979 resultados para TS Manufacturas


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Puisque l’altération des habitats d’eau douce augmente, il devient critique d’identifier les composantes de l’habitat qui influencent les métriques de la productivité des pêcheries. Nous avons comparé la contribution relative de trois types de variables d’habitat à l’explication de la variance de métriques d’abondance, de biomasse et de richesse à l’aide de modèles d’habitat de poissons, et avons identifié les variables d’habitat les plus efficaces à expliquer ces variations. Au cours des étés 2012 et 2013, les communautés de poissons de 43 sites littoraux ont été échantillonnées dans le Lac du Bonnet, un réservoir dans le Sud-est du Manitoba (Canada). Sept scénarios d’échantillonnage, différant par l’engin de pêche, l’année et le moment de la journée, ont été utilisés pour estimer l’abondance, la biomasse et la richesse à chaque site, toutes espèces confondues. Trois types de variables d’habitat ont été évalués: des variables locales (à l’intérieur du site), des variables latérales (caractérisation de la berge) et des variables contextuelles (position relative à des attributs du paysage). Les variables d’habitat locales et contextuelles expliquaient en moyenne un total de 44 % (R2 ajusté) de la variation des métriques de la productivité des pêcheries, alors que les variables d’habitat latérales expliquaient seulement 2 % de la variation. Les variables les plus souvent significatives sont la couverture de macrophytes, la distance aux tributaires d’une largeur ≥ 50 m et la distance aux marais d’une superficie ≥ 100 000 m2, ce qui suggère que ces variables sont les plus efficaces à expliquer la variation des métriques de la productivité des pêcheries dans la zone littorale des réservoirs.

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Les personnes vieillissantes doivent composer au quotidien avec des douleurs chroniques. Le but de ce travail est de mieux comprendre les mécanismes sous-jacents qui contribueraient aux douleurs chroniques liées au vieillissement et par là, ouvrir un chemin vers de nouvelles perspectives thérapeutiques. Les contrôles inhibiteurs diffus nociceptifs (CIDN) ont un rôle qui n’est pas des moindres dans le contrôle de la douleur. Des études expérimentales examinant l’effet analgésique de la contre stimulation hétérotopique nociceptive (HNCS), un protocole permettant de tester l’efficacité de ces CIDN, suggèrent que le recrutement des CIDN au sein de cette population était plus faible (i.e. moins d’inhibition) comparé à une population plus jeune. En revanche, les études examinant la sensibilisation centrale induite par sommation temporelle (TS) de la douleur rapportent des résultats mitigés. De plus, une composante importante influençant l’expérience de douleur, les ressources cognitives, dont l’inhibition cognitive, se voient aussi décliner avec l’âge. Premièrement, le recrutement des CIDN a été comparé entre des participants sains, jeunes et des plus âgés avec la HNCS, et le recrutement des mécanismes de sensibilisation centrale avec la TS. La stimulation électrique du nerf sural a été choisie pour permettre de quantifier la douleur, tout en prenant une mesure indicative de la nociception spinale qu’est le réflexe nociceptif spinal (RIII). Nos sujets ont aussi participé à une tâche cognitive (le Stroop), testant l’inhibition cognitive. Deuxièmement, l’efficacité des CIDN ainsi que de l’inhibition cognitive a été testée chez les jeunes et les aînés en imagerie par résonance magnétique (IRM), afin de vérifier la relation entre ces deux mesures psychophysiques et l’épaisseur corticale des régions qui y sont impliquées ainsi que l’effet de l’âge sur celles-ci. Les résultats suggèrent un moindre recrutement des CIDN chez les plus âgés lors de l’expérimentation de la HNCS. Également, les sujets âgés présentaient des capacités d’inhibitions cognitives plus faibles que les jeunes. En plus, une corrélation entre l’inhibition cognitive et la modulation du réflexe RIII par la HNCS a été mise en évidence. Pour l’expérience de TS, les résultats étaient comparables pour les deux groupes, suggérant que les mécanismes impliqués dans la régulation de la douleur ne subiraient pas l’effet de l’âge de la même manière. Pour l’étude de l’épaisseur corticale, on y trouve une diminution globale de l’épaisseur corticale liée à l’âge, mais aussi une corrélation de l’analgésie par la HNCS avec l’inhibition cognitive et également, une relation des deux avec l’épaisseur corticale du cortex orbitofrontal (OFC) latéral gauche, suggérant la possibilité d’une existence d’un réseau neuronal au moins partiellement commun du contrôle inhibiteur descendant sensoriel et cognitif. Ce travail montre que l’effet de l’âge sur les mécanismes centraux de la régulation de la douleur est loin d’être uniforme. Également, il montre une corrélation entre la modulation endogène de la douleur et l’inhibition cognitive, ces deux processus seraient associés à une même région cérébrale. Ces résultats pourraient contribuer à identifier d’autres méthodes thérapeutiques, ouvrant ainsi une nouvelle avenue vers d’autres options dans la prise en charge des douleurs chroniques chez les personnes vieillissantes.

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The research work which was carried out to characterization of wastes from natural rubber and rubber wood processing industries and their utilization for biomethanation. Environmental contamination is an inevitable consequence of human activity. The liquid and solid wastes from natural rubber based industries were: characterized and their use for the production of biogas investigated with a view to conserve conventional energy, and to mitigate environmental degradation.Rubber tree (flevea brasiliensis Muell. Arg.), is the most important commercial source of natural rubber and in india. Recently, pollution from the rubber processing factories has become very serious due to the introduction of modern methods and centralized group processing practices.The possibility of the use of spent slurry as organic manure is discussed.l0 percent level of PSD, the activity of cellulolytic, acid producing,proteolytic, lipolytic and methanogenic bacteria were more in the middle stage of methanogenesis.the liquid wastes from rubber processing used as diluents in combination with PSD, SPE promoted more biogas production with high methane content in the gas.The factors that favour methane production like TS, VS, cellulose and hemicellulose degradation were favoured in this treatment which led to higher methane biogenesis.The results further highlight ways and means to use agricultural wastes as alternative sources of energy.

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The research work which was carried out to characterization of wastes from natural rubber and rubber wood processing industries and their utilization for biomethanation. Environmental contamination is an inevitable consequence of human activity. The liquid and solid wastes from natural rubber based industries were: characterized and their use for the production of biogas investigated with a view to conserve conventional energy, and to mitigate environmental degradation.Rubber tree (flevea brasiliensis Muell. Arg.), is the most important commercial source of natural rubber and in india. Recently, pollution from the rubber processing factories has become very serious due to the introduction of modern methods and centralized group processing practices.The possibility of the use of spent slurry as organic manure is discussed.l0 percent level of PSD, the activity of cellulolytic, acid producing,proteolytic, lipolytic and methanogenic bacteria were more in the middle stage of methanogenesis.the liquid wastes from rubber processing used as diluents in combination with PSD, SPE promoted more biogas production with high methane content in the gas.The factors that favour methane production like TS, VS, cellulose and hemicellulose degradation were favoured in this treatment which led to higher methane biogenesis.The results further highlight ways and means to use agricultural wastes as alternative sources of energy.

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Solid waste generation is a natural consequence of human activity and is increasing along with population growth, urbanization and industrialization. Improper disposal of the huge amount of solid waste seriously affects the environment and contributes to climate change by the release of greenhouse gases. Practicing anaerobic digestion (AD) for the organic fraction of municipal solid waste (OFMSW) can reduce emissions to environment and thereby alleviate the environmental problems together with production of biogas, an energy source, and digestate, a soil amendment. The amenability of substrate for biogasification varies from substrate to substrate and different environmental and operating conditions such as pH, temperature, type and quality of substrate, mixing, retention time etc. Therefore, the purpose of this research work is to develop feasible semi-dry anaerobic digestion process for the treatment of OFMSW from Kerala, India for potential energy recovery and sustainable waste management. This study was carried out in three phases in order to reach the research purpose. In the first phase, batch study of anaerobic digestion of OFMSW was carried out for 100 days at 32°C (mesophilic digestion) for varying substrate concentrations. The aim of this study was to obtain the optimal conditions for biogas production using response surface methodology (RSM). The parameters studied were initial pH, substrate concentration and total organic carbon (TOC). The experimental results showed that the linear model terms of initial pH and substrate concentration and the quadratic model terms of the substrate concentration and TOC had significant individual effect (p < 0.05) on biogas yield. However, there was no interactive effect between these variables (p > 0.05). The optimum conditions for maximizing the biogas yield were a substrate concentration of 99 g/l, an initial pH of 6.5 and TOC of 20.32 g/l. AD of OFMSW with optimized substrate concentration of 99 g/l [Total Solid (TS)-10.5%] is a semi-dry digestion system .Under the optimized condition, the maximum biogas yield was 53.4 L/kg VS (volatile solid).. In the second phase, semi-dry anaerobic digestion of organic solid wastes was conducted for 45 days in a lab-scale batch experiment for substrate concentration of 100 g/l (TS-11.2%) for investigating the start-up performances under thermophilic condition (50°C). The performance of the reactor was evaluated by measuring the daily biogas production and calculating the degradation of total solids and the total volatile solids. The biogas yield at the end of the digestion was 52.9 L/kg VS for the substrate concentration of 100 g/l. About 66.7% of volatile solid degradation was obtained during the digestion. A first order model based on the availability of substrate as the limiting factor was used to perform the kinetic studies of batch anaerobic digestion system. The value of reaction rate constant, k, obtained was 0.0249 day-1. A laboratory bench scale reactor with a capacity of 36.8 litres was designed and fabricated to carry out the continuous anaerobic digestion of OFMSW in the third phase. The purpose of this study was to evaluate the performance of the digester at total solid concentration of 12% (semi-dry) under mesophlic condition (32°C). The digester was operated with different organic loading rates (OLRs) and constant retention time. The performance of the reactor was evaluated using parameters such as pH, volatile fatty acid (VFA), alkalinity, chemical oxygen demand (COD), TOC and ammonia-N as well as biogas yield. During the reactor’s start-up period, the process is stable and there is no inhibition occurred and the average biogas production was 14.7 L/day. The reactor was fed in continuous mode with different OLRs (3.1,4.2 and 5.65 kg VS/m3/d) at constant retention time of 30 days. The highest volatile solid degradation of 65.9%, with specific biogas production of 368 L/kg VS fed was achieved with OLR of 3.1 kg VS/m3/d. Modelling and simulation of anaerobic digestion of OFMSW in continuous operation is done using adapted Anaerobic Digestion Model No 1 (ADM1).The proposed model, which has 34 dynamic state variables, considers both biochemical and physicochemical processes and contains several inhibition factors including three gas components. The number of processes considered is 28. The model is implemented in Matlab® version 7.11.0.584(R2010b). The model based on adapted ADM1 was tested to simulate the behaviour of a bioreactor for the mesophilic anaerobic digestion of OFMSW at OLR of 3.1 kg VS/m3/d. ADM1 showed acceptable simulating results.

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Ausgehend von zwei Beispielen wird in Abschnitt 1 der derzeitige Fachrechenunterricht in der Berufsschule kurz beschrieben (ausführlichere Analysen sind bei BARDY u, a. 1980 und bei BARDY/BLUM/BRAUN 1985 zu finden). Dann wird in Abschnitt 2 eine eigene Konzeption für den mathematischen Unterricht in der Berufsschule skizziert (ausführlicher ist diese Konzeption bei BLUM 1976 und BLUM 1981 dargestellt) und anhand der einleitenden Beispiele verdeutlicht.

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Diese Arbeit behandelt die Problemstellung der modellbasierten Fehlerdiagnose für Lipschitz-stetige nichtlineare Systeme mit Unsicherheiten. Es wird eine neue adaptive Fehlerdiagnosemethode vorgestellt. Erkenntnisse und Verfahren aus dem Bereich der Takagi-Sugeno (TS) Fuzzy-Modellbildung und des Beobachterentwurfs sowie der Sliding-Mode (SM) Theorie werden genutzt, um einen neuartigen robusten und nichtlinearen TS-SM-Beobachter zu entwickeln. Durch diese Zusammenführung lassen sich die jeweiligen Vorteile beider Ansätze miteinander kombinieren. Bedingungen zur Konvergenz des Beobachters werden als lineare Matrizenungleichungen (LMIs) abgeleitet. Diese Bedingungen garantieren zum einen die Stabilität und liefern zum anderen ein direktes Entwurfsverfahren für den Beobachter. Der Beobachterentwurf wird für die Fälle messbarer und nicht messbarer Prämissenvariablen angegeben. Durch die TS-Erweiterung des in dieser Arbeit verwendeten SM-Beobachters ist es möglich, den diskontinuierlichen Rückführterm mithilfe einer geeigneten kontinuierlichen Funktion zu approximieren und dieses Signal daraufhin zur Fehlerdiagnose auszuwerten. Dies liefert eine Methodik zur Aktor- und Sensorfehlerdiagnose nichtlinearer unsicherer Systeme. Gegenüber anderen Ansätzen erlaubt das Vorgehen eine quantitative Bestimmung und teilweise sogar exakte Rekonstruktion des Fehlersignalverlaufs. Darüber hinaus ermöglicht der Ansatz die Berechnung konstanter Fehlerschwellen direkt aus dem physikalischen Vorwissen über das betrachtete System. Durch eine Erweiterung um eine Betriebsphasenerkennung wird es möglich, die Schwellenwerte des Fehlerdiagnoseansatzes online an die aktuelle Betriebsphase anzupassen. Hierdurch ergibt sich in Betriebsphasen mit geringen Modellunsicherheiten eine deutlich erhöhte Fehlersensitivität. Zudem werden in Betriebsphasen mit großen Modellunsicherheiten Falschalarme vermieden. Die Kernidee besteht darin, die aktuelle Betriebsphase mittels eines Bayes-Klassikators in Echtzeit zu ermitteln und darüber die Fehlerschwellen an die a-priori de nierten Unsicherheiten der unterschiedlichen Betriebsphasen anzupassen. Die E ffektivität und Übertragbarkeit der vorgeschlagenen Ansätze werden einerseits am akademischen Beispiel des Pendelwagens und anderseits am Beispiel der Sensorfehlerdiagnose hydrostatisch angetriebener Radlader als praxisnahe Anwendung demonstriert.

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Summary - Cooking banana is one of the most important crops in Uganda; it is a staple food and source of household income in rural areas. The most common cooking banana is locally called matooke, a Musa sp triploid acuminate genome group (AAA-EAHB). It is perishable and traded in fresh form leading to very high postharvest losses (22-45%). This is attributed to: non-uniform level of harvest maturity, poor handling, bulk transportation and lack of value addition/processing technologies, which are currently the main challenges for trade and export, and diversified utilization of matooke. Drying is one of the oldest technologies employed in processing of agricultural produce. A lot of research has been carried out on drying of fruits and vegetables, but little information is available on matooke. Drying of matooke and milling it to flour extends its shelf-life is an important means to overcome the above challenges. Raw matooke flour is a generic flour developed to improve shelf stability of the fruit and to find alternative uses. It is rich in starch (80 - 85%db) and subsequently has a high potential as a calorie resource base. It possesses good properties for both food and non-food industrial use. Some effort has been done to commercialize the processing of matooke but there is still limited information on its processing into flour. It was imperative to carry out an in-depth study to bridge the following gaps: lack of accurate information on the maturity window within which matooke for processing into flour can be harvested leading to non-uniform quality of matooke flour; there is no information on moisture sorption isotherm for matooke from which the minimum equilibrium moisture content in relation to temperature and relative humidity is obtainable, below which the dry matooke would be microbiologically shelf-stable; and lack of information on drying behavior of matooke and standardized processing parameters for matooke in relation to physicochemical properties of the flour. The main objective of the study was to establish the optimum harvest maturity window and optimize the processing parameters for obtaining standardized microbiologically shelf-stable matooke flour with good starch quality attributes. This research was designed to: i) establish the optimum maturity harvest window within which matooke can be harvested to produce a consistent quality of matooke flour, ii) establish the sorption isotherms for matooke, iii) establish the effect of process parameters on drying characteristics of matooke, iv) optimize the drying process parameters for matooke, v) validate the models of maturity and optimum process parameters and vi) standardize process parameters for commercial processing of matooke. Samples were obtained from a banana plantation at Presidential Initiative on Banana Industrial Development (PIBID), Technology Business Incubation Center (TBI) at Nyaruzunga – Bushenyi in Western Uganda. A completely randomized design (CRD) was employed in selecting the banana stools from which samples for the experiments were picked. The cultivar Mbwazirume which is soft cooking and commonly grown in Bushenyi was selected for the study. The static gravitation method recommended by COST 90 Project (Wolf et al., 1985), was used for determination of moisture sorption isotherms. A research dryer developed for this research. All experiments were carried out in laboratories at TBI. The physiological maturity of matooke cv. mbwazirume at Bushenyi is 21 weeks. The optimum harvest maturity window for commercial processing of matooke flour (Raw Tooke Flour - RTF) at Bushenyi is between 15-21 weeks. The finger weight model is recommended for farmers to estimate harvest maturity for matooke and the combined model of finger weight and pulp peel ratio is recommended for commercial processors. Matooke isotherms exhibited type II curve behavior which is characteristic of foodstuffs. The GAB model best described all the adsorption and desorption moisture isotherms. For commercial processing of matooke, in order to obtain a microbiologically shelf-stable dry product. It is recommended to dry it to moisture content below or equal to 10% (wb). The hysteresis phenomenon was exhibited by the moisture sorption isotherms for matooke. The isoteric heat of sorption for both adsorptions and desorption isotherms increased with decreased moisture content. The total isosteric heat of sorption for matooke: adsorption isotherm ranged from 4,586 – 2,386 kJ/kg and desorption isotherm from 18,194– 2,391 kJ/kg for equilibrium moisture content from 0.3 – 0.01 (db) respectively. The minimum energy required for drying matooke from 80 – 10% (wb) is 8,124 kJ/kg of water removed. Implying that the minimum energy required for drying of 1 kg of fresh matooke from 80 - 10% (wb) is 5,793 kJ. The drying of matooke takes place in three steps: the warm-up and the two falling rate periods. The drying rate constant for all processing parameters ranged from 5,793 kJ and effective diffusivity ranged from 1.5E-10 - 8.27E-10 m2/s. The activation energy (Ea) for matooke was 16.3kJ/mol (1,605 kJ/kg). Comparing the activation energy (Ea) with the net isosteric heat of sorption for desorption isotherm (qst) (1,297.62) at 0.1 (kg water/kg dry matter), indicated that Ea was higher than qst suggesting that moisture molecules travel in liquid form in matooke slices. The total color difference (ΔE*) between the fresh and dry samples, was lowest for effect of thickness of 7 mm, followed by air velocity of 6 m/s, and then drying air temperature at 70˚C. The drying system controlled by set surface product temperature, reduced the drying time by 50% compared to that of a drying system controlled by set air drying temperature. The processing parameters did not have a significant effect on physicochemical and quality attributes, suggesting that any drying air temperature can be used in the initial stages of drying as long as the product temperature does not exceed gelatinization temperature of matooke (72˚C). The optimum processing parameters for single-layer drying of matooke are: thickness = 3 mm, air temperatures 70˚C, dew point temperature 18˚C and air velocity 6 m/s overflow mode. From practical point of view it is recommended that for commercial processing of matooke, to employ multi-layer drying of loading capacity equal or less than 7 kg/m², thickness 3 mm, air temperatures 70˚C, dew point temperature 18˚C and air velocity 6 m/s overflow mode.

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Manufacturas Hortúa Leal (MHL) es una PYME familiar dedicada a la producción de calzado y artículos de cuero. Debido a la sobre oferta en el mercado colombiano, la empresa ha perdido clientes importantes y como consecuencia sus ganancias han disminuido considerablemente durante los últimos años. Para garantizar la perdurabilidad de la organización, la gerencia ha propuesto como alternativa la búsqueda de mercados extranjeros para exportar el calzado. El problema radica en la inexperiencia de la empresa en materia de exportación y en la incertidumbre del mercado al que se debe exportar. Este trabajo se enfoca en medir el potencial exportador de la empresa para determinar si está en condiciones de desarrollar un proceso de expansión y examinar a través de un filtro los países candidatos para exportar el calzado.

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Se caracterizan las malformaciones renales y urinarias (MRU), y cardiovasculares (CV), así como la función renal (FR) y la presión arterial (PA) en pacientes con Sindrome de Turner (ST) mediante un estudio retrospectivo entre 1999 y 2009 en Bogotá. Se encontró 10 pacientes con algún grado de insuficiencia renal crónica (IRC). Además 4 pacientes presentaron prehipertensión arterial, y 5 (HTA); en ellos se encontró hidronefrosis y riñón poliquístico. Las MRU más frecuentes fueron únicas; en ellas las mayores alteraciones cromosómicas son la monosomía y el mosaicismo. La mayor malformación CV fué la válvula aórtica bicúspide. El ST amerita seguimiento de FR y PA para prevenir complicaciones a largo plazo por IRC e HTA.