Impact of cathode evaporation on a free-burning arc

A free-burning, high-intensity argon arc at atmospheric pressure was modelled during the evaporation of copper from the cathode. The effect of cathode evaporation on the temperature, mass flow, current flow and Cu concentration was studied for the entire plasma region. The copper evaporates from the tip of the cathode with an evaporation rate of 1 mg s-1. The copper vapour in the cathode region has a velocity of 210 m s-1 with a mass concentration of above 90% within 0.5 mm from the arc axis. The vapour passes from the cathode toward the anode with a slight diffusion in the argon plasma. Higher temperatures and current densities were calculated in the core of the arc caused by the cathode evaporation.

Experimental Studies on Model Scramjet in a Mach 6 High Enthalpy Free-Jet Wind Tunnel

A side-wall compression scramjet model with different combustor geometries has been tested in a propulsion tunnel that typically provides the testing flow with Mach number of 5.8, total temperature of 1800K, total pressure of 4.5MPa and mass flow rate of 4kg/s. This kerosene-fueled scramjet model consists of a side-wall compression inlet, a combustor and a thrust nozzle. A strut was used to increase the contraction ratio and to inject fuels, as well as a mixing enhancement device. Several wall cavities were also employed for flame-holding. In order to shorten the ignition delay time of the kerosene fuel, a little amount of hydrogen was used as a pilot flame. The pressure along the combustor has an evident raise after ignition occurred. Consequently thrust was observed during the fuel-on period. However, the thrust was still less than the drag of the scramjet model. For this reason, the drag variation produced by different strut and cavities was tested. Typical results showed that the cavities do not influence the drag so much, but the length of the strut does.

Experimental Studies on Scramjet Tested in a Freejet Facility

Two different type scramjet models with side-wall compression and top-wall compression inlets have been tested in HPTF (Hypersonic Propulsion Test Facility) under the experimental conditions of Mach number 5.8, total temperature 1700K, total pressure 4.5MPa and mass flow rate 3.5kg/s. The liquid kerosene was used as main fuel for the scramjets. In order to get fast ignition in the combustor, a small amount of hydrogen was used as a pilot. A strut with alternative tail was employed for increasing the compression ratio and for mixing enhancement in the side-wall compression case. Recessed cavities were used as a flameholder for combustion stability. The combustion efficiency was estimated by one dimensional theory. The uniformity of the facility nozzle flow was verified by a scanning pitot rake. The experimental results showed that the kerosene fuel was successfully ignited and stable combustion was achieved for both scramjet models. However the thrusts were still less than the model drags due to the low combustion efficiencies.

Performance of a Supersonic Model Combustor using Vaporized Kerosene Injection

Characteristics of supersonic combustion by injecting kerosene vapor into a Mach 2.5 crossflow at various preheat temperatures and pressures were investigated experimentally. A two-stage heating system has been designed and tested, which can prepare heated kerosene of 0.8 kg up to 820 K at pressure of 5.5 Mpa with minimum/negligible fuel coking. In order to simulate the thermophysical properties of kerosene over a wide range of thermodynamic conditions, a three-component surrogate that matches the compound class of the parent fuel was employed. The flow rate of kerosene vapor was calibrated using a sonic nozzle. Computed flow rates using the surrogate fuel are in agreement with the experimental data. Kerosene jets at various preheat temperatures injecting into both quiescent environment and Mach 2.5 crossflow were visualized. It was found that at injection pressure of 4 Mpa and preheat temperature of 550 K the kerosene jet was completely in vapor phase, while keeping almost the same penetration depth as compared to the liquid kerosene injection. Supersonic combustion tests were also carried out to compare the combustor performance for the cases of vaporized kerosene injection, liquid kerosene injection, and effervescent atomization with hydrogen barbotage, under the similar stagnation conditions. Experimental results demonstrated that the use of vaporized kerosene injection leads to better combustor performance. Further parametric study on vaporized kerosene injection in a supersonic model combustor is needed to assess the combustion efficiency as well as to identify the controlling mechanism for the overall combustion enhancement.

Catalytic Cracking and Heat Sink Capacity of Aviation Kerosene Under Supercritical Conditions

Catalytic cracking of China no. 3 aviation kerosene using a zeolite catalyst was investigated under supercritical conditions. A three-stage heating/cracking system was specially designed to be capable of heating 0.8 kg kerosene to a temperature of 1050 K and pressure of 7.0 MPa with maximum mass flow rate of 80 g/s. Sonic nozzles of different diameters were used to calibrate and monitor the mass flow rate of the cracked fuel mixture. With proper experiment arrangements, the mass flow rate per unit throat area of the cracked fuel mixture was found to well correlate with the extent of fuel conversion. The gaseous products obtained from fuel cracking under different conditions were also analyzed using gas chromatography. Composition analysis showed that the average molecular weight of the resulting gaseous products and the fuel mass conversion percentage were a strong function of the fuel temperature and were only slightly affected by the fuel pressure. The fuel conversion was also shown to depend on the fuel residence time in the reactor, as expected. Furthermore, the heat sink levels due to sensible heating and endothermic cracking were determined and compared at varying test conditions. It was found that at a fuel temperature of similar to 1050 K, the total heat sink reached similar to 3.4 MJ/kg, in which chemical heat sink accounted for similar to 1.5 MJ/kg.

Thermal cracking of aviation kerosene for scramjet applications

Thermal cracking of China No.3 aviation kerosene was studied experimentally and analytically under supercritical conditions relevant to regenerative cooling system for Mach-6 scramjet applications. A two-stage heated tube system with cracked products collection/analysis was used and it can achieve a fuel temperature range of 700-1100 K, a pressure range of 3.5-4.5 MPa and a residence time of approximately 0.5-1.3 s. Compositions of the cracked gaseous products and mass flow rate of the kerosene flow at varied temperatures and pressures were obtained experimentally. A one-step lumped model was developed with the cracked mixtures grouped into three categories: unreacted kerosene, gaseous products and residuals including liquid products and carbon deposits. Based on the model, fuel conversion on the mass basis, the reaction rate and the residence time were estimated as functions of temperature. Meanwhile, a sonic nozzle was used for the control of the mass flow rate of the cracked kerosene, and correlation of the mass flow rate gives a good agreement with the measurements.

A Simple Model For Predicting The Void Fraction Of Gas/Non-Newtonian Fluid Intermittent Flows In Upward Inclined Pipes

In this work, a simple correlation, which incorporates the mixture velocity, drift velocity, and the correction factor of Farooqi and Richardson, was proposed to predict the void fraction of gas/non-Newtonian intermittent flow in upward inclined pipes. The correlation was based on 352 data points covering a wide range of flow rates for different CMC solutions at diverse angles. A good agreement was obtained between the predicted and experimental results. These results substantiated the general validity of the model presented for gas/non-Newtonian two-phase intermittent flows.

The Flocculation of E. coli with Polyethyleneimine

A comprehensive study was made of the flocculation of dispersed E. coli bacterial cells by the cationic polymer polyethyleneimine (PEI). The three objectives of this study were to determine the primary mechanism involved in the flocculation of a colloid with an oppositely charged polymer, to determine quantitative correlations between four commonly-used measurements of the extent of flocculation, and to record the effect of varying selected system parameters on the degree of flocculation. The quantitative relationships derived for the four measurements of the extent of flocculation should be of direct assistance to the sanitary engineer in evaluating the effectiveness of specific coagulation processes.

A review of prior statistical mechanical treatments of absorbed polymer configuration revealed that at low degrees of surface site coverage, an oppositely- charged polymer molecule is strongly adsorbed to the colloidal surface, with only short loops or end sequences extending into the solution phase. Even for high molecular weight PEI species, these extensions from the surface are theorized to be less than 50 Å in length. Although the radii of gyration of the five PEI species investigated were found to be large enough to form interparticle bridges, the low surface site coverage at optimum flocculation doses indicates that the predominant mechanism of flocculation is adsorption coagulation.

The effectiveness of the high-molecular weight PEI species 1n producing rapid flocculation at small doses is attributed to the formation of a charge mosaic on the oppositely-charged E. coli surfaces. The large adsorbed PEI molecules not only neutralize the surface charge at the adsorption sites, but also cause charge reversal with excess cationic segments. The alignment of these positive surface patches with negative patches on approaching cells results in strong electrostatic attraction in addition to a reduction of the double-layer interaction energies. The comparative ineffectiveness of low-molecular weight PEI species in producing E. coli flocculation is caused by the size of the individual molecules, which is insufficient to both neutralize and reverse the negative E.coli surface charge. Consequently, coagulation produced by low molecular weight species is attributed solely to the reduction of double-layer interaction energies via adsorption.

Electrophoretic mobility experiments supported the above conclusions, since only the high-molecular weight species were able to reverse the mobility of the E. coli cells. In addition, electron microscope examination of the seam of agglutination between E. coli cells flocculation by PEI revealed tightly- bound cells, with intercellular separation distances of less than 100-200 Å in most instances. This intercellular separation is partially due to cell shrinkage in preparation of the electron micrographs.

The extent of flocculation was measured as a function of PEl molecular weight, PEl dose, and the intensity of reactor chamber mixing. Neither the intensity of mixing, within the common treatment practice limits, nor the time of mixing for up to four hours appeared to play any significant role in either the size or number of E.coli aggregates formed. The extent of flocculation was highly molecular weight dependent: the high-molecular-weight PEl species produce the larger aggregates, the greater turbidity reductions, and the higher filtration flow rates. The PEl dose required for optimum flocculation decreased as the species molecular weight increased. At large doses of high-molecular-weight species, redispersion of the macroflocs occurred, caused by excess adsorption of cationic molecules. The excess adsorption reversed the surface charge on the E.coli cells, as recorded by electrophoretic mobility measurements.

Successful quantitative comparisons were made between changes in suspension turbidity with flocculation and corresponding changes in aggregate size distribution. E. coli aggregates were treated as coalesced spheres, with Mie scattering coefficients determined for spheres in the anomalous diffraction regime. Good quantitative comparisons were also found to exist between the reduction in refiltration time and the reduction of the total colloid surface area caused by flocculation. As with turbidity measurements, a coalesced sphere model was used since the equivalent spherical volume is the only information available from the Coulter particle counter. However, the coalesced sphere model was not applicable to electrophoretic mobility measurements. The aggregates produced at each PEl dose moved at approximately the same vlocity, almost independently of particle size.

PEl was found to be an effective flocculant of E. coli cells at weight ratios of 1 mg PEl: 100 mg E. coli. While PEl itself is toxic to E.coli at these levels, similar cationic polymers could be effectively applied to water and wastewater treatment facilities to enhance sedimentation and filtration characteristics.

Suspension mechanics: I. Inertial and non-Newtonian migration of neutrally buoyant rigid spheres in two-dimensional unidirectional flows; II. The effect of viscoelasticity on the creeping motion of a train of neutrally buoyant Newtonian drops through a circular tube

The lateral migration of neutrally buoyant rigid spheres in two-dimensional unidirectional flows was studied theoretically. The cases of both inertia-induced migration in a Newtonian fluid and normal stress-induced migration in a second-order fluid were considered. Analytical results for the lateral velocities were obtained, and the equilibrium positions and trajectories of the spheres compared favorably with the experimental data available in the literature. The effective viscosity was obtained for a dilute suspension of spheres which were simultaneously undergoing inertia-induced migration and translational Brownian motion in a plane Poiseuille flow. The migration of spheres suspended in a second-order fluid inside a screw extruder was also considered.

The creeping motion of neutrally buoyant concentrically located Newtonian drops through a circular tube was studied experimentally for drops which have an undeformed radius comparable to that of the tube. Both a Newtonian and a viscoelastic suspending fluid were used in order to determine the influence of viscoelasticity. The extra pressure drop due to the presence of the suspended drops, the shape and velocity of the drops, and the streamlines of the flow were obtained for various viscosity ratios, total flow rates, and drop sizes. The results were compared with existing theoretical and experimental data.

Alveolar nitric oxide and its role in pediatric asthma control assessment

Resumen Background: Nitric oxide can be measured at multiple flow rates to determine proximal (maximum airway nitric oxide flux; Jaw(NO)) and distal inflammation (alveolar nitric oxide concentration; CA(NO)). The main aim was to study the association among symptoms, lung function, proximal (maximum airway nitric oxide flux) and distal (alveolar nitric oxide concentration) airway inflammation in asthmatic children treated and not treated with inhaled glucocorticoids. Methods: A cross-sectional study with prospective data collection was carried out in a consecutive sample of girls and boys aged between 6 and 16 years with a medical diagnosis of asthma. Maximum airway nitric oxide flux and alveolar nitric oxide concentration were calculated according to the two-compartment model. In asthmatic patients, the asthma control questionnaire (CAN) was completed and forced spirometry was performed. In controls, differences between the sexes in alveolar nitric oxide concentration and maximum airway nitric oxide flux and their correlation with height were studied. The correlation among the fraction of exhaled NO at 50 ml/s (FENO50), CA(NO), Jaw(NO), forced expiratory volume in 1 second (FEV1) and the CAN questionnaire was measured and the degree of agreement regarding asthma control assessment was studied using Cohen's kappa. Results: We studied 162 children; 49 healthy (group 1), 23 asthmatic participants without treatment (group 2) and 80 asthmatic patients treated with inhaled corticosteroids (group 3). CA(NO) (ppb) was 2.2 (0.1-4.5), 3 (0.2-9.2) and 2.45 (0.1-24), respectively. Jaw(NO) (pl/s) was 516 (98.3-1470), 2356.67 (120-6110) and 1426 (156-11805), respectively. There was a strong association (r = 0.97) between FENO50 and Jaw(NO) and the degree of agreement was very good in group 2 and was good in group 3. There was no agreement or only slight agreement between the measures used to monitor asthma control (FEV1, CAN questionnaire, CA(NO) and Jaw(NO)). Conclusions: The results for CA(NO) and Jaw(NO) in controls were similar to those found in other reports. There was no agreement or only slight agreement among the three measure instruments analyzed to assess asthma control. In our sample, no additional information was provided by CA(NO) and Jaw(NO).

Reservatório de gás não convencional: história de caso na Bacia do Recôncavo - Brasil

O principal objetivo deste trabalho foi à realização de um estudo geológico sobre os folhelhos fraturados da Formação Candeias que ocorrem em diferentes partes da Bacia do Recôncavo, sendo enfatizadas suas principais relações com a acumulação de petróleo. Este trabalho contempla, ainda, uma revisão bibliográfica acerca da evolução da campanha exploratória nesta bacia, desde seus primórdios, na década de trinta, além de uma análise sob as perspectivas na área de exploração e produção. A Bacia do Recôncavo, situada na região Nordeste do Brasil, está inserida numa grande bacia tafrogênica (Rifte abortado Recôncavo-Tucano-Jatobá), originada nos momentos iniciais de ruptura do paleocontinente Gondwana ocidental, no Eocretáceo, sob os campos de tensões que produziram o Oceano Atlântico. Em termos estratigráficos, a bacia guarda um importante registro geológico, compreendido por depósitos continentais (lacustres, fluvio-deltáicos, neríticos, eólicos e leques aluviais), sendo subdividido em seis seqüências sedimentares, referentes aos estágios pré-rifte e rifte. As principais acumulações de petróleo na bacia podem ser agrupadas em três grandes sistemas: pré-rifte, rifte-Candeias e rifte-Ilhas, representando plays exploratórios distintos. As perspectivas futuras para a Bacia do Recôncavo devem considerar a importância da identificação de novos plays exploratórios, através da caracterização de novos intervalos geradores e reservatórios, como é o caso dos folhelhos fraturados e do shale gas. Não menos importante é o desenvolvimento de novas técnicas de produção, aumentando o fator de recuperação de campos produtores.

Witcherwell hatchery husbandry regime

Witcherwell like most new hatcheries has gone through a honeymoon period during which no major fish health problems have occurred. However, in 1994, there was an outbreak of Bacterial Gill Disease which caused high mortalities. This has emphasised the importance of developing and maintaining optimum husbandry practices for Witcherwell. These may also be applicable to other fish culture units in Central Area and the NW. To avoid the reoccurence of bacterial gill disease or other health problems and to ensure that stock of good health and quality are produced good husbandry practices must be followed. This report inculdes information on stock, disinfection, cross-contamination, cleaning, feed rates, flow rates, screening, treatments and possible problems.

O fluxo de massa do Vieira, Teresópolis-RJ, megadesastre da serra em 2011: análise das feições sedimentológicas e de sua fenomenalogia

Em janeiro de 2011, o grande número de escorregamentos naturais e induzidos que afetaram a Região Serrana do Estado do Rio de Janeiro, durante o Megadesastre, são processos destruidores de grande impacto, mas com tempo de recorrência maior. Em particular a bacia do rio Vieira (noroeste de Teresópolis), afetada pelo evento, apresentou magnitude espetacular do desastre registrado, com os materiais mobilizados em fluxos gravitacionais de massa atingindo quilômetros de distâncias das suas escarpas principais, o que causou, horas depois, prejuízos significativos. A pesquisa da presente dissertação discutiu a caracterização destes processos e dos ambientes deposicionais, a partir da análise das feições sedimentológicas e apreciação das características mecânicas, do vale do rio Vieira para estabelecer base de conhecimento da evolução da paisagem local. O método de trabalho utilizou o reconhecimento dos condicionantes geológicos e a leitura do registro sedimentar. A corrida de massa do Vieira foi zoneada em diferentes estágios de comportamento baseado na classificação de fluxos gravitacionais de massa de Middleton e Hampton (1973). Esta classificação é adequada para linha de pesquisa, pois os autores definem fluxos gravitacionais de sedimentos como um termo geral para fluxos de sedimentos ou misturas sedimentos/fluidos, que fluem sob a ação da gravidade. Os resultados obtidos caracterizam o fenômeno do ponto de vista geológico, estratigráfico e geomorfológico. Uma corrida de massa afetou o canal do rio Vieira desde a sua nascente, na cota 1750m, até o fim da sua planície de inundação, na cota 900m; o movimento de massa com extensão de 7,5km, 30-100m de largura máxima e 4m de espessura média, causou diretamente 86 mortes e a destruição de casas e lavouras da zona rural do bairro Vieira, Teresópolis-RJ. O fluxo gravitacional do Vieira aparentemente contou com diferentes condicionantes e envolveu diferentes fases, passando pelo debrisflow e pelo mudflow, provavelmente em diferentes pulsos, e no seu estágio final para o waterflow.

Construção e operação de wetland como polimento de lixiviado de aterro de resíduos sólidos urbanos.

O presente trabalho tem o objetivo de avaliar a metodologia de construção, de plantio, de manutenção, de operação e a eficiência de um sistema de tratamento por wetland construído como etapa de polimento da Estação de Tratamento de Lixiviado (ETC) de Aterro já encerrado de Resíduos Sólidos Urbanos na Região Metropolitana do Rio de Janeiro. Parte do efluente tratado por lodos ativados na ETC foi direcionado e tratado no wetland construído. Foi escolhido o projeto de Fluxo Horizontal Subsuperficial e a vegetação selecionada foi a taboa (Typha latifolia) que é nativa da área do aterro. Em média, foram feitas três amostragens mensais do afluente e do efluente do wetland, de maio a outubro de 2013. A eficiência do sistema foi avaliada por meio de parâmetros físico-químicos e de parâmetros coletivos específicos. A eficiência de remoção de Demanda Química de Oxigênio (DQO) foi de 60%, nitrogênio amoniacal de 67%, nitrito de 72% e nitrato de 57%. Outro parâmetro avaliado foi a toxicidade aguda, foram utilizados os organismos teste Danio rerio (peixe), a Daphnia similis (microcrustáceo) e a Aliivibrio fischeri (bactéria luminescente). Durante o período foram coletados diariamente as vazões de entrada e saída, a condutividade elétrica e o índice pluviométrico. Os resultados mostraram que o uso de wetland como etapa de polimento pode ser uma alternativa para o tratamento de lixiviado.

Aplicação de técnicas de otimização no gerenciamento da deposição em redes de trocadores de calor

Deposição é um fenômeno indesejável que ocorre na superfície dos trocadores de calor ao longo de sua operação, ocasionando redução na efetividade térmica e aumento da resistência ao escoamento nestes equipamentos. Estes efeitos trazem grandes consequências econômicas e ambientais, devido ao aumento dos custos operacionais (energia adicional é requerida), aumento dos custos de projeto (demanda por equipamentos de maior área de troca térmica), limitações hidráulicas (que pode levar a uma diminuição da carga processada) e aumento das emissões (aumento da queima de combustíveis fósseis para suprir a energia adicional requerida). Neste contexto, o presente trabalho tem por objetivo fornecer ferramentas computacionais robustas que apliquem técnicas de otimização para o gerenciamento da deposição em redes de trocadores de calor, visando minimizar os seus efeitos negativos. Estas ferramentas foram desenvolvidas utilizando programação matemática no ambiente computacional GAMS, e três abordagens distintas para a resolução do problema da deposição foram pesquisadas. Uma delas consiste na identificação do conjunto ótimo de trocadores de calor a serem limpos durante uma parada para manutenção da planta, visando restaurar a carga térmica nesses equipamentos através da remoção dos depósitos existentes. Já as duas outras abordagens consistem em otimizar a distribuição das vazões das correntes ao longo de ramais paralelos, uma de forma estacionária e a outra de forma dinâmica, visando maximizar a recuperação de energia ao longo da rede. O desempenho destas três abordagens é ilustrado através de um conjunto de exemplos de redes de trocadores de calor, onde os ganhos reais obtidos com estas ferramentas de otimização desenvolvidas são demonstrados