996 resultados para air injection


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Ethylene gas is burnt and the carbon soot particles are thermophoretically collected using a home-built equipment where the fuel air injection and intervention into the 7.5-cm long flame are controlled using three small pneumatic cylinders and computer-driven controllers. The physical and mechanical properties and tribological performance of the collected soot are compared with those of carbon black and diesel soot. The crystalline structures of the nanometric particles generated in the flame, as revealed by high-resolution transmission electron studies, are shown to vary from the flame root to the exhaust. As the particle journeys upwards the flame, through a purely amorphous coagulated phase at the burner nozzle, it leads to a well-defined crystalline phase shell in the mid-flame zone and to a disordered phase consisting of randomly distributed short-range crystalline order at the exhaust. In the mid-flame region, a large shell of radial-columnar order surrounds a dense amorphous core. The hardness and wear resistance as well as friction coefficient of the soot extracted from this zone are low. The mechanical properties characteristics of this zone may be attributed to microcrystalline slip. Moving towards the exhaust, the slip is inhibited and there is an increase in hardness and friction compared to those in the mid-flame zone. This study of the comparison of flame soot to carbon black and diesel soot is further extended to suggest a rationale based on additional physico-chemical study using micro-Raman spectroscopy.

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A Echinodorus macrophyllus (Alismataceae), conhecida como chapéu de couro no Brasil, é usada popularmente para tratar doenças reumáticas e inflamatórias. Neste trabalho, foram avaliados os efeitos antiinflamatórios do extrato aquoso de E. macrophyllus (EAEm) e suas frações etanólicas no modelo murino de air pouch. Para a obtenção das frações, 7 g do EAEm foram aplicadas em uma coluna cromatográfica aberta de sílica gel eluída com diferentes concentrações de etanol. Os cromatogramas do EAEm/frações foram obtidos usando um sistema de HPLC. Foram obtidas quatro frações, duas delas com maior rendimento. Resumidamente, a bolha de ar foi induzida pela injeção de 5 mL de ar estéril (s.c) no dorso de camundongos SW machos (25-35 g). Após 3 dias, mas 3 mL de ar estéril foram injetados para manter a bolha. No sexto dia, cada grupo (n = 4) foi tratado intraperitoneal (ip) ou oralmente (v.o) com EAEm (25 ou 250 mg/kg), Fr20 ou Fr40 (2,5, 25, 50 ou 100 mg/kg) e os controles com indometacina (10 mg/kg, v.o.) ou veículo (salina). Uma hora depois, 1 mL de salina ou de carragenina 1% estéril foi injetada dentro da bolha. Após 4 h, a cavidade foi lavada com NaCl 0,9%, EDTA 2 mM (1 mL), para a determinação do número de leucócitos, volume do exsudato e concentração de proteínas. Células do exsudato foram preparadas em citocentrífuga e coradas pelo método do Panótico para a contagem diferencial dos leucócitos. Cortes histológicos coletados dos diferentes grupos foram fixados com formol tamponado 10% (pH 7,4) por 7 dias, corados com HE e analisados em MO. A análise da expressão da iNOS e da COX-2 foi realizada em células do exsudato por RT-PCR. O acúmulo de nitrito (NO2−) no sobrenadante do cultivo de células RAW 264.7 foi determinado usando um ensaio colorimétrico baseado na reação de Griess. Os resultados foram expressos como média EP e comparados usando ANOVA seguido de teste de Dunnet. Os experimentos foram realizados em triplicata. No modelo air pouch, a injeção de carragenina 1% aumentou tanto a migração celular quanto a concentração de proteína no exsudato. Contudo, enquanto o pré-tratamento com a Fr40 aumentou a resposta inflamatória, o pré-tratamento com o EAEm e a Fr20, sobretudo por via i.p., inibiu esta resposta quando comparado ao grupo controle tratado apenas com o veículo. Assim, foram observadas as seguintes razões de inibição da migração de células: EAEm, i.p. a 25 mg/kg (66,44%) e a 250 mg/kg (87,27%) e Fr20 a 2,5 mg/kg (26,89%), 25 mg/kg (60,06%), 50 mg/kg (63,13%) e a 100 mg/kg (77,47%). Em relação à contagem diferencial, o EAEm e a Fr20 afetaram principalmente o número de neutrófilos, inibindo sua migração no exsudato. O EAEm e a Fr20 também reduziram a concentração total de proteínas no exsudato principalmente no tratamento i.p.; EAEm a 25 e 250 mg/kg mostrou 3,33 0,55 e 2,05 0,51 mg/mL, respectivamente, quando comparado aos grupos controles (Indometacina 2.88 0.64 mg/mL; Veículo 5.48 0.88 mg/mL). A Fr20 a 2,5, 25, 50 e 100 mg/kg mostrou 4,788 0,444, 1,417 0,519, 2,474 0,529 e 2,215 0, 361 mg/mL. A análise histológica mostrou infiltrado celular, principalmente composto de leucócitos polimorfonucleares ao longo da derme inflamada de animais tratados com veículo. O tratamento com o EAEm ou Fr20 reduziu a infiltração de leucócitos no tecido inflamado. Além disso, o tratamento com o EAEm e a Fr20 mostrou atividade supressora sobre a expressão de iNOS e COX-2, e mostrou efeitos inibitórios na produção de NO induzida por LPS. Concluindo, todos estes resultados confirmam o potencial antiinflamatório sugerido para esta planta e fornecem uma base para a compreensão de seus mecanismos moleculares de ação. Contudo, outros estudos devem ser realizados para melhor elucidar as vias pelas quais o EAEm e a Fr20 exercem seus efeitos antiinflamatórios. Além disso, estudos fitoquímicos devem ser realizados para identificar os compostos ativos no EAEm e na Fr20.

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The three Biesbosch Reservoirs are pumped storage reservoirs, fed with rather polluted and highly eutrophic water from the River Meuse. Air injection at the bottom of the reservoirs prevents thermal stratification, which would otherwise result in serious water quality deterioration. Reservoir mixing also serves as an economic algal control measure; mixing over sufficient depth causes light to play the role of limiting factor and this, combined with zooplankton grazing, keeps the biomass of phytoplankton at acceptable levels. Special problems are caused by benthic, geosmin-producing Oscillatoria species growing on the inner embankment. Rooting up the bottom with a harrow is used as the method of control, based on underwater observations by biological staff trained as SCUBA-divers. With regard to pollutant behaviour the three reservoirs act as a series of fully mixed reactors. This enables the application of kinetic models to describe their behaviour and allows the use of a selective intake policy, e.g. for suspended solids with associated contaminants, ammonia and polynuclear aromatic hydrocarbons. A combination of selective intake and self- purification processes - enhanced by the compartmentalisation of the storage volume in three reservoirs - leads to a striking improvement for many water-quality parameters.

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A descarga desenfreada de águas residuais no meio ambiente, ao longo dos últimos anos, vem acelerando o processo de contaminação e degradação dos corpos hídricos no mundo. Tais rejeitos apresentam elevada carga de contaminantes e de concentração de matéria orgânica o que leva a mortandade das espécies pela concorrência ao oxigênio e, em casos extremos, a aceleração dos processos de eutrofização. Pensando nisso, o presente trabalho estudou um sistema híbrido, em batelada, de tratamento de águas oleosas simuladas em laboratório pela adição de um determinado óleo lubrificante em uma solução aquosa de agentes emulsificantes e eletrólito suporte. O sistema de tratamento foi composto de duas etapas, onde na primeira avaliou-se o uso da técnica da eletrofloculação, responsável por quebrar a estabilidade das emulsões óleo/água e de uma segunda que avaliou o uso de processos de separação com membranas visando à remoção do metal adicionado ao efluente na etapa anterior. O sistema de eletrofloculação foi avaliado em relação ao uso de eletrodos de alumínio e ferro com correntes elétricas de 1A, 2A e 3A, nos modos contínuo e alternado. Os resultados apontaram um maior consumo evidente de massa de eletrodos quando do uso da corrente contínua, 4,0337g 0,0132 para o alumínio e 3,8260g 0,0181 para o ferro ao passo que o consumo foi de 2,1400g 0,0099 para o alumínio e 2,4121g 0,0127 para o ferro quando do o uso da corrente alternada. Foram alcançadas remoções máximas de 98 % 0 da DQO, 99,77 % 0,27 de remoção da cor e 100 % 0 de remoção da turbidez para o uso de corrente alternada e eletrodos de alumínio enquanto se alcançaram remoções máximas 96 % 1 da DQO, 99,46 % 0,82 de remoção da cor e também 100 % 0 de remoção da turbidez no uso de eletrodos de ferro. Na segunda etapa do estudo, a osmose inversa, o sistema utilizado atingiu rejeições de 99,53 % 0,12; 99,56 % 0,13 e de 98,87 % 0,36, para pressões respectivas de 10, 20 e 30 bar. Além disso, foram obtidos fluxos crescentes de permeado 10,87 L/h.m2 0,25; 15,67 L/h.m2 0,53; 18,49 L/h.m2 0,74 com o também aumento da pressão. Ao final do estudo alcançou-se um efluente final com baixa carga orgânica e de metais, estando o mesmo apto ao lançamento nos corpos receptores. Entretanto, mecanismos de controle, sobretudo de pH devem ser incluídos no projeto desses sistemas uma vez que esse parâmetro sofre alterações ao longo do processo

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O gênero Pterodon compreende algumas espécies largamente distribuídas sobre a região central do Brasil. Seus frutos são comercialmente disponíveis no mercado da flora medicinal sendo amplamente utilizados pelas suas propriedades farmacológicas como antirreumático, anti-inflamatório e analgésicas. O objetivo deste trabalho foi biomonitorar o fracionamento do extrato hexânico de Pterodon polygalaeflorus Benth. (ExPpg), utilizando modelos de inflamação aguda (edema de pata e bolha de ar). O fracionamento/sub-fracionamento foi realizado por cromatografia em coluna de sílica e as amostras analisadas por cromatografia em camada fina e cromatografia gasosa acoplada a espectrômetro de massas. O edema de pata foi induzido em camundongos SW por injeção (s.c.) de carragenina. Uma hora antes da inoculação de carragenina os animais foram tratados v.o. com veículo (EtOH 15%, 1,25% Tween-20), indometacina (10 mg/kg p.c.) ou ExHPpg/frações/sub-frações de Ppg. No modelo bolha de ar, a cavidade foi desenvolvida em camundongos SW através da injeção de ar estéril (s.c.) no dorso e a inflamação induzida por carragenina. Uma hora antes de inocular a carragenina os animais foram tratados (v.o) com o veículo, indometacina (10 mg/kg) ou ExHPpg/Fr2Ppg/sub-frações. Após 4 h o exsudato da bolha foi coletado para contagem total e diferencial de leucócitos (Panótico rápido) e dosagem de proteínas (biureto), e a pele referente à bolha foi removida para análises macroscópica e histológica (HE). Também foi realizado estudo de migração de neutrófilos pelo ensaio do transwell. Após demonstração do efeito antiedematogênico do ExHPpg, este foi fracionado em quatro frações. A fração Fr2Ppg, mais ativa no modelo de edema de pata, também inibiu os diferentes parâmetros inflamatórios avaliados no modelo de bolha de ar, com a menor dose testada, e foi sub-fracionada em cinco sub-frações. Destas, as SF2.1 e SF2.2 foram as que mostraram melhor efeito anti-inflamatório pelo modelo da bolha de ar. Em relação ao grupo controle com carragenina, o ExHppg, Fr2Ppg, SF 2.1 e SF 2.2, na dose 0,02 mg/kg, exerceram inibições de 70,6%, 62,8%, 54,7% e 79% no número total de células no exsudato, reduções de 76,8%, 76,9%, 71,1% e 73,3% na concentração de proteína, respectivamente. Com a dose de 0,2 mg/kg, foram observadas inibições apenas para ExHPpg e SF 2.1, com intensidades menores, na leucometria total (62,9% e 48,62%, respectivamente), e na concentração de proteína para SF 2.1 e SF 2.2 (reduções de 68,2% e 30,4%, respectivamente). As análises macroscópica e histológica mostraram redução importante da vasodilatação e do infiltrado inflamatório pelo tratamento com o ExHppg, Fr2Ppg, SF 2.1 e SF 2.2. No ensaio de transwell a Fr2Ppg exibiu 31,4% de inibição na migração de neutrófilos. As sub-frações SF2.1 e SF2.2 foram avaliadas por GC-MS, identificando-se de diversos compostos majoritários. Em resumo, este trabalho confirma o potencial anti-inflamatório da espécie Pterodon polygalaeflorus e mostra um fracionamento efetivo do ExHPpg quanto à composição e ação anti-inflamatória.

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Half of the world’s urban population will live in informal settlements or “slums” by 2030. Affordable urban sanitation presents a unique set of challenges as the lack of space and resources to construct new latrines makes the de-sludging of existing pits necessary and is something that is currently done manually with significant associated health risks. Therefore various mechanised technologies have been developed to facilitate pit emptying, with the majority using a vacuum system to remove material from the top of the pit. However, this results in the gradual accumulation of unpumpable sludge in the pit, which eventually fills the latrine and forces it to be abandoned. This study has developed a method for fluidising unpumpable pit latrine sludge, based on laboratory experiments using a harmless synthetic sludge. Such a sludge consisting of clay and compost was developed to replicate the physical characteristics of pit latrine sludges characterised in Botswana during the 1980s. Undrained shear strength and density are identified as the critical parameters in controlling pumpability and a method of sludge characterisation based on these parameters is reported. In a series of fluidisation tests using a one fifth scale pit emptying device the reduction in sludge shear strength was found to be caused by i) dilution, which increases water content, and ii) remoulding, which involves mechanical agitation to break down the structure of the material. The tests demonstrated that even the strongest of sludges could be rendered “pumpable” by sufficient dilution. Additionally, air injection alone produced a three-fold decrease in strength of consolidated samples as a result of remoulding at constant water content. The implications for sludge treatment and disposal are discussed, and the classification of sludges according to the equipment required to remove them from the latrine is proposed. Possible field tests to estimate sludge density and shear strength are suggested. The feasibility of using low cost vacuum cleaners to replace expensive vane pumps is demonstrated. This offers great potential for the development of affordable pit emptying technologies that can remove significantly stronger sludges than current devices through fluidising the wastes at the bottom of the pit before emptying

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Droplet size and dynamics of blended palm oil-based fatty acid methyl ester (FAME) and diesel oil spray were mechanistically investigated using a phase Doppler anemometry. A two-fluid atomizer was applied for dispersing viscous blends of blended biodiesel oil with designated flow rates. It was experimentally found that the atomizer could generate a spray with large droplets with Sauter mean diameters of ca. 30 mm at low air injection pressure. Such large droplets traveled with a low velocity along their trajectory after emerging from the nozzle tip. The viscosity of blended biodiesel could significantly affect the atomizing process, resulting in the controlled droplet size distribution. Blended biodiesel with a certain fraction of palm oil-based FAME would be consistently atomized owing to its low viscosity. However, the viscosity could exert only a small effect on the droplet velocity profile with the air injection pressure higher than 0.2 MPa.

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Droplet size distribution of biodiesel oil with various compositions was investigated in this work. The droplets generated by a two-fluid atomizer were measured by a commercial PDA. It was found that viscosity of the fuel has a strong effect on the drop size distribution. Additionally, effect of air injection pressures applied to atomize the spray was taken into account. Shear force induced by flow field exerts an effect on distribution of biodiesel droplets in atomized spray.

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Small off-road engines (SORE) have been recognised as a major source of air pollution. It is estimated that non handheld SORE annually produce over 1 million tonnes of HC+NOx and over 50 million tonnes of CO2. The fuel system design and its operating AFR are of key importance with regard to engine operation and engine out emissions. The conventional low-cost float carburettors used in these engines are relatively ineffective at atomising and preparing the fuel for combustion requiring a rich setting for acceptable functional performance. EPA and CARB have confirmed that Phase 3 limits are achievable for a “durable” engine fitted with a conventional well calibrated and manufactured “stock rich setting” float carburettor together with catalytic oxidation after-treatment and passive secondary air injection. The EPA and CARB strategy for meeting Phase 3 only considers the use of conventional float carburettors that operate at rich AFR’s over their entire engine operating range as no other cost effective alternative fuel system is yet available on the market. A cost effective alternative to the conventional carburettor that enabled leaner or optimised AFR operation with load and improved combustion performance would open the door to alternative strategies to meeting the phase 3 limits. This paper presents a completely new form of mechanical carburettor that gives AFR control with load, improved mixture preparation for improved combustion performance and has a lower production cost than conventional carburettors. The conventional and new fuel system designs and operation are discussed in detail and their technical merits demonstrated in the form of engine test data. The performance of different after-treatment systems is also simulated for different AFR profiles with load for a conventional or unmodified SORE engine. With optimised leaner operation and improved combustion characteristics, this new carburettor technology can provide significant engine out CO and HC+NOx reductions on the J1088 test cycle without loss of functional performance. Depending on the chosen emissions control strategy, minimum engine out emissions or optimum engine AFR for oxidation or three-way after-treatment or another, this new carburettor technology can be easily calibrated to provide the desired engine operating AFR profile on the J1088 cycle.

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The study aims to the hydrodynamic characteristics of swirling fluidized bed, using large particles (Geldart D-type) selected from locally available agricultural produce (coffee beans and black pepper). The important variables considered in the present study include percentage area of opening, angle of air injection and the percentage useful area of the distributor. A total of seven distributors have been designed and fabricated for a bed column of 300 mm, namely single row vane type distributors (15˚ and 20˚ vane angle), inclined hole type distributors (15˚ and 20˚ vane angle) and perforated plate distributors. The useful area of distributor of single row vane type, three now vane-type and inclined hole-type distributors are respectively 64%,91% and 94%. The hydrodynamic parameters considered in the present study include distributor pressure drop, air velocity, minimum fluidizing velocity, bed pressure drop, bed height and the bed behaviour. It has been observed that, in general, the distributor pressure drop decreases with an increase in the percentage area of opening, Further, and increase in the area of opening above 17% will not considerably reduce the distributor pressure drop. In the present study, for the distributor with an area of opening 17%, and corresponding to the maximum measured superficial velocity of 4.33 m/s, the distributor pressure drop obtained was 55.25mm of water. The study on the bed behavior revealed that, in a swirling fluidized bed, once swirl motion starts, the bed pressure drop increases with superficial velocity in the outer region and it decreases in the inner region. This means that, with higher superficial velocity, the air might get by-passed through the inner boundary of the bed (around the cone). So, depending on the process for which the bed is used, the maximum superficial velocity is to be limited to have an optimum bed performance.

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The occurrence of heavy oil reservoirs have increased substantially and, due to the high viscosity characteristic of this type of oil, conventional recovery methods can not be applied. Thermal methods have been studied for the recovery of this type of oil, with a main objective to reduce its viscosity, by increasing the reservoir temperature, favoring the mobility of the oil and allowing an increasing in the productivity rate of the fields. In situ combustion (ISC) is a thermal recovery method in which heat is produced inside the reservoir by the combustion of part of the oil with injected oxygen, contrasting with the injection of fluid that is heated in the surface for subsequent injection, which leads to loss heat during the trajectory to the reservoir. The ISC is a favorable method for recovery of heavy oil, but it is still difficult to be field implemented. This work had as an objective the parametric analysis of ISC process applied to a semi-synthetic reservoir with characteristics of the Brazilian Northeast reservoirs using vertical production and vertical injection wells, as the air flow injection and the wells completions. For the analysis, was used a commercial program for simulation of oil reservoirs using thermal processes, called Steam, Thermal and Advanced Processes Reservoir Simulator (STARS) from Computer Modelling Group (CMG). From the results it was possible to analyze the efficiency of the ISC process in heavy oil reservoirs by increasing the reservoir temperature, providing a large decrease in oil viscosity, increasing its mobility inside the reservoir, as well as the improvement in the quality of this oil and therefore increasing significantly its recovered fraction. Among the analyzed parameters, the flow rate of air injection was the one which had greater influence in ISC, obtaining higher recovery factor the higher is the flow rate of injection, due to the greater amount of oxygen while ensuring the maintenance of the combustion front

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Aerobic internal-loop reactors use active biomass attached in a supporting media (biofilm) with the advantage of retaining a big biomass concentration in a small physical space, removing carbonaceous matter and nitrogen in only one reactor. Liquid circulation occurs due to hydrostatic pressure difference produced by air injection in the riser. In biphasic conditions liquid circulation velocities, gas holdup and oxygen transfer coefficient in four different reactor configurations were studied. For the three-phase conditions, the same parameters in just one of those configurations were evaluated. Also, there were three granular supporting media characterized. On the other hand, the relationship between internal and external tube areas and supporting media concentrations influence the liquid velocity, gas holdup and oxygen mass transfer values and some important supporting media characteristics were observed and compared.

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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

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Pós-graduação em Engenharia e Ciência de Alimentos - IBILCE