties of given particles, a second type of particles can be chosen in order to avoid or to promote segregation according to the particular process requirements. The model is then advanced for multicomponent fluidized beds and validated against experimental results observed for ternary fluidized beds. (C) 2002 Elsevier Science B.V. All rights reserved.