992 resultados para Tés
Resumo:
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.
Resumo:
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.
Nachwort [und Auswahlbibliografie] zur Neuauflage von L. P. "Sozialpolitik in der Weimarer Republik"
Resumo:
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.
Resumo:
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.
Resumo:
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.
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En este artículo utilizamos un modelo de generaciones traslapadas con heterogeneidad en la tasa de impaciencia para mostrar que los efectos de un cambio tecnológico aumentador de capital no son simétricos en los agentes y pueden conllevar una reducci on en el consumo. La asimetría en la tasa de impaciencia de los agentes en un período, tiene consecuencias sobre los beneficios del cambio tecnológico para las generaciones futuras. Menores tasas de impaciencia llevan a mayores niveles de capital y de consumo, si se entiende que la economía tiene el suficiente nivel de capital per capita.
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Resumen tomado del autor. Incluye gr??ficos y tablas de datos
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El presente trabajo se estructuró en tres partes principalmente. El objetivo del trabajo es analizar las tendencias a futuro después de la entrada en vigencia de los tratados de libre comercio con Corea del sur y Estados Unidos. Para lograr este cometido, se empezará explicando el origen y desarrollo del sector automotriz en Colombia, las políticas e incentivos del gobierno que tuvieron lugar para estimular el desarrollo de la industria. Posteriormente, se analizará cómo fue el origen de las ensambladoras y la llegada de los primeros automotores al territorio nacional e igualmente el surgimiento de las primeras industrias del sector de autopartes como parte de una estrategia del gobierno y, como a partir de allí, se empezaron a conformar las principales asociaciones que tiene el sector automotriz. A su vez, se analizará el estado actual del sector automotriz en Colombia teniendo en cuenta el desarrollo económico, los principales actores que están involucrados en el sector y el papel del gobierno. Dentro de esta segunda parte también se analizará el rol de Colombia frente a Estados unidos y Corea, las relaciones comerciales y el perfil de los países firmantes, los cuales son claves para el desarrollo del sector. Finalmente, en la última parte del proyecto, se analizará la industria y su preparación ante la inminente llegada de productos provenientes del extranjero, se tendrá en cuenta las opiniones a favor y en contra diferentes expertos en el tema y finalmente se darán recomendaciones para la industria nacional que se podría aplicar en el mediano y largo plazo.
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Este trabajo de grado se realizó con el fin de hacer un diagnóstico para evaluar y analizar la estructuración un departamento de mercadeo en Rhodia Colombia, teniendo en cuenta la coyuntura actual de la compañía y su intensión expansionista en los mercados de industria química en Colombia. Para lograr esta intención es necesario que este departamento pueda llevar procesos de investigación alineados con las estrategias de Marketing que desarrolla Rhodia Brasil, y así mismo brindar a los gerentes comerciales información valiosa para realizar esfuerzos en los mercados potenciales de Rhodia y a los mercados en que se ha posicionado Solvay en Colombia. Las expectativas se fundamentan en lograr establecer un departamento de Mercadeo estructurado donde se lleven a cabo procesos de Marketing “Business to Business” en pro de buscar nuevas oportunidades de mercado, fortalecer la presencia comercial en nichos de mercado estratégicos y monitorear los mercados de la compañía para anticiparse ante los sucesos coyunturales donde interactúan los productos de Rhodia en Colombia.
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En este trabajo examinamos la migración de ciudadanos de la Ex-Unión Soviética a la ciudad de Bucaramanga. Migración que a pesar de su alto impacto regional no aparece en los registros estadísticos ni académicos. A través de las historias de vida reconstruimos los procesos migratorios de los migrantes, desde el momento en que deciden dejar sus regiones de origen, hasta su integración en la ciudad. Es un caso de estudio basado en varias teorias sobre la migración.
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En esta investigación se exploran distintas herramientas usadas por comunidades virtuales en Internet para la creación, difusión y defensa de sus ideas en contra de comunidades rivales y algunas veces la sociedad. El caso de estudio particular en que se ha centrado este trabajo es el de distintos grupos relacionados con la anorexia nerviosa y sus usos de la imagen de los nombres e imagen de usuario. La metodología de investigación usada es cualitativa y experimental.
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El presente trabajo de investigación, estudia a través del caso de la cohorte del 2000 de la Facultad de Ingeniería de la Universidad Distrital, el tipo de coyuntura que le permitió a este grupo de jóvenes reingresar a la Universidad y culminar la carrera al haber tenido que abandonarla en un primer momento, por problemas socio-económicos y/o académicos. Por medio del estudio del reintegro universitario, este trabajo se enmarca en el campo, poco explorado, de la existencia y efectividad de medidas de "segundas oportunidades" educativas que las instituciones de educación superior le ofrecen a estudiantes que por problemas de orden estructural se ven obligados a abandonar la Universidad.
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Características de la política por Internet en el marco de los contextos. Casos de estudio: la Obamanía en Estados Unidos y la Ola Verde en Colombia.