15 resultados para decanting
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Trabalho Final de Mestrado para obtenção do grau de Mestre em Engenharia Química
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The objective of this work was to clarify whether the method to extract nematodes from European soils is suitable for forest soils and litter in the eastern of Paraná state, Brazil, and whether nematode abundance differs between sites with different ecosystems and levels of human interference. The study sites were situated in the coastal area of the Serra do Mar, near the town of Antonina, in Eastern Paraná, Brazil. Cobb's sieving and decanting method was more appropriate than ISO method, since extraction efficiency was higher and intra-sample variability was significantly lower. In order to achieve an extraction efficiency higher than 90%, Cobb's method was modified. For the extraction of nematodes from litter, the Baermann funnel, with an extraction time of 48 hours, yielded an extraction efficiency higher than 90%. Nematode abundance in litter was higher than in soil. The mean number of individuals extracted from the litter increased with the age stage of the forest sites sampled, and there was no difference in the number of individuals in the soil of the four forest sites. Mean nematode abundance in soil in banana plantations was about twice as high compared to the banana-palmito mixed stands and to the forest sites.
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In the sparsely populated areas of Finland there are approximately 350 000 households and 450 000 leisure time residences outside sewer networks. According to the Finnish domestic wastewater act outside sewer networks, the Finnish Government is reducing the environmental load of domestic wastewaters by the year 2017. The law is aimed at restricting the quality of sludge from domestic wastewater purification systems. The wastewater purification systems are complex systems, which often include sedimentation basins. The sedimentation basins remove most of the nutrients from the domestic wastewaters. The Finnish Government has decided that sedimentation basin sludge must be treated before reusing. One possibility is to stabilise domestic sludge with slaked lime and to reuse treated sludge in agriculture. According to this master’s thesis lime stabilisation can be done in sedimentation basins or in decanting tanks. Decanting tanks must be under 100 m3. Dosage of stabilisation is 8,5 kg/m3 of lime. If you are treading sludge that is highly hydrous, you need 13,5 kg/m3 of lime. In stabilisation lime and sludge must be thoroughly mixed. Mixed sludge must be in sedimentation basin at least two hours. If there is evidence that sludge contains salmonella or if it’s decanting tank stabilisation time is 48 hours. Sludge must be mixed at least once during the longer stabilisation time. Lime destroys Esherichia coli and enterococcus concentrations below accepted level. Lime also destroys Salmonella bacterium. After treating, sludge’s can be distributed over a field. You can safely spread lime treated domestic sludge’s about 40 m3/ha. Lime stabilisation can also be used to treat separately and collectively collected domestic wastewaters.
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This work describes the results of the purification of methyl biodiesel, obtained by oxidized soybean oil, using different methods. After the ester separation from the glycerin by decanting, the ester was purified each time with distillation, washing with water and adsorption with bauxite, bentonite and attapulgite. The removal of total contamination, unsaponifiable material, concentrations of free glycerin and soap were analyzed in the purified ester phase. The best result of purification was observed with the use of bentonite and bauxite, in the removal of soap and free glycerin respectively.
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This paper evaluates the efficiency of geotextile filters for sludge from a compact water treatment plant (WTP). The key aspects required in the methodology of selection and designing geotextile filters for sludge from dewatering was investigated based on laboratory tests results. The analyses were supported by the measured filtrated volume of water and turbidity resulting from variable head permeability tests carried out in two geotextiles and using the conventional granular filter (sand and gravel). The results of the present study showed that more than 75% of the dewatering sludge can be filtrated with low turbidity, which permits that this water can return to the treatment plan in order to be reuse in another cycle. The reduced volume of sludge retained by the geotextile that is transferred to the drying pound increases its efficiency by reducing the drying time. The low volume of the dry waste can be removed and the geotextile can be easily cleaned or replaced when needed. These procedures significantly reduce the volume of water needed in dewatering and also avoids waste discharges in the environment.
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Phosphorus is considered an essential element for plants and it is found in small amounts in Brazilian soils. The filter cake residue, composed of a mixture of bagasse and decanting sludge, has high levels of organic matter, phosphorus and calcium. The phosphorus present in the filter cake is organic, and its release, as it happens to the nitrogen, occurs gradually by mineralization and by microorganisms attack in the soil. This study aimed to evaluate sugarcane vegetative growth and yield under fertilization with filter cake enriched with soluble phosphate. The experiment was carried out in Presidente Prudente, São Paulo State, Brazil, by using a randomized complete block design, in a 5x4 factorial scheme, where the first factor consisted of filter cake doses (0 t ha-1, 0.5 t ha-1, 1.0 t ha-1, 2.0 t ha-1, and 4.0 t ha-1) and the second of phosphorus fertilizer doses (0 kg ha-1, 50 kg ha -1, 100 kg ha-1, and 200 kg ha-1 of P 2O5), with 4 repetitions, totalizing 80 plots. The experiment evaluated the tiller number, at 30, 60, 90, and 120 days after planting, oBrix, and yield. The stalk yield and tillering were influenced by the filter cake rates applied to the soil. Filter cake doses and their combination with phosphate did not change the juice quality (Brix) at harvest.
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Neste trabalho foi estudado o processo de craqueamento termocatalítico do óleo de fritura nas escalas de bancada e piloto, variando-se o percentual do catalisador carbonato de sódio de 5 e 10% m/m em relação a matéria prima utilizada e temperatura de 440 ºC. O objetivo foi obter misturas de hidrocarbonetos ricas na fração diesel. O óleo de fritura neutralizado e seco foi caracterizado em relação ao Índice de Acidez, Índice de saponificação, Viscosidade Cinemática, Densidade e Índice de Refração. Após o craqueamento, o produto líquido obtido foi purificado por decantação da fase aquosa e filtração simples em escala de bancada. Esse produto foi fracionado por destilação fracionada e os condensados foram coletados em um funil de decantação de acordo a faixa de destilação da gasolina (40ºC-175ºC), querosene (175ºC-235ºC), diesel leve (235°C-305ºC) e diesel pesado (305ºC-400 ºC). Foi realizada a caracterização tanto físico química quanto da composição dos produtos líquidos e suas respectivas frações. Também foi realizada a evolução do processo de craqueamento em escala piloto, acompanhando o comportamento das características físico químicas e de composição do produto formado no decorrer do processo de craqueamento. Os resultados mostraram que o catalisador carbonato de sódio forneceu produtos de baixa acidez e com boas características para uso como combustível. A variação do percentual de catalisador influencia significamente as propriedades físico químicas e composição tanto do produto quanto de suas frações. Verificou-se, ainda, que o craqueamento termocatalítico do óleo de fritura propicia a formação de hidrocarbonetos ricos na fração do diesel (19,16% diesel leve e 41,18% diesel pesado para o teste com 10% de Na2CO3 e de 13,53% leve e 52,73% diesel pesado para o teste com 5% de Na2CO3 ). Os intervalos de tempos finais do craqueamento geram um combustível com baixo teor de acidez e com propriedades físico químicas em conformidade a norma especificada para o diesel mineral.
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Neste trabalho foi estudado o processo de destilação do produto líquido orgânico, obtido no craqueamento catalítico do óleo de palma (Elaeis guineensis, Jacq) bruto em escala piloto, empregando os catalisadores carbonato de sódio (Na2CO3) e a lama vermelha, variando o percentual de catalisador em 10% m/m e 15% m/m em relação à matéria prima utilizada, sendo fixada uma temperatura operacional de 450ºC, visando obter frações de biocombustíveis (bio-gasolina, bio-querosene e bio-óleo) semelhantes aos combustíveis derivados do petróleo. Os catalisadores foram submetidos a um pré-tratamento de desidratação durante 2 horas em uma estufa à 300ºC, posteriormente foram realizadas as análises de DRX, IR e TG. Quanto à matéria prima, foram realizadas análises físico-químicas, visando à caracterização do óleo de palma. Os produtos líquidos orgânicos (PLOs) obtidos foram submetidos a operações unitárias de separação, decantação e filtração simples em escala de bancada, para posteriormente serem realizadas análises físico-químicas e composicionais. Os PLOs foram destilados em uma coluna Vigreux de seis (06) estágios, e as frações condensadas foram coletadas de acordo com as faixas de destilação da gasolina (60ºC - 190ºC), querosene (190ºC - 235ºC) e diesel (235°C - 370ºC), para posteriormente serem caracterizadas. Verificou-se uma melhor eficiência para o catalisador carbonato de sódio a 15% m/m quanto a redução do índice de acidez, cerca de 1,7 mgKOH/g, assim como uma conversão mássica de 97% do óleo em PLO, notou-se também que, ao aumentar a quantidade de catalisador, isto favoreceu a obtenção de um produto final com uma melhor qualidade. A lama vermelha por outro lado, apresentou rendimentos de até 64% m/m e produtos com baixa acidez cerca de 62,90 mgKOH/g, comparando este resultado com dados encontrados na literatura. A partir dos resultados finais, verificou-se a eficiência dos catalisadores, no qual o catalisador carbonato de sódio forneceu produtos com baixa acidez e com boas características para uso como combustível.
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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)
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Pós-graduação em Engenharia Mecânica - FEIS
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
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It is well known that gases adsorb on many surfaces, in particular metal surfaces. There are two main forms responsible for these effects (i) physisorption and (ii) chemisorption. Physisorption is associated with lower binding energies in the order of 1–10 kJ mol−¹, compared to chemisorption which ranges from 100 to 1000 kJ mol−¹. Furthermore, chemisorption only forms monolayers, contrasting physisorption that can form multilayer adsorption. The reverse process is called desorption and follows similar mathematical laws; however, it can be influenced by hysteresis effects. In the present experiment, we investigated the adsorption/desorption phenomena on three steel and three aluminium cylinders containing compressed air in our laboratory and under controlled conditions in a climate chamber, respectively. Our observations from completely decanting one steel and two aluminium cylinders are in agreement with the pressure dependence of physisorption for CO₂, CH₄, and H₂O. The CO₂ results for both cylinder types are in excellent agreement with the pressure dependence of a monolayer adsorption model. However, mole fraction changes due to adsorption on aluminium (< 0.05 and 0 ppm for CO₂ and H₂O) were significantly lower than on steel (< 0.41 ppm and about < 2.5 ppm, respectively). The CO₂ amount adsorbed (5.8 × 1019 CO₂ molecules) corresponds to about the fivefold monolayer adsorption, indicating that the effective surface exposed for adsorption is significantly larger than the geometric surface area. Adsorption/desorption effects were minimal for CH₄ and for CO but require further attention since they were only studied on one aluminium cylinder with a very low mole fraction. In the climate chamber, the cylinders were exposed to temperatures between −10 and +50 °C to determine the corresponding temperature coefficients of adsorption. Again, we found distinctly different values for CO₂, ranging from 0.0014 to 0.0184 ppm °C−¹ for steel cylinders and −0.0002 to −0.0003 ppm °C−¹ for aluminium cylinders. The reversed temperature dependence for aluminium cylinders points to significantly lower desorption energies than for steel cylinders and due to the small values, they might at least partly be influenced by temperature, permeation from/to sealing materials, and gas-consumption-induced pressure changes. Temperature coefficients for CH₄, CO, and H₂O adsorption were, within their error bands, insignificant. These results do indicate the need for careful selection and usage of gas cylinders for high-precision calibration purposes such as requested in trace gas applications.
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La industria vitivinícola genera efluentes sólidos y líquidos en cantidad apreciable. Los sólidos son aprovechados en distintas aplicaciones e inclusive tienen valor comercial. En cambio, los líquidos pueden originar problemas cuando es necesario decidir cómo desecharlos o transformarlos en desechables. En Mendoza (Argentina), es común enviarlos después de su decantación a cauces y campos abiertos. En ambos casos aparece un serio riesgo de contaminación. Visto que generalmente se desconoce la composición de tales efluentes, este trabajo pretende caracterizarlos físico-químicamente en el período de elaboración de vinos, determinando: pH, conductividad eléctrica, DBO, DQO, cloruros, sulfatos, carbonatos y bicarbonatos, calcio, magnesio, sodio y potasio. La calidad de los efluentes varía notablemente con el agua empleada en los lavados, que aporta mayoritariamente aniones y cationes. Cuando el agua de lavado es abundante, los valores de pH, DBO y DQO de los efluentes permiten su eliminación junto con otros residuos cloacales o en campo abierto.
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OntoTag - A Linguistic and Ontological Annotation Model Suitable for the Semantic Web
1. INTRODUCTION. LINGUISTIC TOOLS AND ANNOTATIONS: THEIR LIGHTS AND SHADOWS
Computational Linguistics is already a consolidated research area. It builds upon the results of other two major ones, namely Linguistics and Computer Science and Engineering, and it aims at developing computational models of human language (or natural language, as it is termed in this area). Possibly, its most well-known applications are the different tools developed so far for processing human language, such as machine translation systems and speech recognizers or dictation programs.
These tools for processing human language are commonly referred to as linguistic tools. Apart from the examples mentioned above, there are also other types of linguistic tools that perhaps are not so well-known, but on which most of the other applications of Computational Linguistics are built. These other types of linguistic tools comprise POS taggers, natural language parsers and semantic taggers, amongst others. All of them can be termed linguistic annotation tools.
Linguistic annotation tools are important assets. In fact, POS and semantic taggers (and, to a lesser extent, also natural language parsers) have become critical resources for the computer applications that process natural language. Hence, any computer application that has to analyse a text automatically and ‘intelligently’ will include at least a module for POS tagging. The more an application needs to ‘understand’ the meaning of the text it processes, the more linguistic tools and/or modules it will incorporate and integrate.
However, linguistic annotation tools have still some limitations, which can be summarised as follows:
1. Normally, they perform annotations only at a certain linguistic level (that is, Morphology, Syntax, Semantics, etc.).
2. They usually introduce a certain rate of errors and ambiguities when tagging. This error rate ranges from 10 percent up to 50 percent of the units annotated for unrestricted, general texts.
3. Their annotations are most frequently formulated in terms of an annotation schema designed and implemented ad hoc.
A priori, it seems that the interoperation and the integration of several linguistic tools into an appropriate software architecture could most likely solve the limitations stated in (1). Besides, integrating several linguistic annotation tools and making them interoperate could also minimise the limitation stated in (2). Nevertheless, in the latter case, all these tools should produce annotations for a common level, which would have to be combined in order to correct their corresponding errors and inaccuracies. Yet, the limitation stated in (3) prevents both types of integration and interoperation from being easily achieved.
In addition, most high-level annotation tools rely on other lower-level annotation tools and their outputs to generate their own ones. For example, sense-tagging tools (operating at the semantic level) often use POS taggers (operating at a lower level, i.e., the morphosyntactic) to identify the grammatical category of the word or lexical unit they are annotating. Accordingly, if a faulty or inaccurate low-level annotation tool is to be used by other higher-level one in its process, the errors and inaccuracies of the former should be minimised in advance. Otherwise, these errors and inaccuracies would be transferred to (and even magnified in) the annotations of the high-level annotation tool.
Therefore, it would be quite useful to find a way to
(i) correct or, at least, reduce the errors and the inaccuracies of lower-level linguistic tools;
(ii) unify the annotation schemas of different linguistic annotation tools or, more generally speaking, make these tools (as well as their annotations) interoperate.
Clearly, solving (i) and (ii) should ease the automatic annotation of web pages by means of linguistic tools, and their transformation into Semantic Web pages (Berners-Lee, Hendler and Lassila, 2001). Yet, as stated above, (ii) is a type of interoperability problem. There again, ontologies (Gruber, 1993; Borst, 1997) have been successfully applied thus far to solve several interoperability problems. Hence, ontologies should help solve also the problems and limitations of linguistic annotation tools aforementioned.
Thus, to summarise, the main aim of the present work was to combine somehow these separated approaches, mechanisms and tools for annotation from Linguistics and Ontological Engineering (and the Semantic Web) in a sort of hybrid (linguistic and ontological) annotation model, suitable for both areas. This hybrid (semantic) annotation model should (a) benefit from the advances, models, techniques, mechanisms and tools of these two areas; (b) minimise (and even solve, when possible) some of the problems found in each of them; and (c) be suitable for the Semantic Web. The concrete goals that helped attain this aim are presented in the following section.
2. GOALS OF THE PRESENT WORK
As mentioned above, the main goal of this work was to specify a hybrid (that is, linguistically-motivated and ontology-based) model of annotation suitable for the Semantic Web (i.e. it had to produce a semantic annotation of web page contents). This entailed that the tags included in the annotations of the model had to (1) represent linguistic concepts (or linguistic categories, as they are termed in ISO/DCR (2008)), in order for this model to be linguistically-motivated; (2) be ontological terms (i.e., use an ontological vocabulary), in order for the model to be ontology-based; and (3) be structured (linked) as a collection of ontology-based
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No presente trabalho foi investigada a transesterificação de blendas dos óleos de soja e de tungue com metanol ou etanol empregando catalisador alcalino (NaOH ou KOH). Foi investigado o tempo reacional, a proporção da blenda, a concentração e o tipo de catalisador, tipo de álcool e razão molar, temperatura e metodologia empregada no tratamento da reação. Nas reações com metanol obtiveram-se melhores conversões com tempo reacional de 1,5h; temperatura de 60°C; proporção blenda dos óleos de soja e de tungue de 90:10 (m/m); concentração de NaOH de 0,5% em relação a massa da blenda e razão molar metanol:blenda de 6:1. O tratamento dos ésteres metílicos produzidos na reação foi realizado por lavagem com água a 60°C após o processo de decantação das fases, metodologia C. O rendimento de ésteres metílicos foi superior a 96% e, o teor de mono-, di- e triacilglicerídeos, glicerol livre e total ficou abaixo dos limites estabelecidos pela ANP, indicando boa conversão (> 96,5%). Nas reações com etanol verificou-se que as melhores condições reacionais foram com uma concentração de catalisador de 0,8% de NaOH em relação a massa da blenda, razão molar etanol:blenda de 9:1, tempo de 1,5h e temperatura de 60°C. O tratamento dos produtos da reação foi realizado por lavagem com água a 60°C após o processo de remoção do etanol e decantação das fases, metodologia D. A concentração do catalisador foi um fator determinante na separação das fases. Uma maior concentração de catalisador favorece a saponificação, dificultando a separação das fases e afetando o rendimento do biodiesel sintetizado, tanto para o metílico quanto o etílico. O índice de acidez, tanto para o biodiesel metílico como o etílico, para qualquer proporção da blenda dos óleos de soja e tungue, ficaram dentro das normas da ANP, com valores abaixo de 0,5 mg.g-1 de KOH.