Constata-se, atualmente, uma grande demanda de crescimento na produção de painéis MDF de madeira de eucalipto em relação à do pinus, comumente utilizada na indústria. Pelo exposto, o presente trabalho teve como objetivo caracterizar os componentes morfológicos da madeira de cavacos de Eucalyptus grandis, “in natura” e submetidas a três condições diferentes de desfibramento (tempo, pressão e energia), sendo denominadas de condição intermediária, de menor e de maior intensidade de refino (A, B e C, respectivamente). As características tecnológicas das chapas MDF obtidas para as três condições de desfibramento foram, da mesma forma, analisadas segundo a norma NBR 15316. No desenvolvimento do trabalho foram coletados para as três condições de desfibramento, em toda a cadeia produtiva do painel MDF: cavacos de madeira, material lenhoso desfibrado e painéis MDF final em escala industrial e laboratorial. Os cavacos de madeira foram caracterizados com respeito a sua estrutura microscópica; o material lenhoso desfibrado nas 3 condições foi avaliado através do seu fracionamento em peneiras seguindo-se a classificação morfológica e a caracterização microscópica dos componentes celulares de cada fração. Os resultados mostraram que os cavacos de madeira coletados no silo da unidade fabril apresentaram-se homogêneos nas 3 pré-condições avaliadas e não exerceram qualquer influência nos tratamentos. A condição de desfibramento mais branda induziu a formação de feixes de fibra e manutenção de vasos e parênquima com as fibras apresentando maior comprimento médio. A condição de desfibramento mais drástica induziu o rompimento da parede das fibras, com polpa apresentando fibras de menor comprimento e com baixa freqüência de vasos e de parênquima. As características de coloração foram observadas, sendo que a massa de fibras mais escura foi decorrente da alta pressão, maior tempo e mais energia de refinação aplicada. Os painéis MDF obtidos na condição mais branda apresentaram maior resistência ao arranque de parafuso, ao contrário dos painéis MDF confeccionados com polpa da condição de desfibramento mais drástica mostrando menores propriedades mecânicas de resistência à tração perpendicular e superficial e maiores valores de inchamento e de absorção. Os resultados do trabalho evidenciam a importância das variáveis de produção relacionadas com os tratamentos da madeira e do material fibroso nas propriedades tecnológicas dos painéis MDF de eucalipto. / Currently is evidenced a great demand of growth in eucalypts MDF panels production in relation with pinus, commonly used in the industry. The present study had the objective to characterize the morphologic components of Eucalyptus grandis wood chips “in natura” submitted in three different refining conditions (time, pressure and energy), named intermediate, smaller and biggest intensity of refining (A, B and C, respectively). The technological characteristics of MDF panels from three refining conditions were analyzed according standard NBR 15316. During this development were collected for three refining conditions, in all the productive chain of the MDF panels: wood chips, wooden dissociated material and panels MDF in industrial and laboratorial scale. The wood chips structure were microscopically characterized; the dissociated wood cells suspended in water of 3 refining conditions were evaluated through its separation in sieves and each fraction of woody material was morphologically classified and microscopically described. The results showed that the wood chips collected in industry storage compartment were homogeneous in the 3 refining preconditions and not influenced the MDF panel's treatments. The softness refining condition induced the shives formation and maintenance of vessels, parenchyma and the longest fibers. The more drastic refining condition induced the fiber cell walls broking, with wood pulp presenting shortest fibers and lower vessels and parenchyma frequency. The coloration characteristics were observed, and the fiber pulp was darker as result of the high pressure, greater time and more refinement energy applied. The MDF panels elaborated by softness refining condition presented greater resistance to screw pull in contrast of panels confectioned with hardness refining condition showing lesser mechanical properties of perpendicular and superficial tensile strength and bigger values of swelling and absorption. The results showed the importance of the variable related production with the wood and pulp wood treatments in technological properties of eucalypts MDF panels.

Nesse trabalho foi estudada uma técnica para a detecção de OHTC na água salina. Descobriu-se que certos complexos de rutênio em determinados valores de pH reagem com a molécula de OHTC e isto é detectável por espectrofotometria UV-Vis. Foram estudados os complexos fac-[RuCl2(S-DMSO)3(O-DMSO)] (complexo 1), {[(DMSO)2H][trans-RuCl4(DMSO)2]} (complexo 2) e cis-[RuCl2(bpy)2].2H2O (complexo 3). O complexo 1 possui um dos ligante (O-DMSO) que pode ser substituído pelo OHTC. Já o complexo 2 possui um dos ligantes (S-DMSO) na posição trans um ao outro, e o complexo 3 possui os 2 íons Cl- para tal finalidade. Determinou-se que o complexo 1 é viável, mesmo em presença de sais presentes na água do mar. Assim a reação foi realizada em função do tempo, variação do pH, temperatura e concentração de OHTC. Nos outros dois complexos os estudos foram realizados sem a variação da temperatura e concentração de OHTC. / p>In this work we studied a technique for detection of OHTC in water. It was discovered that complexes involving ruthenium, on determined pH values, react with the OHTC molecule and this is detectable by UV-VIS spectroscopy. The complexes fac-[RuCl2(S-dmso)3(O-dmso)] (complex 1), {[(DMSO)2H][trans-Ru(DMSO)2Cl4]} (complex 2), and cis-[RuCl2(bpy)2].2H2O (complex 3) were studied. The complex 1 present one position ( O - DMSO) which can be substituted by the OHTC. Additionally, the complex 2 present two ligands ( S- DMSO) trans between each other, and the complex 3 present two chloride ions for the same porpose of complex 1 respectively. It was determined that the complex 1 was able to react with OHTC even in presence of the salts present in sea water. Thereby, the reaction involving complex 1 and OHTC was monitored in function of the time, pH, temperature, and finally concentration of OHTC. On the other two complexes, the reaction was studied without variation of temperature and concentration of OHTC.

[pt] O mercado brasileiro de derivados de petróleo está sendo aberto para competição este ano, saindo de um ambiente de preços regulados pelo Governo Federal para um ambiente onde os preços são estabelecidos pelas leis de oferta e demanda. Neste contexto, existe a preocupação de como serão estes preços, e seus impactos sobre os consumidores e sobre os produtores locais. Esta Tese propõe alguns modelos matemáticos para estimar preços, níveis de produção, níveis de consumo (demanda), e importação e exportação de derivados de petróleo nas diversas regiões do mercado brasileiro. O fornecimento de derivados de petróleo não é considerado um mercado competitivo, e sim oligopolizado, principalmente no curto prazo, devido à capacidade instalada de refinarias e aos altos custos envolvidos na construção de novas refinarias. Estes modelos são multi- produto, considerando um fato importante na produção de derivados que é a impossibilidade de produzir apenas um derivado. Assim, existem restrições onde a oferta de um derivado é relacionada a oferta dos outros. O primeiro modelo considera um mercado de oligopólio fechado, com um número fixo de firmas. Tal modelo é formulado como um problema de equilíbrio a Nash. Um segundo modelo é apresentado expandindo o primeiro para o caso em que existem preços teto de demanda definidos politicamente. O terceiro modelo relaxa a suposição do mercado fechado, com número fixo de firmas, e considera a possibilidade de competição de novas firmas no mercado. Um quarto modelo é discutido, onde assume-se que existe uma firma líder no mercado, que consegue definir sua estratégia antes das demais firmas, semelhante ao problema econômico de Stackelberg. Todos os modelos foram formulados como problemas de inequações variacionais, sendo que o último modelo é ainda um problema de programação binível. Algoritmos de solução são propostos para os três primeiros modelos. Simulações sobre o mercado brasileiro de derivados são apresentadas. / [en] The Brazilian petroleum refined products market is being opened to competition this year, leaving an environment of regulated prices to another one where the prices are defined by the supply demand interactions. Considering this new scenario, there is a concern about how high the prices will be, and about their impact on the consumers and on the local producers. This thesis proposes some mathematical models to predict prices, production, consumption, and import and export levels of petroleum-refined products in all the sub-regions of the Brazilian market. Instead of a competitive market, the supply of refined products is considered an oligopoly market, especially in the short term, given the already installed refining capacity and the high costs involved in building new refineries. These models are multi-products, and they consider an important characteristic of the production of refined products, the impossibility of producing only one refined product. Hence, constraints where the production of one refined product is related to the production of the others are considered. The first model considers a closed oligopoly market, with a fixed number of firms. This problem is formulated as a Nash equilibrium problem. A second model is presented generalizing the first one to consider the possibility of ceiling demand prices politically defined. The third model relaxes the assumption of a fixed number of firms in the first model, and considers the possibility of competition by new entrants. A fourth model is discussed, where it is assumed that there is a leader firm in the market, which can define its strategy before the other firms, similar to the economic problem of Stackelberg. All the models are formulated as variational inequalities problems, and the last model is also a bi-level programming problem. Solution algorithms for the three first models are proposed. Some analyses of the Brazilian petroleum refined- products market are presented.

"April 2004" / Bibliography: leaves 319-342. / viii, 387 leaves : ill., maps ; 30 cm. / Title page, contents and abstract only. The complete thesis in print form is available from the University Library. / Thesis (Ph.D.)--University of Adelaide, School of History and Politics, Discipline of History, 2004

The increased concentration of greenhouse gases in theatmosphere, in particular CO2, is changing the Earth’s climate. Accordingto the Kyoto protocol, where the international community agreedon binding emission targets, developed countries are committedto reduce their greenhouse gas emissions. The increased use ofbiomass in energy systems is an important strategy to reduce CO2emissions. The purpose of this thesis has been toanalyse the opportunities for Sweden to further reduce CO2emissions in the energy system, by rationallyutilising woody biomass energy. The characteristics of currentcommercially operating biofuel-based CHP plants in Sweden aresurveyed and systematically presented. A consistent andtransparent comprehensive reference base for system comparisonsis given. Furthermore, the fuel effectiveness and contributionto CO2reduction is calculated. The governmentalsubsidies of the CHP plants’investment, expressed as costof specific CO2reduction, appears to be low. The competitiveness of biomass-fuelled energy production inrelation to fossil-based production with carbon capture isanalysed, showing that the biomass-fuelled systems provide acompetitive option, in terms of cost of electricity andefficiencies. The remaining Swedish woody biofuel potential ofat least 100 PJ/yr is principally available in regions with abiomass surplus. Transportation is therefore required to enableits utilisation in a further national and international market.Refining the biofuel feedstock to pellets, or even furtherrefining to motor fuels (DME, methanol or ethanol) or power,could facilitate this transport. Different options for fuelrefining are studied and compared. The entire fuel chain, fromfuel feedstock to end users, is considered and CO2emissions are quantified. Substituting fuelpellets for coal appears to be the most costeffectivealternative and shows the largest CO2reduction per energy unit biofuel. Motor fuelsappear more costly and give about half the CO2reduction. Transportation of the upgraded biofuelpellets is highly feasible from CO2emissions point of view and does not constitute ahindrance for further utilisation, i.e. the pellets can betransported over long distances efficiently with only limitedemissions of CO2. Bioenergy utilisation has additional features forenvironmental improvement, apart from the CO2aspect. Waste heat from biofuel-based CHP can becost-effectively used in conjunction with sewage treatment. Theincoming sewage water to the nitrification process can bepreheated with the waste heat, and thereby substantiallyenhance the nitrification and the reduction of ammoniumnitrogen during the winter season. <b>Keywords:</b>CO2reduction, energy system, biofuel, CHP, refining,fuel pellets, ethanol, methanol, DME, fuel substitution, sewagewater, nitrification.

Impurity optimized silicon is needed for the advancement of terrestrial photovoltaic power generation. In this study the possibility of producing solar grade silicon from rice husks has been pursued. An integrated process flowsheet was developed and practiced that included initial leaching, reduction of Rice husk ash (RHA) and post-reduction purification of silicon. Metallothermic reduction of purified RHA with magnesium was investigated within the temperature range of 500-950 oC. The reduction product was purified by two stage acid leaching sequence. Analysis of the final silicon powder product by XRD and ICP-OES showed crystalline silicon with boron content to be less than 3ppm- corresponding to reduction by a factor greater than 10, whilst the phosphorus content was reduced by a factor of over 20 and reaching less than 73ppm. The effects of temperature, magnesium amount and leaching agents were optimized in this study. A one step test melting was also carried out to convert the silicon powder into silicon chunks.

Impurity optimized silicon is needed for the advancement of terrestrial photovoltaic power generation. In this study the possibility of producing solar grade silicon from rice husks has been pursued. An integrated process flowsheet was developed and practiced that included initial leaching, reduction of Rice husk ash (RHA) and post-reduction purification of silicon. Metallothermic reduction of purified RHA with magnesium was investigated within the temperature range of 500-950 oC. The reduction product was purified by two stage acid leaching sequence. Analysis of the final silicon powder product by XRD and ICP-OES showed crystalline silicon with boron content to be less than 3ppm- corresponding to reduction by a factor greater than 10, whilst the phosphorus content was reduced by a factor of over 20 and reaching less than 73ppm. The effects of temperature, magnesium amount and leaching agents were optimized in this study. A one step test melting was also carried out to convert the silicon powder into silicon chunks.

Thermal recovery methods are frequently used to enhance the production of heavy crude oils. Steam-based processes are the most economically popular and effective methods for heavy oil recovery for several decades. In general, there are various mechanisms over steam injection to enhance and have additional oil recovery. However, among these mechanisms, steam distillation plays pivotal role in the recovery of crude oil during thermal recovery process. In this study, an experimental investigation was carried out to investigate the role of various minerals present in both sandstone and carbonate formations as well as the effect of steam temperature on steam distillation process. Two different types of dead-heavy crude oils were tested in a batch autoclave reactor with 30 % water and the content of the reactor (crude oil, 10 % rock and mineral). The results were compared as the changes in the density, viscosity and chemical composition (SARA and TPH analyses) of heavy crude oil. Five different mineral types (bentonite, sepiolite, kaolinite, illite and zeolite) were added into the original crude oil and reservoir rocks to observe their effects on the rheological and compositional changes during steam distillation process. Analysis of the results of experiments with Camurlu and Bati Raman heavy crude oils in the presence of different minerals such as Bentonite, Zeolite, Illite, Sepiolite, and Kaolinite in both sandstone and limestone reservoir rocks indicate that steam distillation produces light end condensates which can be considered as solvent or condensate bank during steam flooding operation. It was also illustrated that minerals in reservoir formations perform the function of producing distilled light oil compounds, resulting in enhancement of heavy crude oils recovery in steam flooding. Measurements showed that the remaining oil after steam distillation has higher viscosity and density. On the other hand, the effect of steam distillation is more pronounced in limestone reservoirs compared to sandstone reservoirs for the given heavy crude oil and steam temperature. Among the five different minerals tested, kaolinite found to be the most effective mineral in terms of steam distillation.

Detta examensarbete är en förundersökning till Glafos undersökning angående rening av glasbrukens processvatten från antimon med zeolit. Förundersökningen gick ut på att via experiment ta reda på hur mycket antimon som adsorberas av behandlad (för optimering: dels med NaNO3 och dels med NaCl) och obehandlad zeolit (porstorlek 0.4 nm). pH mättes och ställdes eftersom det har betydelse för adsorptionen, åtminstone vid väldigt lågt pH. När lösningarna hade filtrerats mättes den kvarvarande antimonhalten med atomabsorptionsspektrofotometri. Mätningarna visade att i genomsnitt 53 % av Sb-halten i lösningarna hade adsorberats av zeoliten. Förundersökningen visade att det inte blir någon adsorption då pH är väldigt lågt (under 1). Den visade också att när pH är över 4 verkar det inte ha någon betydelse om zeoliten är behandlad eller inte. Zeoliten bör behandlas med NaCl först i en tank med omrörning, sedan blandas i processvattnet (vars pH justerats till pH 4) i en tank eller bassäng och därefter filtreras. Tidsfaktorn för hur lång tid det tar för zeoliten att nå jämvikt och temperaturens inverkan bör även undersökas. / The aim of this diploma work is to study the removal of antimony from glassworks process water using zeolites. The experimental part of the studies were carried out to find the quantity of antimony adsorbed by the zeolite. The studies included treated (for optimization: partly with NaNO3 and partly with NaCl) and untreated zeolite. The pore size is 0.4 nm. pH was measured and adjusted because it is important for the antimony adsorption. When the solutions were filtrated the content of antimony left was measured with atomic absorption spectrophotometry. The measurements showed an average uptake of antimony by the zeolite of 53 %.The preinvestigation indicates that with a very low pH (below 1) there is no antimony adsorption. It also indicates that with pH above 4 it does not matter if the zeolite are treated or not. In further investigations the zeolite should be treated with NaCl in a stirred tank, then be mixed in the process water (pH is set to 4) in a tank or basin and then be filtrated. The time to reach equilibrium and the influence of temperature should also be investigated.

No description available.