997 resultados para PLA Folding


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The core descriptions (chapter 7) summarize the most important results of the analysis of each sediment core following procedures applied during ODP/IODP expeditions. All cores were opened, described, and color-scanned. In the core descriptions the first column displays the lithological data that are based on visual analysis of the core and are supplemented by information from binocular and smear slide analyses. The sediment classification largely follows ODP/IODP convention. Lithological names consist of a principal name based on composition, degree of lithification, and/or texture as determined from visual description and microscopic observations. In the structure column the intensity of bioturbation together with individual or special features (turbidites, volcanic ash layers, plant debris, shell fragments, etc.) is shown. The hue and chroma attributes of color were determined by comparison with the Munsell soil color charts and are given in the color column in the Munsell notation. A GretagMacbethTM Spectrolino spectrophotometer was used to measure percent reflectance values of sediment color at 36 wavelength channels over the visible light range (380-730 nm) on all of the cores. The digital reflectance data of the spectrophotometer readings were routinely obtained from the surface (measured in 1 cm steps) of the split cores (archive half). The Spectrolino is equipped with a measuring aperture with folding mechanism allowing an exact positioning on the split core and is connected to a portable computer. The data are directly displayed within the software package Excel and can be controlled simultaneously. From all the color measurements, for each core the red/blue ratio (700 nm/450 nm) and the lightness are shown together with the visual core description. The reflectance of individual wavelengths is often significantly affected by the presence of minor amounts of oxyhydroxides or sulphides. To eliminate these effects, we used the red/blue ratio and lightness.

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Copia digital: Biblioteca valenciana, 2010

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Implants that can be metabolized by the human body have appeared as one of the most attractive and promising solutions to overcome limitations and improve the features of current implantable devices. Biodegradable polymers and magnesium (Mg) alloys have played an important role writing the history of resorbable implants [1,2]. This paper presents the processing by extrusion/compression moulding, mechanical characterization, thermal characterization and in vitro biocompatibility of a novel generation of resorbable materials based on a polymeric matrix reinforced with metallic Mg particles.

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Los polímeros compostables suponen en torno al 30% de los bioplásticos destinados a envasado, siendo a su vez esta aplicación el principal destino de la producción de este tipo de materiales que, en el año 2013, superó 1,6 millones de toneladas. La presente tesis aborda la biodegradación de los residuos de envases domésticos compostables en medio aerobio para dos tipos de formato y materiales, envase rígido de PLA (Clase I) y dos tipos de bolsas de PBAT+PLA (Clases II y III). Sobre esta materia se han realizado diversos estudios en escala de laboratorio pero para otro tipo de envases y biopolímeros y bajo condiciones controladas del compost con alguna proyección particularizada en plantas. La presente tesis da un paso más e investiga el comportamiento real de los envases plásticos compostables en la práctica del compostaje en tecnologías de pila y túnel, tanto a escala piloto como industrial, dentro del procedimiento y con las condiciones ambientales de instalaciones concretas. Para ello, con el método seguido, se han analizado los requisitos básicos que debe cumplir un envase compostable, según la norma UNE – EN 13432, evaluando el porcentaje de biodegradación de los envases objeto de estudio, en función de la pérdida de peso seco tras el proceso de compostaje, y la calidad del compost obtenido, mediante análisis físico-químico y de fitotoxicidad para comprobar que los materiales de estudio no aportan toxicidad. En cuanto a los niveles de biodegrabilidad, los resultados permiten concluir que los envases de Clase I se compostan adecuadamente en ambas tecnologías y que no requieren de unas condiciones de proceso muy exigentes para alcanzar niveles de biodegradación del 100%. En relación a los envases de Clase II, se puede asumir que se trata de un material que se composta adecuadamente en pila y túnel industrial pero que requiere de condiciones exigentes para alcanzar niveles de biodegradación del 100% al afectarle de forma clara la ubicación de las muestras en la masa a compostar, especialmente en el caso de la tecnología de túnel. Mientras el 90% de las muestras alcanza el 100% de biodegradación en pila industrial, tan sólo el 50% lo consigue en la tecnología de túnel a la misma escala. En cuanto a los envases de Clase III, se puede afirmar que es un material que se composta adecuadamente en túnel industrial pero que requiere de condiciones de cierta exigencia para alcanzar niveles de biodegradación del 100% al poderle afectar la ubicación de las muestras en la masa a compostar. El 75% de las muestras ensayadas en túnel a escala industrial alcanzan el 100% de biodegradación y, aunque no se ha ensayado este tipo de envase en la tecnología de pila al no disponer de muestras, cabe pensar que los resultados de biodegrabilidad que hubiera podido alcanzar habrían sido, como mínimo, los obtenidos para los envases de Clase II, al tratarse de materiales muy similares en composición. Por último, se concluye que la tecnología de pila es más adecuada para conseguir niveles de biodegradación superiores en los envases tipo bolsa de PBAT+PLA. Los resultados obtenidos permiten también sacar en conclusión que, en el diseño de instalaciones de compostaje para el tratamiento de la fracción orgánica recogida selectivamente, sería conveniente realizar una recirculación del rechazo del afino del material compostado para aumentar la probabilidad de someter este tipo de materiales a las condiciones ambientales adecuadas. Si además se realiza un triturado del residuo a la entrada del proceso, también se aumentaría la superficie específica a entrar en contacto con la masa de materia orgánica y por tanto se favorecerían las condiciones de biodegradación. En cuanto a la calidad del compost obtenido en los ensayos, los resultados de los análisis físico – químicos y de fitotoxicidad revelan que los niveles de concentración de microorganismo patógenos y de metales pesados superan, en la práctica totalidad de las muestras, los niveles máximos permitidos en la legislación vigente aplicable a productos fertilizantes elaborados con residuos. Mediante el análisis de la composición de los envases ensayados se constata que la causa de esta contaminación reside en la materia orgánica utilizada para compostar en los ensayos, procedente del residuo de origen doméstico de la denominada “fracción resto”. Esta conclusión confirma la necesidad de realizar una recogida selectiva de la fracción orgánica en origen, existiendo estudios que evidencian la mejora de la calidad del residuo recogido en la denominada “fracción orgánica recogida selectivamente” (FORM). Compostable polymers are approximately 30% of bioplastics used for packaging, being this application, at same time, the main destination for the production of such materials exceeded 1.6 million tonnes in 2013. This thesis deals with the biodegradation of household packaging waste compostable in aerobic medium for two format types and materials, rigid container made of PLA (Class I) and two types of bags made of PBAT + PLA (Classes II and III). There are several studies developed about this issue at laboratory scale but for other kinds of packaging and biopolymers and under composting controlled conditions with some specifically plants projection. This thesis goes one step further and researches the real behaviour of compostable plastic packaging in the composting practice in pile and tunnel technologies, both at pilot and industrial scale, within the procedure and environmental conditions of concrete devices. Therefore, with a followed method, basic requirements fulfilment for compostable packaging have been analysed according to UNE-EN 13432 standard. It has been assessed the biodegradability percentage of the packaging studied, based on loss dry weight after the composting process, and the quality of the compost obtained, based on physical-chemical analysis to check no toxicity provided by the studied materials. Regarding biodegradability levels, results allow to conclude that Class I packaging are composted properly in both technologies and do not require high exigent process conditions for achieving 100% biodegradability levels. Related to Class II packaging, it can be assumed that it is a material that composts properly in pile and tunnel at industrial scale but requires exigent conditions for achieving 100% biodegradability levels for being clearly affected by sample location in the composting mass, especially in tunnel technology case. While 90% of the samples reach 100% of biodegradation in pile at industrial scale, only 50% achieve it in tunnel technology at the same scale. Regarding Class III packaging, it can be said that it is a material properly composted in tunnel at industrial scale but requires certain exigent conditions for reaching 100% biodegradation levels for being possibly affected by sample location in the composting mass. The 75% of the samples tested in tunnel at industrial scale reaches 100% biodegradation. Although this kind of packaging has not been tested on pile technology due to unavailability of samples, it is judged that biodegradability results that could be reached would have been, at least, the same obtained for Class II packaging, as they are very similar materials in composition. Finally, it is concluded that pile technology is more suitable for achieving highest biodegradation levels in bag packaging type of PBAT+PLA. Additionally, the obtained results conclude that, in the designing of composting devices for treatment of organic fraction selectively collected, it would be recommended a recirculation of the refining refuse of composted material in order to increase the probability of such materials to expose to proper environmental conditions. If the waste is grinded before entering the process, the specific surface in contact with organic material would also be increased and therefore biodegradation conditions would be more favourable. Regarding quality of the compost obtained in the tests, physical-chemical and phytotoxicity analysis results reveal that pathogen microorganism and heavy metals concentrations exceed, in most of the samples, the maximum allowed levels by current legislation for fertilizers obtained from wastes. Composition analysis of tested packaging verifies that the reason for this contamination is the organic material used for composting tests, comes from the household waste called “rest fraction”. This conclusion confirms the need of a selective collection of organic fraction in the origin, as existing studies show the quality improvement of the waste collected in the so-called “organic fraction selectively collected” (FORM).

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Protein folding occurs on a time scale ranging from milliseconds to minutes for a majority of proteins. Computer simulation of protein folding, from a random configuration to the native structure, is nontrivial owing to the large disparity between the simulation and folding time scales. As an effort to overcome this limitation, simple models with idealized protein subdomains, e.g., the diffusion–collision model of Karplus and Weaver, have gained some popularity. We present here new results for the folding of a four-helix bundle within the framework of the diffusion–collision model. Even with such simplifying assumptions, a direct application of standard Brownian dynamics methods would consume 10,000 processor-years on current supercomputers. We circumvent this difficulty by invoking a special Brownian dynamics simulation. The method features the calculation of the mean passage time of an event from the flux overpopulation method and the sampling of events that lead to productive collisions even if their probability is extremely small (because of large free-energy barriers that separate them from the higher probability events). Using these developments, we demonstrate that a coarse-grained model of the four-helix bundle can be simulated in several days on current supercomputers. Furthermore, such simulations yield folding times that are in the range of time scales observed in experiments.

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Hydrogen–deuterium exchange experiments have been used previously to investigate the structures of well defined states of a given protein. These include the native state, the unfolded state, and any intermediates that can be stably populated at equilibrium. More recently, the hydrogen–deuterium exchange technique has been applied in kinetic labeling experiments to probe the structures of transiently formed intermediates on the kinetic folding pathway of a given protein. From these equilibrium and nonequilibrium studies, protection factors are usually obtained. These protection factors are defined as the ratio of the rate of exchange of a given backbone amide when it is in a fully solvent-exposed state (usually obtained from model peptides) to the rate of exchange of that amide in some state of the protein or in some intermediate on the folding pathway of the protein. This definition is straightforward for the case of equilibrium studies; however, it is less clear-cut for the case of transient kinetic intermediates. To clarify the concept for the case of burst-phase intermediates, we have introduced and mathematically defined two different types of protection factors: one is Pstruc, which is more related to the structure of the intermediate, and the other is Papp, which is more related to the stability of the intermediate. Kinetic hydrogen–deuterium exchange data from disulfide-intact ribonuclease A and from cytochrome c are discussed to explain the use and implications of these two definitions.

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An antibody generated to an α-keto amide containing hapten 1 catalyzes the cis-trans isomerization of peptidyl-prolyl amide bonds in peptides and in the protein RNase T1. The antibody-catalyzed peptide isomerization reaction showed saturation kinetics for the cis-substrate, Suc-Ala-Ala-Pro-Phe-pNA, with a kcat/Km value of 883 s−1⋅M−1; the reaction was inhibited by the hapten analog 13 (Ki = 3.0 ± 0.4 μM). Refolding of denatured RNase T1 to its native conformation also was catalyzed by the antibody, with the antibody-catalyzed folding reaction inhibitable both by the hapten 1 and hapten analog 13. These results demonstrate that antibodies can catalyze conformational changes in protein structure, a transformation involved in many cellular processes.

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The chaperonin GroEL is an oligomeric double ring structure that, together with the cochaperonin GroES, assists protein folding. Biochemical analyses indicate that folding occurs in a cis ternary complex in which substrate is sequestered within the GroEL central cavity underneath GroES. Recently, however, studies of GroEL “minichaperones” containing only the apical substrate binding subdomain have questioned the functional importance of substrate encapsulation within GroEL-GroES complexes. Minichaperones were reported to assist folding despite the fact that they are monomeric and therefore cannot form a central cavity. Here we compare directly the folding activity of minichaperones with that of the full GroEL-GroES system. In agreement with earlier studies, minichaperones assist folding of some proteins. However, this effect is observed only under conditions where substantial spontaneous folding is also observed and is indistinguishable from that resulting from addition of the nonchaperone protein α-casein. By contrast, the full GroE system efficiently promotes folding of several substrates under conditions where essentially no spontaneous folding is observed. These data argue that the full GroEL folding activity requires the intact GroEL-GroES complex, and in light of previous studies, underscore the importance of substrate encapsulation for providing a folding environment distinct from the bulk solution.

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Divalent metal ions, such as Mg2+, are generally required for tertiary structure formation in RNA. Although the role of Mg2+ binding in RNA-folding equilibria has been studied extensively, little is known about the role of Mg2+ in RNA-folding kinetics. In this paper, we explore the effect of Mg2+ on the rate-limiting step in the kinetic folding pathway of the Tetrahymena ribozyme. Analysis of these data reveals the presence of a Mg2+-stabilized kinetic trap that slows folding at higher Mg2+ concentrations. Thus, the Tetrahymena ribozyme folds with an optimal rate at 2 mM Mg2+, just above the concentration required for stable structure formation. These results suggest that thermodynamic and kinetic folding of RNA are cooptimized at a Mg2+ concentration that is sufficient to stabilize the folded form but low enough to avoid kinetic traps and misfolding.