Modeling of burden distribution in the blast furnace

The blast furnace is the main ironmaking production unit in the world which converts iron ore with coke and hot blast into liquid iron, hot metal, which is used for steelmaking. The furnace acts as a counter-current reactor charged with layers of raw material of very different gas permeability. The arrangement of these layers, or burden distribution, is the most important factor influencing the gas flow conditions inside the furnace, which dictate the efficiency of the heat transfer and reduction processes. For proper control the furnace operators should know the overall conditions in the furnace and be able to predict how control actions affect the state of the furnace. However, due to high temperatures and pressure, hostile atmosphere and mechanical wear it is very difficult to measure internal variables. Instead, the operators have to rely extensively on measurements obtained at the boundaries of the furnace and make their decisions on the basis of heuristic rules and results from mathematical models. It is particularly difficult to understand the distribution of the burden materials because of the complex behavior of the particulate materials during charging. The aim of this doctoral thesis is to clarify some aspects of burden distribution and to develop tools that can aid the decision-making process in the control of the burden and gas distribution in the blast furnace. A relatively simple mathematical model was created for simulation of the distribution of the burden material with a bell-less top charging system. The model developed is fast and it can therefore be used by the operators to gain understanding of the formation of layers for different charging programs. The results were verified by findings from charging experiments using a small-scale charging rig at the laboratory. A basic gas flow model was developed which utilized the results of the burden distribution model to estimate the gas permeability of the upper part of the blast furnace. This combined formulation for gas and burden distribution made it possible to implement a search for the best combination of charging parameters to achieve a target gas temperature distribution. As this mathematical task is discontinuous and non-differentiable, a genetic algorithm was applied to solve the optimization problem. It was demonstrated that the method was able to evolve optimal charging programs that fulfilled the target conditions. Even though the burden distribution model provides information about the layer structure, it neglects some effects which influence the results, such as mixed layer formation and coke collapse. A more accurate numerical method for studying particle mechanics, the Discrete Element Method (DEM), was used to study some aspects of the charging process more closely. Model charging programs were simulated using DEM and compared with the results from small-scale experiments. The mixed layer was defined and the voidage of mixed layers was estimated. The mixed layer was found to have about 12% less voidage than layers of the individual burden components. Finally, a model for predicting the extent of coke collapse when heavier pellets are charged over a layer of lighter coke particles was formulated based on slope stability theory, and was used to update the coke layer distribution after charging in the mathematical model. In designing this revision, results from DEM simulations and charging experiments for some charging programs were used. The findings from the coke collapse analysis can be used to design charging programs with more stable coke layers.

Culturing the African lungfish in Uganda: effects of exogenous fish feed on growth performance in tanks

The availability of African lungfish (Protopterus aethiopicus) in many communities in Uganda is declining. Indigenous efforts to culture this fish usually produce poor yields and depend on feeding fish fry, minced meat, and leftover food. This study evaluates three formulated diets (diet-1, diet-2, diet-3) fed to wild caught lungfish fingerlings reared in indoor tanks for 77 days. Experimental fish gradually accepted sinking pellets, and marginal increases in average body weight were observed. Mean (± SE) final weight (15.86 ± 0.80 g) for fish fed on diet-3 was significantly higher (p < 0.05) than fish fed diet-1 and diet-2. Specific growth rates (SGR) for diet- 3 were significantly higher (p < 0.05) than diet-1, and marginally more than diet-2 (0.37 ± 0.04 %/ d). Feed conversions were similar (p >0.05), ranging from 1.61 ± 0.26 to 2.07 ± 0.11. Survivals after an 11-week culture were relatively low (< 60%), but generally increased (R2 = 0.667, P = 0.007) with increasing dietary proteins. Diet-3 had a significant higher survival rate (p< 0.05) than diet-1 and diet-2. Significant growth performance was attained with diet-3. This study demonstrated that sinking fish feed pellets can be used to culture wild-caught African fingerlings in captivity.

Características do gás durante a gasificação de biomassa em leito fluidizado

Durante os últimos anos, a procura mundial de recursos energéticos renováveis tem sofrido um grande aumento. Neste grupo insere-se a biomassa, cuja conversão termoquímica, principalmente através de tecnologias de combustão e gasificação, é utilizada para a produção de energia térmica e elétrica. No processo de gasificação de biomassa é possível obter um combustível gasoso secundário com variadas aplicações, podendo inclusive servir como substituto do gás natural. No entanto, ao contrário da combustão, esta tecnologia aplicada à biomassa ainda está em fase de demonstração a nível industrial, apresentando algumas limitações em alguns aspetos tecnológicos, entre os quais a qualidade do gás produzido. Neste contexto, e com o objetivo de contribuir para o conhecimento da aplicabilidade desta tecnologia, surge o presente trabalho, onde a caracterização e definição das condições de operação de um gasificador de biomassa, bem como a caracterização do gás produzido foram objeto de estudo. Foi realizado um conjunto de experiências de gasificação direta, num reator de leito fluidizado borbulhante à escala piloto, com dois tipos de biomassa tipicamente encontrados em Portugal, e para diferentes condições de operação do gasificador, nomeadamente no que diz respeito à razão de equivalência. A biomassa utilizada consistiu em pellets comerciais de madeira e estilha de biomassa florestal residual derivada de pinheiro (Pinus pinaster), e resultante de operações florestais em Portugal. Na gama de temperatura do leito aplicada, tipicamente entre 800ºC e 875ºC, o reator funcionou em condições auto térmicas, isto é, sem a necessidade de recorrer a uma fonte de calor auxiliar externa. Em relação à composição do gás seco durante o processo de gasificação, os gases presentes em maior percentagem (em volume), para as experiências com ambos os tipos de biomassa, são o CO2 e o CO, com o primeiro a registar valores médios entre os 13.4% e os 16%, e o segundo entre 11.3% e 16.3%. Por ordem decrescente de concentração encontra-se o H2, na gama de 5.8% a 12.7%, o CH4 com valores médios entre 2.8% e 4.5%, e o C2H4 com concentrações médias entre 1.0% e 2.2%. Importa referir ainda a ausência de O2 no gás produzido. Verificou-se na concentração de H2, a principal diferença na composição do gás seco relativamente à gasificação dos dois combustíveis utilizados, com valores de concentração inferiores durante a operação com estilha de biomassa florestal residual derivada de pinheiro. Nas várias experiências realizadas, e para as condições operatórias utilizadas, observou-se que a razão de equivalência (RE) exerce um efeito significativo na composição do gás, verificando-se, genericamente, que com o aumento da RE a concentração de gases combustíveis diminui. Os valores de Poder Calorífico Inferior (PCI) obtidos para o gás seco produzido encontram-se na gama 3.4-5.6 MJ/Nm3, sendo que os valores mais elevados foram registados no decorrer dos ensaios de gasificação com pellets de madeira. Para ambos os combustíveis, o PCI do gás seco diminui com o aumento da RE.

Microplastics in sediments: A review of techniques, occurrence and effects

Microplastics are omnipresent in the marine environment and sediments are hypothesized to be major sinks of these plastics. Here, over 100 articles spanning the last 50 year are reviewed with following objectives: (i) to evaluate current microplastic extraction techniques, (ii) to discuss the occurrence and worldwide distribution of microplastics in sediments, and (iii) to make a comprehensive assessment of the possible adverse effects of this type of pollution to marine organisms. Based on this review we propose future research needs and conclude that there is a clear need for a standardized techniques, unified reporting units and more realistic effect assessments.

Effects of sodium hyaluronate and triamcinolone acetonide on proteoglycan metabolism in equine articular chondrocytes treated with interleukin-1

The objective of this study is to determine if the effects of a high molecular weight sodium hyaluronate (HA) alone or in combination with triamcinolone acetate (TA) can mitigate chondrocyte proteoglycan catabolism caused by interleukin-1 (IL-1) administration. Chondrocytes were collected from fetlock joints of ten horses euthanized for reasons unrelated to joint disease. Chondrocyte pellets were treated with media (negative control); media containing IL-1 only (positive control); or media containing IL-1 with HA only (0.5 or 2.0 mg/mL), TA only (0.06 or 0.6 mg/mL), or HA (0.5 or 2.0 mg/mL) and TA (0.06 or 0.6 mg/mL) in combination. Chondrocyte pellets were assayed for newly synthesized GAG, total GAG content, total DNA content, and mRNA levels of collagen type II, aggrecan, and COX-2. The high concentration of HA (2.0 mg/mL) increased GAG synthesis while the high concentration of TA (0.6 mg/mL) decreased loss of GAG into the media. Both the high concentration of HA and TA increased the total GAG content within the pellet. There was no change in pellet DNA content with either treatment. TA reduced COX-2 mRNA levels as well as aggrecan and collagen type II expression. Treatment with HA had no effect on mRNA levels of COX-2, aggrecan or collagen type II. These results indicate that the high concentration of HA or TA alone or in combination will mitigate effects of IL-1 administration on proteoglycan catabolism of equine articular chondrocytes.

Gasificação de biomassa num reator de leito fluidizado à escala piloto

A gasificação de biomassa permite a produção de um gás combustível com capacidade para reduzir o consumo de combustíveis fósseis. Contudo, para promover a utilização deste processo a nível industrial é necessário ultrapassar diversas limitações e elaborar tecnologias de gasificação que sejam mais rentáveis e eficientes. No presente trabalho efetuou-se a gasificação direta com ar, num reator auto-térmico com um leito fluidizado borbulhante, de diferentes tipos de biomassa provenientes da floresta portuguesa, nomeadamente pellets de madeira e diferentes tipos de biomassa florestal residual derivada de eucalipto. A investigação foi realizada numa instalação à escala piloto localizada no Departamento de Ambiente e Ordenamento da Universidade de Aveiro. A infraestrutura foi desenvolvida de modo a permitir o estudo do processo de gasificação de biomassa. O reator utilizado apresenta 3 metros de altura, consistindo a câmara de gasificação em 2.25 metros, 0.25 metros de diâmetro interno e uma potência entre 40 e 70 kWth. O leito é composto por areia (partículas com granulometria entre os 355 e 1000 µm) e tem uma altura de 0.23 m. A infraestrutura experimental oferece condições para efetuar a gasificação de biomassa, determinar a composição do gás produzido em termos de CO, CO2, H2, N2, CH4 e C2H4 e efetuar a sua combustão num queimador localizado a jusante do reator. O leito fluidizado operou com temperaturas médias entre os 700 e 850ºC. Para as razões de equivalência estabelecidas, entre 0.17 e 0.36, o gás seco apresentou uma composição que, em termos volumétricos e em função das condições operatórias, variou entre 14.0 a 21.4% CO, 14.2 a 17.5% CO2, 3.6 a 5.8% CH4, 1.3 a 2.4% C2H4, 2.0 a 10.2% H2 e 48.9 a 61.1% N2. A maior concentração de CO, CH4 e C2H4 foi observada durante a gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.17, contudo, a maior concentração de H2 foi obtida na gasificação de pellets de madeira com razão de equivalência de 0.25. Tendo em conta a composição gasosa, o poder calorífico inferior do gás seco encontrou-se entre 4.4 e 6.9 MJ/Nm3 e os valores mais elevados foram observados durante os processos de gasificação efetuados com menor razão de equivalência. A produção específica de gás variou entre 1.2 e 2.2 Nm3/kg biomassa bs, a eficiência do gás arrefecido entre 41.1 e 62.6% e a eficiência de conversão de carbono entre 60.0 e 87.5%, encontrando-se na gama dos valores reportados na literatura. A melhor condição, em termos da eficiência de gás arrefecido, consistiu na gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.25, e em termos da produção específica de gás seco e eficiência de conversão de carbono, na gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.35. Contudo, o gás com maior poder calorífico inferior foi obtido durante a gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.17. O reator demonstrou adequabilidade na gasificação de diferentes tipos de biomassa e foram observadas condições estáveis de operação, tanto em termos de temperatura como da composição do gás produzido. Geralmente, o gás apresentou propriedades combustíveis apropriadas para ser comburido de forma contínua e estável pelo queimador de gás, sem ser necessária uma fonte de ignição permanente ou a utilização de um combustível auxiliar.

Production responses of reproducing ewes to a by-product-based diet inoculated with the probiotic Bacillus amyloliquefaciens strain H57

The potential application of the spore-forming probiotic Bacillus amyloliquefaciens strain H57 (H57) as a novel probiotic for ruminants was evaluated in reproducing ewes. Performance responses were determined by delivering H57 in a pelleted diet based mainly on palm kernel meal (PKM) and sorghum grain. PKM is an agro-industrial by-product with a reputation for poor palatability and the availability of the starch in sorghum grain can be limited in ruminants. The hypothesis was that H57 improves the feeding value of a relatively low quality concentrate diet. Twenty-four first-parity white Dorper ewes were fed PKM-based pellets manufactured with or without H57 (109 cfu/kg pellet) in late pregnancy. During this phase of late pregnancy, the H57 ewes ate 17% more dry matter (1019 vs 874 g/day, P = 0.03), gained more weight (194 vs 30 g/day, P = 0.008) and retained more nitrogen (6.13 vs 3.34 g/day, P = 0.01), but produced lambs with a similar birthweight (4.1 vs 4.2 kg, P = 0.73). Rumen fluid collected from H57 ewes in late pregnancy had higher pH (7.1 vs 6.8, P = 0.07), acetate : propionate ratio (3.4 vs 2.7, P = 0.04), lower ammonia (69 vs 147 mmol/L, P = 0.001) and total volatile fatty acid concentrations (40 vs 61 mg/L, P = 0.02). The digestibility of dry matter, organic matter and fibre were similar between the two groups. The lambs of the H57 ewes grew faster than those of the Control ewes for the first 21 days of lactation (349 vs 272 g/day, P = 0.03), but not thereafter. H57 can improve feed intake and maternal liveweight gain in late pregnancy of first-parity ewes fed a diet based on PKM.

Pilot scale production of sea bass (Dicentrarchus labrax) fry

Determination of rearing data enabled production of sea bass fry for three years in Station DEVA-SUD, CNEXO, France. The larval breeding process is described. The food consists of the ROlÎfer Brachionus plicatilis, then nauplii and 1 mm long metanauplii of the Brachiopod Artemia salina. Weaning on dry pellets oceurs when larvae are 35 days old when an optimum temperature curve is respected. Production of season 1977-78 was 380 000 two month old weaned fry.

Sinterização de Ce1-XEuXO2-(X/2) para aplicação como eletrólito sólido em células a combustível de temperaturas intermediárias

Given the environmental concern over global warming that occurs mainly by emission of CO2 from the combustion of petroleum, coal and natural gas research focused on alternative and clean energy generation has been intensified. Among these, the highlight the solid oxide fuel cell intermediate temperature (IT-SOFC). For application as electrolyte of the devices doped based CeO2 with rare earth ions (TR+ 3) have been quite promising because they have good ionic conductivity and operate at relatively low temperatures (500-800 ° C). In this work, studied the Ce1-xEuxO2-δ (x = 0,1, 0,2 and 0,3), solid solutions synthesized by the polymeric precursor method to be used as solid electrolyte. It was also studied the processing steps of these powders (milling, compaction and two step sintering) in order to obtain dense sintered pellets with reduced grain size and homogeneous microstructure. For this, the powders were characterized by thermal analysis, X-ray diffraction, particle size distribution and scanning electrons microscopy, since the sintered samples were characterized by dilatometry, scanning electrons microscopy, density and grain size measurements. By x-ray diffraction, it was verified the formation of the solid solution for all compositions. Crystallites in the nanometric scale were found for both sintering routes but the two step sintering presented significant reduction in the average grain size

Adsorção de Pb(II) utilizando adsorvente composto por montmorilonita e dolomita

The destructive impact of improper disposal of heavy metals in the environment increases as a direct result of population explosion, urbanization and industrial expansion and technological developments. Argil are potential materials for adsorption of inorganic and the pelletization of it is required for use in adsorptive columns of fixed bed. The low cost and the possibility of regeneration makes these materials attractive for use in the purification process, capable of removing inorganic compounds in contaminated aquatic environments. In this work was made pellets of a mixture of dolomite and montmorillonite by wet agglomeration, in different percentages. The removal of Pb (II) was investigated through experimental studies, and was modeled by kinetic models and isotherms of adsorption. The materials were characterized using the techniques of XRD, TG / DTA, FT-IR, and surface area by BET method. The results showed the adsorption efficiency of the contaminant by the composite material studied in synthetic solution. The study found that the adsorption follows the Langmuir model, and the kinetics of adsorption follows the model of pseudosecond order

SEDIMENT BIOTURBATION POTENTIAL of UCA RAPAX and UCA URUGUAYENSIS AS A RESULT of THEIR FEEDING ACTIVITY

Bioturbation of mangrove sediments by Uca uruguayensis (Nobili, 1901) and U. rapax (Smith, 1870) was compared based on the grain-size composition and organic content in surface sediment around the burrow and feeding pellets in two mangrove zones of the Sao Vicente Estuary, state of São Paulo, Brazil. For each species, 25 burrows with active crabs were selected. All pellets within a 15-cm radius of each burrow were carefully collected; samples of substrate were taken; and the crab occupant was excavated, sexed, and measured for carapace width (CW). The number of spoon-tipped setae on the second maxilliped of each species was estimated; U. uruguayensis showed more of these setae than U. rapax. For both species, the sediment post-processed by feeding activity (feeding pellets) showed a similar increase of coarser fractions and a smaller organic content. However. U. uruguayensis was more efficient in removing organic matter (88.1%) from the sediment than U. rapax (37.5%). These results suggest that different numbers of spoon-tipped setae on the second maxillipeds of the fiddler crabs do not affect the potential for grain-size selection, but result in differing abilities to remove organic matter from the sediment.

Bioadsorción de Pb2+ en una columna empacada con biomasa inmovilizada

Se realizó la bioadsorciónde Pb2+ a escala laboratorio utilizando una columna empacada con biomasa de alga Chlorella sp. inmovilizada en pellets de alginato de calcio, variando el tamaño de partícula, el pH, y la concentraciónde Pb2+.