Yes / Naphtha isomerization is an important issue in petroleum industries and it has to be a simple and cost effective technology for producing clean fuel with high gasoline octane number. In this work, based on real industrial data, a detailed process model is developed for an existing naphtha isomerization reactor of Baiji North Refinery (BNR) of Iraq which involves estimation of the kinetic parameters of the reactor. The optimal values of the kinetic parameters are estimated via minimizing the sum of squared errors between the predicted and the experimental data of BNR. Finally, a new isomerization process (named as AJAM process) is proposed and using the reactor model developed earlier, the reactor condition is optimized which maximizes the yield and research octane number (RON) of the reactor.

No description available.

Yes / Due to the environmental legislations related to sulfur content and proceeding with the challenges to find an appropriate catalyst of such contamination producing clean fuel, a main thrust for improving of more efficient technologies on new oxidative catalyst is viewed a vital issue in fuel quality development. So, in this study, the sulfur compound (ethyl mercaptan) presents in light naphtha feedstock is removed by oxidative desulfurization (ODS) in a batch reactor using a new homemade nano-catalyst and air as oxidant under different reaction conditions (reaction temperatures, reaction time and the initial sulfur concentrations) that has not been studied in such field. The catalyst is zinc oxide supported on zeolite nanoparticles which is locally prepared by Incipient Wetness Impregnation (IWI) method. Mathematical model of the relevant reactions is also developed in this study to match the experimental results via obtaining the optimal kinetic parameters utilizing optimization techniques within gPROMS program. Such optimization is conducted using two approaches (linear and nonlinear regression) and the results showed that the nonlinear approach is more accurate than linear approach. The optimal kinetic parameters are then used to achieve a clean fuel via getting the optimal operation conditions based on the maximum conversion. Where, higher than 99% of the process conversion has obtained at temperature of 327.4 K, reaction time at163.6 min and initial concentration of 335.3 ppm.

The main goal of this work has been that of optimizing the operating conditions of a biofilter, intended for the control of methane, an important greenhouse gas widely emitted by older or smaller landfill installations.The specific objectives were: (1) to select a suitable packing material (of organic or inorganic type); (2) to optimize the concentrations of input nutrients, mainly consisting of nitrogen, phosphorus, potassium and copper, which are intended to be introduced via the nutrient solution; (3) to determine the optimized values of the most important design parameters, such as the methane inlet load (which depends on the air flow rate and the inlet methane concentration); and (4) to model the biofilter performance. Firstly, the comparison of the two packing materials, one of organic type, and the other of inorganic type, has revealed that the latter was the more appropriate material for the methane biofiltration. Then, through the use of the selected packing material, the influence of each individual nutrient on the efficiency of the process has been investigated.The results obtained have shown that both nitrogen and phosphorus concentrations have to be controlled, while potassium and copper were revealed as being nutrients of only minor importance. Secondly, the optimization of the inlet gas flow rate and of the inlet methane concentration (and consequently, of the methane inlet load also), has been performed. According to the results of the studies, these parameters require good control during methane biofiltration because a limitation in biofilter performance could otherwise be induced. In addition, it was noted that the increase in the inlet gas flow rate led generally to a greater decrease of the methane conversion than the one induced by the inlet methane concentration. Finally, a new method, based on the use of solid extracts sampled from the methane biofilter, has been applied to the determination of methane biofilter kinetic parameters. Following this study, a steady state model of the methane biofiltration, taking into consideration the important operational parameters, as identified previously, has been developed. One particular feature of this model is that it takes into consideration the influence of the biofilter average temperature.The prediction results, obtained with the use of the model, have been successfully compared with the experimental results.

Os ésteres são importantes compostos orgânicos, obtidos por síntese química ou extraídos de alguns produtos naturais utilizando-se solvente em meio adequado. Estudos mostram que enzimas, em particular lipases, podem ser aplicadas na síntese de diversos ésteres. O principal objetivo deste trabalho foi a obtenção de acetato de butila, um éster de aroma característico de abacaxi, utilizando lipase de Geotrichum candidum produzida em fermentação submersa e imobilizada em matriz polimérica de alginato de bário e gelatina reticulada com glutaraldeído. A caracterização bioquímica foi realizada tanto para a lipase na forma livre como para a lipase na forma imobilizada. O rendimento em conversão molar de substrato foi determinado por cromatografia gasosa. A enzima apresentou atividade enzimática máxima após 48 horas de fermentação de 37,7 U/mL. Os valores ótimos para pH e temperatura da enzima na forma livre e imobilizada foram pH 6,5 e 40 °C e pH 7,5 e 45 °C, respectivamente. A enzima na forma livre foi estável do pH 6,0 ao 8,0 e à temperatura de 35 a 45 °C, já na forma imobilizada, foi estável do pH 5,5 ao 8,5 e na faixa de temperatura de 30 a 55 °C. A lipase imobilizada teve seus parâmetros cinéticos determinados, e os valores obtidos para o Km e Vmax, foram 0,115 mmol e 0,718 µmol.mL-1.min-1, respectivamente. As melhores condições de síntese do bioaroma para a enzima na forma livre foram: temperatura de 30 °C, 12,5% de enzima em relação à quantidade de butanol utilizada, proporção molar do substrato 60% de acetato de vinila em um período de 24 horas. O rendimento alcançado neste caso foi de 97,2 % de conversão molar em acetato de butila. Para a enzima imobilizada as melhores condições foram: temperatura de 45 °C, 12,5% de enzima em relação à quantidade de butanol utilizada, proporção molar do substrato 60% de acetato de vinila em um período de 24 horas. O rendimento alcançado neste caso foi de 99,1%, que demonstra que lipase produzida por Geotrichum candidum na forma imobilizada apresenta excelente capacidade de sintetizar acetato de butila (bioaroma de abacaxi). / Esters are important organic compounds obtained by chemical synthesis or derived from some natural products using a solvent in appropriate medium. Studies have shown that enzymes, particularly lipases, ca be applied in the synthesis of various esters. The main objective of this study was to obtain butyl acetate, a characteristic ester aroma of pineapple, using lipase from Geotrichum candidum produced in submerged fermentation and immobilized in a barium alginate and gelatin polymer matrix crosslinked with glutaraldehyde. The biochemical characterization was performed for both free and immobilized lipases. The yield in molar conversion of substrate was determined by gas chromatography. The enzyme showed maximum enzymatic activity after 48 hours of fermentation of 37.7 U/mL. The optimum values for pH and temperature of the enzyme in free and immobilize form were pH 6.5 and 40 °C and pH 7.5 and 45 °C, respectively. The enzyme was stable in free form from pH 6.0 to 8.0 and at temperatures from 35 to 45 °C, and in the immobilized form from pH 5.5 to 8.5 and at temperatures from 30 to 55 °C. Kinetic parameters of the immobilized lipase were determined, and the values obtained for Km and Vmax were 0.115 mmol and 0.718 µmol.mL-1.min-1, respectively. The best conditions for the synthesis of flavor by enzyme in free form were: 30 °C of temperature, 12.5% of enzyme for the amount of butanol used, and molar ratio of substrate 60% of vinyl acetate in a 24 hours period. The yield achieved in this case was 97.2% of molar conversion in butyl acetate. For the immobilized enzyme the best conditions were: 45 °C of temperature, 12.5% of enzyme for the amount of butanol used, and molar ratio of substrate 60% of vinyl acetate in a 24 hours period. The yield achieved in this case was 99.1%, demonstrating that lipase produced by Geotrichum candidum in immobilized form has an excellent ability to synthesize butyl acetate (pineapple flavor).

Este trabalho apresenta uma análise comparativa da atividade biológica das células imobilizadas em um reator anaeróbio, tratando esgoto sanitário. Os materiais utilizados como suporte para o desenvolvimento do biofilme foram: um polimérico poroso (espuma de poliuretano), um polímero menos poroso (PVC), uma cerâmica porosa (cerâmica especial, desenvolvida pelo DEMA-UFSCar) e uma cerâmica menos porosa (tijolo refratário). A concepção do reator anaeróbio possibilitou o desenvolvimento do biofilme de forma igual, assim como a retirada desse suporte mantendo íntegra a biomassa aderida. Alguns suportes e o lodo retirados do reator anaeróbio foram colocados em reatores diferenciais para determinação dos parâmetros cinéticos. Esses parâmetros foram utilizados para avaliar a atividade biológica, tanto do biofilme aderido aos suportes quanto do lodo. As células imobilizadas nos materiais poliméricos apresentaram maior atividade biológica. Não foi verificada nenhuma diferença significativa na remoção dos constituintes da matéria orgânica (proteínas, carboidratos e lipídeos) entre as células imobilizadas. As análises microscópicas não constataram diferenças na predominância de algum gênero nos suportes ou lodo. O reator foi operado durante 183 dias, com remoção média de DQO de 50,5%, a taxa de carregamento orgânico média foi de 0,193 kg DQO.m3.dia-1. / This work presents a comparative analysis of the biological activity of immobilized biomass in a fixed-bed anaerobic reactor treating domestic sewage. The matrices used for biofilm growth were a porous polymer (polyurethane foam), a polymer with low porosity (PVC), a porous ceramic (special ceramic) and a ceramic with low porosity (refractory brick). The conception of the fixed-bed anaerobic reactor warranty the structure and integrity of the biofilm when samples of support material must be taken. Moreover, the conditions for biofilm growth were similar for all the materials used. After start-up period, some supports were taken from the fixed-bed reactor and transferred to differential reactors, where kinetic studies were carried out. Kinetic parameters were estimated for the different supports and for granulated sludge and used to evaluate the biological activity in a comparative way. The cells adhered to the polymeric supports presented higher activities and the highest activity was obtained when polyurethane foam was used. No differences were verified for organic matter consumption (as proteins, carbohydrates and lipids) when different matrices were used for cell immobilization. Microscopic analysis indicated that the morphological types in the biofilms were similar in ali support materiais. The fixed-bed reactor was operated for 183 days with mean COD removal efficiency of 50.5%, subjected to a organic loading rate of 0.193 Kg COD.m3.dia-1.

Este trabalho apresenta uma análise comparativa da atividade biológica das células imobilizadas em um reator anaeróbio, tratando esgoto sanitário. Os materiais utilizados como suporte para o desenvolvimento do biofilme foram: um polimérico poroso (espuma de poliuretano), um polímero menos poroso (PVC), uma cerâmica porosa (cerâmica especial, desenvolvida pelo DEMA-UFSCar) e uma cerâmica menos porosa (tijolo refratário). A concepção do reator anaeróbio possibilitou o desenvolvimento do biofilme de forma igual, assim como a retirada desse suporte mantendo íntegra a biomassa aderida. Alguns suportes e o lodo retirados do reator anaeróbio foram colocados em reatores diferenciais para determinação dos parâmetros cinéticos. Esses parâmetros foram utilizados para avaliar a atividade biológica, tanto do biofilme aderido aos suportes quanto do lodo. As células imobilizadas nos materiais poliméricos apresentaram maior atividade biológica. Não foi verificada nenhuma diferença significativa na remoção dos constituintes da matéria orgânica (proteínas, carboidratos e lipídeos) entre as células imobilizadas. As análises microscópicas não constataram diferenças na predominância de algum gênero nos suportes ou lodo. O reator foi operado durante 183 dias, com remoção média de DQO de 50,5%, a taxa de carregamento orgânico média foi de 0,193 kg DQO.m3.dia-1. / This work presents a comparative analysis of the biological activity of immobilized biomass in a fixed-bed anaerobic reactor treating domestic sewage. The matrices used for biofilm growth were a porous polymer (polyurethane foam), a polymer with low porosity (PVC), a porous ceramic (special ceramic) and a ceramic with low porosity (refractory brick). The conception of the fixed-bed anaerobic reactor warranty the structure and integrity of the biofilm when samples of support material must be taken. Moreover, the conditions for biofilm growth were similar for all the materials used. After start-up period, some supports were taken from the fixed-bed reactor and transferred to differential reactors, where kinetic studies were carried out. Kinetic parameters were estimated for the different supports and for granulated sludge and used to evaluate the biological activity in a comparative way. The cells adhered to the polymeric supports presented higher activities and the highest activity was obtained when polyurethane foam was used. No differences were verified for organic matter consumption (as proteins, carbohydrates and lipids) when different matrices were used for cell immobilization. Microscopic analysis indicated that the morphological types in the biofilms were similar in ali support materiais. The fixed-bed reactor was operated for 183 days with mean COD removal efficiency of 50.5%, subjected to a organic loading rate of 0.193 Kg COD.m3.dia-1.

A crescente necessidade de se obter fontes de energia e materiais mais sustentáveis tem aumentado o interesse em processos baseados na conversão de biomassa. Microalgas são particularmente interessantes por não competirem com alimentos e serem facilmente adaptáveis ao meio de crescimento. Além disso, microalgas podem ser processadas termicamente para geração tanto de biocombustíveis quanto de produtos químicos úteis. Estudos de conversão térmica de microalgas tem aparecido apenas em anos recentes, endereçando principalmente temperaturas entre 350 e 500 ºC. Neste estudo, a pirólise em temperaturas entre 500 e 900 ºC foi avaliada pelo interesse em se obter biocombustíveis e produtos químicos úteis. As classes de compostos obtidos a partir da pirólise isotérmica da microalga da espécie Chlorella vulgaris foram investigadas através de um sistema composto por um pirolisador conectado a um CG/MS. Dentre as classes identificadas, houve uma predominância de compostos aromáticos e nitrogenados, principalmente derivados de proteínas. Além disso, a maioria dos compostos identificados na corrente de produtos voláteis está presente em todas as temperaturas de reação estudadas. Os parâmetros cinéticos de energia de ativação aparente, constante de reação e ordem de reação foram determinados através de três modelos cinéticos conhecidos como K-A-S, Osawa e Freeman-Carroll, a partir de dados termogravimétricos. A energia de ativação determinada para Chlorella apresentou valores entre 60 e 206 kJ/mol, enquanto a ordem de reação teve como resultado valores entre segunda e décima ordem, de acordo com o modelo cinético. / The increasing need to obtain more sustainable sources of energy and raw materials has attracted attention to processes based on biomass conversion. Microalgae are particularly interesting because they do not compete with human food and they are easily adaptable to the growth medium. Besides, microalgae can be thermally processed to produce both biofuels and useful chemicals. Studies on thermal conversion of microalgae have appeared only in recent years, addressing mainly reaction temperatures between 350 and 500 °C. In this study, pyrolysis in temperatures ranging from 500 to 900 ºC have been investigated considering the interest in producing biofuels and useful chemical compounds. The classes of products obtained by isothermal pyrolysis of the Chlorella vulgaris microalgae have been investigated using a pyrolyzer directly connected to a GC/MS system. Among the classes identified, there was a predominance of aromatic and nitrogenous compounds, mainly protein derived compounds. In addition, most products identified in the volatile products stream are present in all reaction temperatures investigated. The kinetic parameters of apparent activation energy, reaction constant and order of reaction were determined through three kinetic models known as K-A-S, Osawa and Freeman-Carroll, calculated from thermogravimetric data. The activation energy for Chlorella presented values within the range of 60 and 206 kJ/mole, while the order of reaction resulted in values between second and tenth order, from the different methods.

Calorimetry is one of the main techniques of thermal analysis. Most of physical or chemical modifications of material are associated with thermal effects whereby heat is absorbed (i.e., melting) or released (i.e., thermal decomposition). Typically, calorimetric experiments are performed with Differential Scanning Calorimetry (DSC), which measures the heat flux absorbed or released by the sample following the same temperature program as a reference material. In these experiments, measurements are typically carried out on a few milligrams of sample. However, for many applications one has to handle nanograms or even picograms of sample. One of such applications is relevant to studies of materials which can release a significant amount of energy during their decomposition (energetic materials). Calorimetry able to handle nanograms of sample could find potential applications in the field of explosives detection. Nanocalorimetry allows to heat small amounts of sample (a few nanograms to a few hundred picograms) at extreme heating rates, i.e. up to one million °C/s. The temperature increase can initiate several phenomena in energetic materials, therefore the calorimetry could be an appropriate technique to characterize and to detect energetic materials. The energetic materials used in this study are nitrocellulose (NC), hexogen (RDX), 2,4,6,8,10,12-hexanitro-2,4,6,8,10,12-ltexaazaisowurtzitane (CL-20) and penthrite (PETN). The manuscript presents our results on the nanocalorimeter calibration, on the thermal behaviour of the explosives studied with nanocalorimetry and also includes an evaluation of nanocalorimetry as a tool for explosives detection.

The biodegradation kinetics of Geropon TC-42 (trademark) by an acclimated culture was investigated in anoxic batch reactors to determine biokinetic coefficients to be implemented in two biofilm mathematical models. Geropon TC-42 (trademark) is the surfactant commonly used in space habitation. The two biofilm models differ in that one assumes a constant biofilm density and the other allows biofilm density changes based on space occupancy theory. Extant kinetic analysis of a mixed microbial culture using Geropon TC-42 (trademark) as sole carbon source was used to determine cell yield, specific growth rate, and the half-saturation constant for S0/X0 ratios of 4, 12.5, and 34.5. To estimate cell yield, linear regression analysis was performed on data obtained from three sets of simultaneous batch experiments for three S0/X0 ratios. The regressions showed non-zero intercepts, suggesting that cell multiplication is not possible at low substrate concentrations. Non-linear least-squares analysis of the integrated equation was used to estimate the specific growth rate and the half-saturation constant. Net specific growth rate dependence on substrate concentration indicates a self-inhibitory effect of Geropon TC-42 (trademark). The flow rate and the ratio of the concentrations of surfactant to nitrate were the factors that most affected the simulations. Higher flow rates resulted in a shorter hydraulic retention time, shorter startup periods, and faster approach to a steady-state biofilm. At steady-state, higher flow resulted in lower surfactant removal. Higher influent surfactant/nitrate concentration ratios caused a longer startup period, supported more surfactant utilization, and biofilm growth. Both models correlate to the empirical data. A model assuming constant biofilm density is computationally simpler and easier to implement. Therefore, a suitable anoxic packed bed reactor for the removal of the surfactant Geropon TC-42 (trademark) can be designed by using the estimated kinetic values and a model assuming constant biofilm density.