Alterações urinárias assintomáticas em portadores do anticorpo para virus da hepatite C

Vários estudos associam a infecção crônica pelo vírus da hepatite C a manifestação extra-hepáticas incluindo glomerulonefrite membranoproliferativa. A prevalência de anormalidades urinárias associadas a esta infecção ainda é controversa. Este trabalho tem por objetivo investigar a prevalência de alterações urinárias assintomáticas em doadores de sangue com anti VHC positivo. No período de Julho de 1997 a Março de 1998 foram avaliados 58 doadores de sangue anti VHC + (41 homens e 17 mulheres; com idade média de 34 anos) e 128 doadores VHC -, considerado grupo controle (93 homens e 35 mulheres; com idade média de 31 anos). Todos foram questionados quanto à história prévia de doenças sistêmicas, do trato urinário, uso de drogas (incluindo AINE e uso de analgésico ), transfusão de sangue, fumo e uso de álcool. O anti VHC foi medido pela técnica de enzima imunoensaio, de segunda geração (Abbot Laboratories). As amostras de urina foram inicialmente rastreadas utilizando-se fitas Combur 10 (Boehringer). A microalbuminuria foi medida pela imunoturbidimetria (Bayer, kit 6813) e a NAG foi medida pela técnica de espectrofotometria ( SIGMA N 9376 ). Hematúria assintomática foi definida como > 5 hemácias no sedimento urinário, proteinúria com o aparecimento de 1+ na fita reagente; cilindrúria quando foi visualizado qualquer tipo de cilindro; microalbuminúria alterada quando foi >16 mg/l; relação microalbuminúria/creatininúria elevada quando >15mg/g e a NAG urinária elevada, quando os valores estavam > 5,6U/g de creatinina na urina. Na análise estatística utilizou-se um nível de significância de 95% (p=0,05). Verificou-se que a cor branca e o sexo masculino predominaram nos dois grupos, o grupo VHC + apresentou uma freqüência significativamente aumentada em relação ao uso de AINE (p= 0,003), álcool p< 0,001), transfusão (p= 0,006) e drogas (p< 0,001) quando comparado ao grupo VHC -. No grupo VHC + as enzimas hepáticas estavam significativamente mais elevadas (AST p=0,004, ALT p< 0,001), assim como as médias de GGT (p= 0,004). Concluímos que o grupo anti VHC + em estudo não apresenta anormalidades urinárias significativas comparativamente com o grupo controle. A prevalência de hematúria e proteinúria nos grupos VHC + e VHC – foi respectivamente 12,0% x 9,4% e 5,4% x 5,5%, sem diferença estatística entre os dois grupos. As médias da microalbuminúria nos dois grupos foram respectivamente (10,5 + 22,5 ; 8,7 +12,2 , p= 0,560) e a da NAG (3,2 + 1,8 ; 4,2 + 3,3 , p= 0,232). Constatamos uma associação estatisticamente significativa entre a presença de hematúria e proteinúria (p= 0,011), proteinúria e cilindrúria ( p< 0,001), proteinúria e índice de elevado de microalbuminúria ( p<0,001), NAG e índice de microalbuminúria elevado (p= 0,02); hematúria e sexo feminino (p<0,001), níveis de GT elevados nos indivíduos com proteinúria (p=0,038) e uma associação entre NAG e tabagismo ( p=0,004).

Desenvolvimento da técnica LTM-BSizer para a caracterização de bolhas e a avaliação de parâmetro no processo de flotação

Este trabalho teve como objetivo o desenvolvimento de uma nova técnica para determinação do tamanho médio e da distribuição de tamanho de bolhas de ar em meio aquoso. A nova técnica, denominada de LTM-BSizer, uma vez otimizada, foi aplicada na caracterização das bolhas geradas por diversos métodos utilizados tanto na flotação para tratamento de efluentes líquidos quanto na flotação de partículas minerais e, principalmente, na investigação de parâmetros operacionais e do efeito do tamanho de bolhas na flotação de partículas minerais (quartzo como modelo) finas (40-10 µm) e ultrafinas (<10 µm). A técnica LTM-BSizer é baseada no conceito da captura, ou seja, ao contrário das técnicas fotográficas até agora propostas, onde as imagens (fotos ou vídeos) das bolhas em movimento foram obtidas com visores verticais, este método obteve as imagens das bolhas estabilizadas em um visor disposto na horizontal. Entre as vantagens em relação aos métodos fotográficos existentes destacam-se a melhor qualidade das imagens e a capacidade de medir distribuições de tamanho de bolha com grande amplitude, desde microbolhas (<100 µm) até bolhas maiores (~ 1 a 3 mm). Os métodos de geração de bolhas pesquisados foram: microbolhas geradas por despressurização de água saturada com ar em um vaso saturador (processo de flotação por ar dissolvido-FAD) ou por uma bomba centrífuga multifase (novo equipamento para geração de microbolhas), injeção de mistura ar-líquido através de um constritor tipo venturi (destaque na flotação não convencional), injeção de ar em cilindro inox poroso (comumente aplicado para dispersão de gás) e bolhas geradas em uma célula de flotação por ar induzido (FAI), convencional de bancada Para todos os métodos citados, exceto o último, a distribuição de tamanho de bolha foi avaliada numa coluna em acrílico com 200 cm de altura e 72 mm de diâmetro, onde através de um ponto de amostragem parte do fluxo foi conduzida até o visor. Os resultados obtidos com esta técnica foram, para os diâmetros médios de bolha: 30 a 70 µm para FAD, 65 a 130 µm para bomba multifase, 200 a 1400 µm para venturi, 500 a 1300 µm para FAI e 500 a 1000 µm para o cilindro poroso. A influência de alguns parâmetros operacionais na formação das bolhas foi estudada em detalhe e os resultados obtidos mostraram uma boa correspondência com os valores encontrados na literatura e em outros casos, elucidaram efeitos considerados contraditórios na literatura técnica. Este trabalho demonstrou que, o tamanho médio e a distribuição de tamanho das microbolhas, não são influenciados pela pressão de saturação no intervalo de 294 a 588 kPa, mas sim pela quantidade de bolhas e pelo tempo de retenção Também foi constatado que a diminuição da tensão superficial da água (adição de 30 mg/L de oleato de sódio) aumenta consideravelmente (3 a 8 vezes) o número de microbolhas na FAD a baixas pressões de saturação (196 e 294 kPa). O tamanho e a distribuição de tamanho de bolhas geradas em constrições de fluxo tipo venturi variam em função dos parâmetros concentração de tensoativo, velocidade superficial de líquido (UL) e razão gás/líquido (Qr). Uma pequena diminuição da tensão superficial, de 73 para 68 mN/m, provocada pela adição de 20 mg/L do tensoativo DF 250, foi suficiente para diminuir consideravelmente o tamanho das bolhas geradas, permanecendo constante para concentrações maiores, sugerindo que esta seja a concentração crítica de coalescência (CCC) para este sistema. Um aumento de UL (mantendo Qr constante) e diminuição de Qr (com UL constante) levaram a distribuições com menor amplitude e diâmetro médio. No caso das microbolhas geradas através da bomba multifase, o tamanho de bolhas diminuiu com a pressão até atingir o limite de solubilidade teórico ar/líquido. O tamanho das bolhas gerados através de placa porosa e FAI apresentaram boa correspondência com os reportados na literatura e em ambas as técnicas foi, de novo, encontrada, para DF 250, a mesma CCC igual a 20 mg/L. O sistema de flotação de partículas finas e ultrafinas, foi estudado via recuperação de finos de quartzo (50% < 10µm) em coluna de laboratório. As variáveis estudadas foram; a distribuição de tamanho de bolhas e a concentração de coletor (amina). Os resultados obtidos mostraram que a recuperação das frações mais finas aumenta com a diminuição do tamanho de bolhas de acordo com os modelos existentes de flotação. Entretanto, foi encontrado, na captura de partículas ultrafinas pelas bolhas, um valor ótimo de tamanho de partícula. Assim, a captura diminui com o tamanho de partícula até 5-7 µm e aumenta, de novo, nas frações menores. Esses resultados são discutidos em termos de um mecanismo de difusão como fenômeno predominante nos mecanismos de adesão bolha-partícula.

Thiamethoxam on the histological characteristics of sugarcane young roots

Thiamethoxam is a systemic insecticide from the neonicotinoid group, nitroguanidin family which affects the nicotinic receptor acetyl choline in the insect membrane, wounding the nervous system and causing the death of the insect. It was used with success in the control of initial pests of several crops. It was considered that thiamethoxam has a bioactivator effect, because in the absence of insects promoted increase in vigor, development and productivity of crops. This work was carried out to verify if thiamethoxam causes histological changes in sugarcane roots. In this work, it was used optical microscopy, images arrest, tissue biometrics and statistical analysis, in young roots of sugarcane RB 83 5486 after the treatments with different thiamethoxam concentrations. It was determined changes in histological structure of tissues 7, 14, 21 and 28 days after the treatments, establishing its effects on root plant anatomy. It was verified that thiamethoxam increased root cortex width, increasing the vascular cylinder and the metaxylem vessel elements number in the vascular tissue until 21 days after application.

Influência da área de amostragem na determinação de perdas totais na colheita de soja

A metodologia, atualmente utilizada, para a determinação das perdas na colheita de soja, que consiste na utilização de armações de 2 m², vem fornecendo resultados com alto coeficiente de variação, o que dificulta detectar diferenças significativas entre os tratamentos, mesmo que esta diferença apresente valores numéricos muito altos. em função deste problema, objetivou-se avaliar o efeito das armações sobre a quantificação das perdas totais na colheita da cultura da soja, alterando-se a velocidade de deslocamento da colhedora e a abertura entre o cilindro e o côncavo. O delineamento experimental foi em blocos casualizados, em esquema fatorial 2 x 3 x 2, totalizando 12 tratamentos com quatro repetições. Os resultados evidenciaram que o coeficiente de variação para a armação de 2 m² foi de 88,26%, enquanto que para a armação de 3 m² este valor foi de 32,85%, e que com a armação de 2 m² foram detectadas perdas totais de 45 kg ha-1, enquanto que com a de 3 m² quantificou-se 73 kg ha-1, indicando que a área das armações interfere na quantificação das perdas totais na cultura da soja.

Colheita mecanizada e perdas quantitativas de sementes de crotalária

In mechanized harvesting of seeds can occur losses, which reduce productivity, decrease the profitability and can do serious damage to the producer. The objective of this work was to evaluate the quantitative seed losses of Crotalaria juncea depending on the harvester speed and the rotation of the threshing cylinder. The experiment was conducted in the area of Education, Research and Production Unesp/Jaboticabal, using a entirely casualized design on factorial away 2x3, with two-speed displacement of the machine (1.8 and 3.2 km h(-1)) and three rotations of threshing cylinder (750, 800 and 850 rpm), with 4 repetitions. It was concluded that the measures relating to the development of the plants showed homogeneous behavior, indicating little dispersion of the data. It was observed that the rate of displacement of the harvester and rotation of the drum track not affected the losses in the plataform of cutting. The largest losses of crotalaria seeds occurred on the plataform of cutting the harvester machine, in the form of pods not harvested. It was observed that the total losses in the harvest of crotalaria seed were high, and the losses in pods on the soil, responsible for almost all the losses encountered.

Avaliação do uso do DCP em areias para controle da capacidade de carga em fundações diretas e controle de compactação de aterros

This work presents results of field and laboratory tests using a Dynamic Cone Penetrometer, DCP. The tests were performed in order to evaluate the use of the equipment in sand for the control of bearing capacity of shallow foundations and fill compaction. For shallow foundations, the laboratory tests were conducted on sand placed in a metallic mould by the method of sand pluviation. Although the results show the inability to reproduce field conditions in the laboratory it was possible to verify the ability of the DCP to identify less resistant soil layers. The DCP tests for the analysis of compaction control were performed in a strong box with inside dimensions of 1,40 m x 1,40 m and 0,70 m in height. The soil layers were compacted with different densities though the use of a vibrating plate in order to obtain correlations between penetration index, DPI, and soil relative density. Other tests were also conducted to assess the influence of soil moisture on tests results. Among other findings, the results showed the great potential for the use of DCP to control the compaction of sand fills

Viabilidades térmica, econômica e de materiais de um sistema solar de aquecimento de água a baixo custo para fins residenciais

An solar alternative system for water heating is presented. Is composed for one low cost alternative collector and alternative thermal reservoir for hot water storing. The collector of the system has box confectioned in composite material and use absorption coils formed for PVC tubes. The box of hot water storage was confectioned from a plastic polyethylene drum used for storage of water and garbage, coated for a cylinder confectioned in fiber glass. The principle of functioning of the system is the same of the conventionally. Its regimen of work is the thermosiphon for a volume of 250 liters water. The main characteristic of the system in considered study is its low cost, allowing a bigger socialization of the use of solar energy. It will be demonstrated the viabilities thermal, economic and of materials of the system of considered heating, and its competitiveness in relation to the available collectors commercially. Relative aspects will be boarded also the susceptibility the thermal degradation and for UV for the PVC tubes. It will be shown that such system of alternative heating, that has as main characteristic its low cost, presents viabilities thermal, economic and of materials

Projeto, construção e levantamento de desempenho de um concentrador solar cilíndro parabólico com mecanismo automático de rastreamento solar

An cylinder-parabolic solar concentrator is presented to produce steam for different applications. This prototype was built in glass fiber with dimensions that follow a study of optimization of parameters inherent in the optical reflection of sunlight by the surface of reflection and absorption of the same by tubing that leads the fluid of work. The surface of the concentrator of 2.24 m² has been covered by layers of mirror with 1.0 m of lenght and 2.0 cm wide. The absorb tubing consists of a copper tube diameter equal to 28 mm. The concentrator is moving to follow the apparent motion of the sun. It will be presented the processes of manufacturing and assembly of the concentrator proposed, which has as main characteristics the facilities construction and assembly, in addition to reduced cost. Will be presented data from tests performed to produce steam setting up some parameters that diagnose the efficiency of the concentrator. It will be demonstrated the viabilities thermal, economic and of materials of the proposed system.The maximum temperature achieved in the vacuum tube absorber was 232.1°C and average temperature for 1 hour interval was 171.5°C, obtained in a test with automation. The maximum temperature achieved in the output of water was 197.7°C for a temperature of 200.0°C in the absorber tube. The best average result of the water exit temperature to interval of 1 hour was 170.2°C for a temperature of 171.2°C, in the absorber tube, obtained in test with automation. Water exit mean temperatures were always above of the water steaming temperature. The concentrator present a useful efficiency of 38% and a production cost of approximately R$ 450,00 ( $ 160.34)

Projeto, construção e análise de desempenho de coletores solares alternativos utilizando garrafas pet

A solar alternative system for water heating is presented. It work on a thermosiphon, consisting of one or two alternative collectors and a water storage tank also alternative, whose main purpose is to socialize the use of energy mainly to be used by people of low income. The collectors were built from the use of pets bottles, cans of beer and soft drinks and tubes of PVC, ½ " and the thermal reservoirs from a drum of polyethylene used for storage of water and garbage placed inside cylinder of fiber glass and EPS ground between the two surfaces. Such collectors are formed by three elements: pet bottles, cans and tubes absorbers. The heating units, which form the collector contains inside the cans that can be closed, in original form or in the form of plate. The collectors have an absorber grid formed by eight absorbers PVC tube, connected through connections at T of the same material and diameter. It will be presented data of the thermal parameters which demonstrate the efficiency of the heating system proposed. Relative aspects will be boarded also the susceptibility the thermal degradation and for UV for the PVC tubes. It will be demonstrated that this alternative heating system, which has as its main feature low cost, presents thermal, economic and materials viabilities

Mecanismos de desgaste, história térmica e ciclo de vida de componentes de um motor de combustão interna de aeromodelo

We developed an assay methodology that considered the temperature variation and the scanning electron microscopy as a method to quantify and characterize respectively the consumption evolution in three 46 LA machines, with internal combustion and two-stroke engines, 7.64 cm3 cylinder capacity, 23.0 millimeters diameter and 18.4 millimeters course, RPM service from 2.000 to 16.000 rpm, 1.2 HP power, and 272 grams weight. The investigated engines components were: (1) head of the engine (Al-Si alloy), (2) piston (Al-Si alloy) and (3) piston pin (AISI 52100 steel). The assays were carried out on a desktop; engines 1 and 2 were assayed with no load, whereas in two assays of engine 3 we added a fan with wind speed that varied from 8.10 m/s to 11.92 m/s, in order to identify and compare the engine dynamic behavior as related to the engines assayed with no load. The temperatures of the engine s surface and surroundings were measured by two type K thermopairs connected to the assay device and registered in a microcomputer with data recording and parameters control and monitoring software, throughout the assays. The consumed surface of the components was analyzed by scanning electron microscopy (SEM) and microanalysis-EDS. The study was complemented with shape deformation and mass measurement assays. The temperature variation was associated with the oxides morphology and the consumption mechanisms were discussed based on the relation between the thermal mechanical effects and the responses of the materials characterization

Desenvolvimento de uma desfribadeira para obtenção da fibra da folha do abacaxi

In 1998 the first decorticator was developed in the Textile Engineering Laboratory and patented for the purpose of extracting fibres from pineapple leaves, with the financial help from CNPq and BNB. The objective of the present work was to develop an automatic decorticator different from the first one with a semiautomatic system of decortication with automatic feeding of the leaves and collection of the extracted fibres. The system is started through a command system that passes information to two engines, one for starting the beater cylinder and the other for the feeding of the leaves as well as the extraction of the decorticated fibres automatically. This in turn introduces the leaves between a knife and a beater cylinder with twenty blades (the previous one had only 8 blades). These blades are supported by equidistant flanges with a central transmission axis that would help in increasing the number of beatings of the leaves. In the present system the operator has to place the leaves on the rotating endless feeding belt and collect the extracted leaves that are being carried out through another endless belt. The pulp resulted form the extraction is collected in a tray through a collector. The feeding of the leaves as well as the extraction of the fibres is controlled automatically by varying the velocity of the cylinders. The semi-automatic decorticator basically composed of a chassis made out of iron bars (profile L) with 200cm length, 91 cm of height 68 cm of width. The decorticator weighs around 300Kg. It was observed that the increase in the number of blades from 8 to twenty in the beater cylinder reduced the turbulence inside the decorticator, which helped to improve the removal of the fibres without any problems as well as the quality of the fibres. From the studies carried out, from each leaf 2,8 to 4,5% of fibres can be extracted. This gives around 4 to 5 tons of fibres per hectare, which is more than that of cotton production per hectare. This quantity with no doubt could generate jobs to the people not only on the production of the fibres but also on their application in different areas

Estudo da influência da temperatura na degradação termoquímica da biomassa de avelós

The bio-oil obtained from the pyrolysis of biomass has appeared as inter-esting alternative to replace fossil fuels. The aim of this work is to evaluate the influence of temperature on the yield of products originating from the pyrolysis process of the powder obtained from the dried twigs of avelós (Euphorbia tirucalli), using a rotating cylinder reactor in laboratory scale. The biomass was treated and characterized by: CHNS, moisture, volatiles, fixed carbon and ashes, as well as evaluation of lignin, cellulose and hemicellulose, besides other instrumental techniques such as: FTIR, TG/DTG, DRX, FRX and MEV. The activation energy was evaluated in non-isothemichal mode with heating rates of 5 and 10 oC/min. The obtained results showed biomass as feedstock with potential for biofuel production, because presents a high organic matter content (78,3%) and fixed-carbon (7,11%). The activation energy required for the degradation of biomass ranged between 232,92 392,84 kJ/mol, in the temperature range studied and heating rate of 5 and 10°C/min. In the pyrolysis process, the influence of the reaction temperature was studied (350-520 ° C), keeping constant the other variables, such as, the flow rate of carrier gas, the centrifugal speed for the bio-oil condensationa, the biomass flow and the rotation of the reactor. The maximum yield of bio-oil was obtained in the temperature of 450°C. In this temperature, the results achieved where: content of bio-oil 8,12%; char 32,7%; non-condensed gas 35,4%; losts 23,8%; gross calorific value 3,43MJ/kg; pH 4,93 and viscosity 1,5cP. The chromatographic analysis of the bio-oil produced under these conditions shows mainly the presence of phenol (17,71%), methylciclopentenone (10,56%) and dimethylciclopentenone (7,76%)

Estudo da influência da temperatura na degradação termoquímica da biomassa de avelós (euphorbia tirucalli Linn)

The bio-oil obtained from the pyrolysis of biomass has appeared as inter-esting alternative to replace fossil fuels. The aim of this work is to evaluate the influence of temperature on the yield of products originating from the pyrolysis process of the powder obtained from the dried twigs of avelós (Euphorbia tirucalli), using a rotating cylinder reactor in laboratory scale. The biomass was treated and characterized by: CHNS, moisture, volatiles, fixed carbon and ashes, as well as evaluation of lignin, cellulose and hemicellulose, besides other instrumental techniques such as: FTIR, TG/DTG, DRX, FRX and MEV. The activation energy was evaluated in non-isothemichal mode with heating rates of 5 and 10 oC/min. The obtained results showed biomass as feedstock with potential for biofuel production, because presents a high organic matter content (78,3%) and fixed-carbon (7,11%). The activation energy required for the degradation of biomass ranged between 232,92 392,84 kJ/mol, in the temperature range studied and heating rate of 5 and 10°C/min. In the pyrolysis process, the influence of the reaction temperature was studied (350-520 ° C), keeping constant the other variables, such as, the flow rate of carrier gas, the centrifugal speed for the bio-oil condensationa, the biomass flow and the rotation of the reactor. The maximum yield of bio-oil was obtained in the temperature of 450°C. In this temperature, the results achieved where: content of bio-oil 8,12%; char 32,7%; non-condensed gas 35,4%; losts 23,8%; gross calorific value 3,43MJ/kg; pH 4,93 and viscosity 1,5cP. The chromatographic analysis of the bio-oil produced under these conditions shows mainly the presence of phenol (17,71%), methylciclopentenone (10,56%) and dimethylciclopentenone (7,76%)