Advanced Reaction Systems for Hydrogen Production

[EN] This PhD work started in March 2010 with the support of the University of the Basque Country (UPV/EHU) under the program named “Formación de Personal Investigador” at the Chemical and Environmental Engineering Department in the Faculty of Engineering of Bilbao. The major part of the Thesis work was carried out in the mentioned department, as a member of the Sustainable Process Engineering (SuPrEn) research group. In addition, this PhD Thesis includes the research work developed during a period of 6 months at the Institut für Mikrotechnik Mainz GmbH, IMM, in Germany. During the four years of the Thesis, conventional and microreactor systems were tested for several feedstocks renewable and non-renewable, gases and liquids through several reforming processes in order to produce hydrogen. For this purpose, new catalytic formulations which showed high activity, selectivity and stability were design. As a consequence, the PhD work performed allowed the publication of seven scientific articles in peer-reviewed journals. This PhD Thesis is divided into the following six chapters described below. The opportunity of this work is established on the basis of the transition period needed for moving from a petroleum based energy system to a renewable based new one. Consequently, the present global energy scenario was detailed in Chapter 1, and the role of hydrogen as a real alternative in the future energy system was justified based on several outlooks. Therefore, renewable and non-renewable hydrogen production routes were presented, explaining the corresponding benefits and drawbacks. Then, the raw materials used in this Thesis work were described and the most important issues regarding the processes and the characteristics of the catalytic formulations were explained. The introduction chapter finishes by introducing the concepts of decentralized production and process intensification with the use of microreactors. In addition, a small description of these innovative reaction systems and the benefits that entailed their use were also mentioned. In Chapter 2 the main objectives of this Thesis work are summarized. The development of advanced reaction systems for hydrogen rich mixtures production is the main objective. In addition, the use and comparison between two different reaction systems, (fixed bed reactor (FBR) and microreactor), the processing of renewable raw materials, the development of new, active, selective and stable catalytic formulations, and the optimization of the operating conditions were also established as additional partial objectives. Methane and natural gas (NG) steam reforming experimental results obtained when operated with microreactor and FBR systems are presented in Chapter 3. For these experiments nickel-based (Ni/Al2O3 and Ni/MgO) and noble metal-based (Pd/Al2O3 and Pt/Al2O3) catalysts were prepared by wet impregnation and their catalytic activity was measured at several temperatures, from 973 to 1073 K, different S/C ratios, from 1.0 to 2.0, and atmospheric pressure. The Weight Hourly Space Velocity (WHSV) was maintained constant in order to compare the catalytic activity in both reaction systems. The results obtained showed a better performance of the catalysts operating in microreactors. The Ni/MgO catalyst reached the highest hydrogen production yield at 1073 K and steam-to-carbon ratio (S/C) of 1.5 under Steam methane Reforming (SMR) conditions. In addition, this catalyst also showed good activity and stability under NG reforming at S/C=1.0 and 2.0. The Ni/Al2O3 catalyst also showed high activity and good stability and it was the catalyst reaching the highest methane conversion (72.9 %) and H2out/CH4in ratio (2.4) under SMR conditions at 1073 K and S/C=1.0. However, this catalyst suffered from deactivation when it was tested under NG reforming conditions. Regarding the activity measurements carried out with the noble metal-based catalysts in the microreactor systems, they suffered a very quick deactivation, probably because of the effects attributed to carbon deposition, which was detected by Scanning Electron Microscope (SEM). When the FBR was used no catalytic activity was measured with the catalysts under investigation, probably because they were operated at the same WHSV than the microreactors and these WHSVs were too high for FBR system. In Chapter 4 biogas reforming processes were studied. This chapter starts with an introduction explaining the properties of the biogas and the main production routes. Then, the experimental procedure carried out is detailed giving concrete information about the experimental set-up, defining the parameters measured, specifying the characteristics of the reactors used and describing the characterization techniques utilized. Each following section describes the results obtained from activity testing with the different catalysts prepared, which is subsequently summarized: Section 4.3: Biogas reforming processes using γ-Al2O3 based catalysts The activity results obtained by several Ni-based catalysts and a bimetallic Rh-Ni catalyst supported on magnesia or alumina modified with oxides like CeO2 and ZrO2 are presented in this section. In addition, an alumina-based commercial catalyst was tested in order to compare the activity results measured. Four different biogas reforming processes were studied using a FBR: dry reforming (DR), biogas steam reforming (BSR), biogas oxidative reforming (BOR) and tri-reforming (TR). For the BSR process different steam to carbon ratios (S/C) from 1.0 to 3.0, were tested. In the case of BOR process the oxygen-to-methane (O2/CH4) ratio was varied from 0.125 to 0.50. Finally, for TR processes different S/C ratios from 1.0 to 3.0, and O2/CH4 ratios of 0.25 and 0.50 were studied. Then, the catalysts which achieved high activity and stability were impregnated in a microreactor to explore the viability of process intensification. The operation with microreactors was carried out under the best experimental conditions measured in the FBR. In addition, the physicochemical characterization of the fresh and spent catalysts was carried out by Inductively Coupled Plasma Atomic Emission Spectroscopy (ICP-AES), N2 physisorption, H2 chemisorption, Temperature Programmed Reduction (TPR), SEM, X-ray Photoelectron Spectroscopy (XPS) and X-ray powder Diffraction (XRD). Operating with the FBR, conversions close to the ones predicted by thermodynamic calculations were obtained by most of the catalysts tested. The Rh-Ni/Ce-Al2O3 catalyst obtained the highest hydrogen production yield in DR. In BSR process, the Ni/Ce-Al2O3 catalyst achieved the best activity results operating at S/C=1.0. In the case of BOR process, the Ni/Ce-Zr-Al2O3 catalyst showed the highest reactants conversion values operating at O2/CH4=0.25. Finally, in the TR process the Rh-Ni/Ce-Al2O3 catalyst obtained the best results operating at S/C=1.0 and O2/CH4=0.25. Therefore, these three catalysts were selected to be coated onto microchannels in order to test its performance under BOR and TR processes conditions. Although the operation using microreactors was carried out under considerably higher WHSV, similar conversions and yields as the ones measured in FBR were measured. Furthermore, attending to other measurements like Turnover Frequency (TOF) and Hydrogen Productivity (PROD), the values calculated for the catalysts tested in microreactors were one order of magnitude higher. Thus, due to the low dispersion degree measured by H2-chemisorption, the Ni/Ce-Al2O3 catalyst reached the highest TOF and PROD values. Section 4.4: Biogas reforming processes using Zeolites L based catalysts In this section three type of L zeolites, with different morphology and size, were synthesized and used as catalyst support. Then, for each type of L zeolite three nickel monometallic and their homologous Rh-Ni bimetallic catalysts were prepared by the wetness impregnation method. These catalysts were tested using the FBR under DR process and different conditions of BSR (S/C ratio of 1.0 and 2.0), BOR (O2/CH4 ratio of 0.25 and 0.50) and TR processes (at S/C=1.0 and O2/CH4=0.25). The characterization of these catalysts was also carried out by using the same techniques mentioned in the previous section. Very high methane and carbon dioxide conversion values were measured for almost all the catalysts under investigation. The experimental results evidenced the better catalytic behavior of the bimetallic catalysts as compared to the monometallic ones. Comparing the catalysts behavior with regards to their morphology, for the BSR process the Disc catalysts were the most active ones at the lowest S/C ratio tested. On the contrary, the Cylindrical (30–60 nm) catalysts were more active under BOR conditions at O2/CH4=0.25 and TR processes. By the contrary, the Cylindrical (1–3 µm) catalysts showed the worst activity results for both processes. Section 4.5: Biogas reforming processes using Na+ and Cs+ doped Zeolites LTL based catalysts A method for the synthesis of Linde Type L (LTL) zeolite under microwave-assisted hydrothermal conditions and its behavior as a support for heterogeneously catalyzed hydrogen production is described in this section. Then, rhodium and nickel-based bimetallic catalysts were prepared in order to be tested by DR process and BOR process at O2/CH4=0.25. Moreover, the characterization of the catalysts under investigation was also carried out. Higher activities were achieved by the catalysts prepared from the non-doped zeolites, Rh-Ni/D and Rh-Ni/N, as compared to the ones supported on Na+ and Cs+ exchanged supports. However, the differences between them were not very significant. In addition, the Na+ and Cs+ incorporation affected mainly to the Disc catalysts. Comparing the results obtained by these catalysts with the ones studied in the section 4.4, in general worst results were achieved under DR conditions and almost the same results when operated under BOR conditions. In Chapter 5 the ethylene glycol (EG) as feed for syngas production by steam reforming (SR) and oxidative steam reforming (OSR) was studied by using microchannel reactors. The product composition was determined at a S/C of 4.0, reaction temperatures between 625°C and 725°C, atmospheric pressure and Volume Hourly Space Velocities (VHSV) between 100 and 300 NL/(gcath). This work was divided in two sections. The first one corresponds to the introduction of the main and most promising EG production routes. Then, the new experimental procedure is detailed and the information about the experimental set-up and the measured parameters is described. The characterization was carried out using the same techniques as for the previous chapter. Then, the next sections correspond to the catalytic activity and catalysts characterization results. Section 5.3: xRh-cm and xRh-np catalysts for ethylene glycol reforming Initially, catalysts with different rhodium loading, from 1.0 to 5.0 wt. %, and supported on α-Al2O3 were prepared by two different preparation methods (conventional impregnation and separate nanoparticle synthesis). Then, the catalysts were compared regarding their measured activity and selectivity, as well as the characterization results obtained before and after the activity tests carried out. The samples prepared by a conventional impregnation method showed generally higher activity compared to catalysts prepared from Rh nanoparticles. By-product formation of species such as acetaldehyde, ethane and ethylene was detected, regardless if oxygen was added to the feed or not. Among the catalysts tested, the 2.5Rh-cm catalyst was considered the best one. Section 5.4: 2.5Rh-cm catalyst support modification with CeO2 and La2O3 In this part of the Chapter 5, the catalyst showing the best performance in the previous section, the 2.5Rh-Al2O3 catalyst, was selected in order to be improved. Therefore, new Rh based catalysts were designed using α-Al2O3 and being modified this support with different contents of CeO2 or La2O3 oxides. All the catalysts containing additives showed complete conversion and selectivities close to the equilibrium in both SR and OSR processes. In addition, for these catalysts the concentrations measured for the C2H4, CH4, CH3CHO and C2H6 by-products were very low. Finally, the 2.5Rh-20Ce catalyst was selected according to its catalytic activity and characterization results in order to run a stability test, which lasted more than 115 hours under stable operation. The last chapter, Chapter 6, summarizes the main conclusions achieved throughout this Thesis work. Although very high reactant conversions and rich hydrogen mixtures were obtained using a fixed bed reaction system, the use of microreactors improves the key issues, heat and mass transfer limitations, through which the reforming reactions are intensified. Therefore, they seem to be a very interesting and promising alternative for process intensification and decentralized production for remote application.

Origin of Chinese ancient glasses;study on the earliest Chinese ancient glasses

The earliest Chinese ancient glasses before the West Han Dynasty (200 BC) from different regions are studied. The glass samples were unearthed from Hunan, Hubei, Yunnan, Sichuan, Guizhou, Guangdong and Xinjiang of China. The chemical composition of these glasses samples is analyzed by proton induced X-ray emission (PIXE) technique, energy dispersive X-ray fluorescence (EDXRF) method and inductively coupled plasma atomic emission spectrometry (ICP-AES). It is shown that the glass chemical compositions belong to barium-lead silicate BaO-PbO-SiO2, potash soda lime silicate K2O (Na2O)-CaO-SiO2 (K2O/Na2O > 1), soda potash lime silicate Na2O (K2O)-CaO-SiO2 (K2O/Na2O < 1) and potash silicate K2O-SiO2 glass systems, respectively. The origins of the earliest Chinese ancient glasses are discussed from the archaeological and historical points of view. These four types of Chinese ancient glasses were all made in Chinese territory using local raw materials. The glass preparation technology was related to the Chinese ancient bronze metallurgy and proto-porcelain glaze technology. The glass technology relationship between the East and the West is analyzed at the same time.

Perfume, história e design: o papel das embalagens no mercado brasileiro de perfumaria

O presente trabalho tem por objetivo apresentar o papel do design no mercado brasileiro de perfumes. Parte-se da hipótese de que é ele o elemento fundamental para o bom desempenho desse segmento. Na medida em que ele possibilita a diferenciação entre as diversas embalagens, criando uma segmentação para o consumo nas mais diversas camadas sociais. Inicialmente será apresentado o universo do perfume, abordando seus aspectos técnicos e culturais. Uma relação de matérias primas utilizadas na indústria de perfumaria será fornecida. Seu propósito é proporcionar ao designer profissional e ao designer pesquisador uma referência visual dos elementos que compõe um perfume. Adiante, os principais aspectos da história do perfume no mercado nacional de perfumaria são destacados, bem como a mudança de paradigmas de consumo ao longo dessa trajetória. Segue-se com a apresentação das peculiaridades de um projeto de embalagens para esse segmento, destacando o perfil do designer, desse mercado e uma relação de termos técnicos. Por fim, um modelo para catalogação será apresentado e aplicado a um grupo de perfumes nacionais e internacionais. O estudo se encerra com uma análise das embalagens catalogadas, a fim de mostrar que existem diferentes soluções de design para comunicar os conceitos de um perfume.

微晶玻璃在大功率脉冲氙灯封接中的应用

：为提高大功率脉冲氙灯的封接强度，将微晶玻璃作为封接材料引入到氙灯封接应用中. 以 Bi2O3,ZnO,Al2O3,MgO,CaCO3,SiO2,BaO,H3BO3,P2O5,Na2O 为原料，通过高温熔融制备了大功率脉冲氙灯封接 用微晶玻璃样品. 测试了样品的热膨胀系数,并通过差热分析(Differential Thermal Analysis，DTA)对脉冲氙灯 微晶玻璃的封接温度进行了讨论，用X 射线衍射(X-ray diffraction ，XRD)表征了封接玻璃，并进行了分析. 将 制得的样品磨成玻璃粉末，制成膏剂状玻璃焊料，对大功率脉冲氙灯进行封接，得到大功率脉冲氙灯的微晶 玻璃封接件. 通过氦质谱检漏仪检测，1#、2#、4#封接件气密性良好，达到10-6 Pa.

Yb：FAP晶体生长

采用中频感应提拉法生长了Yb：FAP晶体。对晶体生长中影响晶体质量的因素特别是原料的处理、CaF2的挥发等进行了研究和讨论。运用ICP-AES测定Yb^3＋离子在Yb：FAP晶体中的分凝系数。对Yb：FAP晶体进行了高分辨X射线的四圆衍射实验，结果表明晶体具有比较高的晶格完整性。

In situ synthesis of ZrO2/ZrW2O8 composites with near-zero thermal expansion

In this paper, ZrO2 and WO3 were used as the raw materials to prepare ZrO2/ZrW2O8 composites by in situ reaction method and the thermal expansion property of the composites was studied. This novel method included a heating step up to 1473 K for 24 h, which combines the synthesizing and sintering of ZrW2O8. The result indicates that ZrO2/ZrW2O8 composite shows near-zero thermal expansion when the weight ratio of ZrO2 and WO3 is 2.5:1. Compared with composites prepared previously by non-reactive sintering of ZrO2 and ZrW2O8, the composites show higher relative density and lower porosity.

Growth of highly sensitive thermoluminescent crystal alpha-Al2O3 : C by the temperature gradient technique

In this work, an alpha-Al2O3:C crystal with highly sensitive thermoluminescence was directly grown by the temperature gradient technique (TGT) using Al2O3 and graphite powders as raw materials. The optical and luminescent properties and the dosimetric characteristics of the crystal were investigated. An as-grown alpha-Al2O3:C crystal shows a single glow peak at 462 K and a blue emission peak at 415 nm. The thermoluminescence (TL) response of the crystal shows a linear-sublinear-saturation characteristic. In the dose range from 5 x 10(-6) to 10Gy, the alpha-Al2O3:C crystal shows excellent linearity, and saturation was observed at about 30Gy. The sensitivity of the crystal decreases as the heating rate increases. (c) 2008 Elsevier B.V. All rights reserved.

α-Al_2O_3:C晶体的热释光和光释光特性

以高纯α-Al2O3和石墨为原料,采用温梯法生长了α-Al2O3:C晶体,使用RisΦTL/OSL-DA-15型热释光和光释光仪研究了其热释光和光释光特性.α-Al2O3:C晶体在462K附近有单一热释光峰,发射波长位于410nm.随着辐照剂量的增加,热释光强度逐渐增强,462K的热释光特征峰位置保持不变.α-Al2O3:C晶体的光释光衰减曲线由快衰减和慢衰减两个部分组成,随着辐照剂量的增加,快衰减部分衰减速率变化不大,而慢衰减部分衰减速率加快.在5×10-6—10Gy剂量范围内,α-Al2O3:C晶体的热释光剂量响应呈现良好的线性关系,30Gy时达到饱和;光释光剂量响应在5×10-6—60Gy剂量范围内呈现良好的线性关系,100Gy时达到饱和.与热释光相比,光释光剂量响应具有更高的灵敏度和更宽的线性剂量响应范围.

Growth of alpha-Al2O3:C crystal with highly sensitive optically stimulated luminescence

In this work. an alpha-Al2O3:C crystal was directly grown by the temperature gradient technique (TGT) using Al2O3 and graphite powders as the raw materials. The optical, optically stimulated luminescence (OSL) properties and dosimetric characteristics of as-grown crystal were investigated. As-grown alpha-Al2O3:C crystal shows strong absorption band at 205, 230 and 256 nm. Three-dimensional thermoluminescence (TL) emission spectrum of the crystal shows a single emission peak at similar to 415 nm. The OSL decay curve can be fitted to two exponentials, the faster component and the slower component. The OSL response of the crystal shows a linear-sublinear-saturation characteristic. As-grown alpha-Al2O3:C crystal shows excellent linearity in the dose range from 5 x 10(-6) to 50 Gy. For doses higher than the saturation dose (100 Gy). the OSL sensitivity decreases as the dose increases. Crown Copyright (C) 2008 Published by Elsevier B.V. All rights reserved.

Metodología analítica para el control de calidad en ambientadores higiénicos basados en la cuantificación de sus componentes mediante cromatografía de gases acoplada a espectrometría de masas (GC/MS).

Nota técnica para el análisis de compuestos volátiles en fórmulas higiénicas

Validação de métodos analíticos - estudos de casos relevantes de atividades dos laboratórios de controle de qualidade de vacinas

A validação dos métodos de análises em situações fora da rotina, em P&D pesquisa e desenvolvimento, pode tornar-se um processo de difícil solução, em oposição àquelas de rotina, onde as concentrações são conhecidas. Nesta última situação, o método analítico é validado e aprovado com simplicidade. Apesar dos elementos de qualidade básicos para análises em P&D serem os mesmos adotados nas análises de rotina, fatores como o comportamento imprevisível da amostra, a composição desconhecida da matriz e interdependência com o analito, mesmo a incerteza a respeito da escolha do método instrumental, requer uma atenção renovada nos elementos de qualidade existentes. A razão pode ser atribuída à imprevisibilidade do procedimento analítico e a extensão do esforço adicional dos elementos de qualidade. As incertezas das análises em P&D requerem uma cuidadosa consideração do problema, assim como a disponibilidade de técnicas analíticas. Ao mesmo tempo, devem-se observar o planejamento e organização do trabalho, a supervisão do desenvolvimento analítico e a adequação dos aspectos técnico e organizacional - no trabalho de P&D, a definição de responsabilidades e a competência do corpo técnico. A garantia da qualidade nas indústrias farmacêuticas é estabelecida pelo desenvolvimento de especificações apropriadas para matérias-primas, produtos intermediários e produtos finais. A importância de especificações adequadas foi estabelecida e exemplos foram dados no desenvolvimento de especificação típica para produtos farmacêuticos, tais como a vacina e matéria prima. Isto incluiu uma discussão dos tipos de parâmetros que precisam ser controlados e uma indicação dos valores numéricos ou faixas esperadas para muitos materiais utilizados. A metrologia analítica que necessita ser aplicada para demonstrar a observância com as especificações foi discutida, com as implicações de desempenho do método para diferenciar variações na qualidade do produto e a simples variabilidade analítica. Esse trabalho foi escrito para laboratórios, com a finalidade de dar um suporte na implementação da validação de métodos analíticos e introduzir o conceito de incerteza da medida nas análises de rotina. O objetivo foi fornecer de uma maneira compreensível e prática a metodologia dos cálculos das medidas de incerteza baseados principalmente em dados de controle de qualidade e de validação já existentes. Exemplos práticos retirados diretamente do Laboratório de Metrologia e Validação, FIOCRUZ / Bio-Manguinhos, foram apresentados. Entretanto, o tratamento usado neste trabalho é genérico e pode ser aplicável a outros laboratórios químicos

Estudo sobre Produção mais Limpa (P+L) aplicado a um serviço de referência de uma Instituição de Ensino e Pesquisa - Rio de Janeiro (RJ).

O objetivo deste trabalho foi avaliar a potencialidade de implantação da Produção Mais Limpa (P+L), através do estudo de caso em Laboratório Biomédico de Referência em uma instituição pública de ensino e pesquisa localizada no Rio de Janeiro. Esta investigação é exploratória e analítica, utilizando-se como instrumentos a revisão bibliográfica e documental, a observação direta e a entrevista com aplicação de questionários voltados aos responsáveis pela área ambiental do laboratório pesquisado. A análise foi realizada confrontando-se os dados levantados com as recomendações da metodologia de P+L, identificando-se as lacunas e oportunidades para a melhoria dos serviços e processos de trabalho. O laboratório possui instalações modernas, organização, sistemas de avaliação da matéria-prima e insumos usados, além do gerenciamento dos resíduos. Contudo, nem todos os procedimentos são validados ou estão adequados às normas. Em geral, problemas em laboratórios dizem respeito ao uso excessivo de substâncias perigosas e ao manejo inadequado de resíduos, o qual pode ser contornado com a P+L, tendo como enfoque a prevenção da poluição e a minimização na fonte geradora. A redução do consumo de materiais e insumos, além da implantação de mudanças nos processos de trabalho, podem diminuir os custos financeiros e os impactos ambientais, como foi demonstrado no estudo. Para a melhoria da gestão dos laboratórios, recomenda-se a continuidade na aquisição, manutenção de equipamentos e infraestrutura. É importante a divulgação de informações ambientais e treinamento permanente para funcionários e alunos. A Sustentabilidade Ambiental só pode ser alcançada quando for bem entendida e absorvida por todos, sendo a alta administração das instituições a maior responsável para liderar esse processo. Para estudos futuros, propõe-se melhor definição e ampliação dos indicadores para o monitoramento e aprimoramento da gestão ambiental. Complementarmente, indicam-se estudos sobre a aquisição de conceitos pelos atores sobre a P+L e como eles podem contribuir com a Sustentabilidade Ambiental e a melhoria no ambiente de trabalho. Espera-se que esta pesquisa auxilie com o aperfeiçoamento da gestão no laboratório estudado e em instituições similares que a venham implantar a P+L.

Trade and Management: Exclusive Economic Zones and the Changing Japanese Surimi Market

The United States' increasing competitive advantage in international seafood trade in Alaska walleye pollock. Theragra chalcogramma, has contributed to higher prices for surimi-based goods and structural changes in seafood production and trade in Japan. The objectives of this analytical investigation include: 1) Evaluation of the role reversal of Japan and the United States in international seafood trade and 2) quantification of the impact of rising prices of frozen surimi on household consumption of surimi-based foods in Japan. This study documents Japan's regression from "seafood self-sufficiency" to increasing dependence on imported products and raw materials. In particular, Japan's growing dependence on American fishermen and seafood producers is described. Surimi production by the United States, and its emerging dominance over Japanese sources of supply, are especially significant. Results of the analysis suggest that Japanese consumer demand for surimi-based food stuffs correlates directly with "competitive" food prices, e.g., pork, chicken, and beef, and inversely with personal income. Also revealed is how rising household income and relative price shifts among competing animal protein sources in the Japanese diet have contributed to declining household consumption of surimi-based foods, specifically, and a shift away from seafoods in favor of beef, in general. The linkages between, for example. Japanese domestic seafood production and consumption, international trade in marine products, and resource management decisions in the U.S. EEZ present a picture of a changing global marketplace. Increasingly, actions in one arena will have perhaps profound implications in the others.

Síntese de ésteres derivados do ácido oléico empregando lipases produzidas por Yarrowia lipolytica

Biodiesel é um biocombustível que consiste na mistura de ésteres monoalquílicos de ácidos graxos de cadeia longa. O processo usual de produção deste combustível é a transesterificação de óleos vegetais com álcoois de cadeia curta. Nesse processo, a matéria prima deve conter baixo conteúdo de ácido graxos livres ( ≤ 1%) e água (≤ 0,5%). Como alternativa ao processo de transesterificação, destaca-se o emprego de matérias-primas de baixo custo, com elevado teor de ácidos graxos livres, para a síntese de ésteres alquílicos através de reações de esterificação. As reações de produção do biodiesel podem ser catalisadas por via química (ácida e básica) ou enzimática. Na catálise enzimática, os biocatalisadores empregados são as lipases, que catalisam a hidrólise e síntese de ésteres e podem ser obtidas a partir de microrganismos, plantas ou tecido animal, sendo as de origem microbiana as mais utilizadas. O objetivo principal deste trabalho foi avaliar o potencial da lipase de Yarrowia lipolytica, uma levedura não convencional, na síntese de ésteres do ácido oleico visando à obtenção de ésteres alquílicos (biodiesel). Foram estudados os efeitos da temperatura (25, 30, 35, 40, 50 e 60oC), do teor enzimático (5, 10, 20, 30 e 40% v/v) e do tipo de álcool (metanol, etanol, n-propanol e n-butanol ) nas reações de esterificação do ácido oleico empregando o extrato enzimático líquido produzido por Yarrowia lipolytica. Os resultados obtidos mostraram que as reações conduzidas a 30oC e com 10% v/v do extrato enzimático apresentaram maior taxa inicial de reação. Também foi avaliada a utilização do extrato enzimático liofilizado (5% m/v) e do PES (produto enzimático sólido) (5% m/v) de Yarrowia lipolytica na reação de esterificação do ácido oleico com n-butanol a 30oC. O maior consumo de ácido oleico ocorreu na reação conduzida com o PES. O efeito da temperatura (25, 30, 35, 40 e 50oC) na síntese de oleato de butila foi, então, investigado nas reações empregando PES como biocatalisador e a maior conversão de ácido oleico foi verificada na temperatura de 40oC

Produção in vitro, análise fitoquímica e avaliação da atividade antineoplásica de metabólitos de Hovenia dulcis Thunb. (Rhamnaceae) obtidos por diferentes estratégias biotecnológicas

Hovenia dulcis Thunberg, natural da Ásia Oriental, é cultivada no Brasil onde é conhecida como uva-do-japão. A espécie possui várias indicações na medicina popular e alguns estudos apontam o seu potencial antineoplásico, tripanocida e hepatoprotetor. Metabólitos secundários são substâncias não essenciais para a sobrevivência celular, mas que fornecem vantagens adaptativas aos vegetais, sendo atribuído, para algumas delas, atividades biológicas importantes. Substâncias de interesse medicinal têm sido obtidas por técnicas da cultura de tecidos vegetais, como a calogênese e a cultura de células em suspensão, que permitem a síntese de matéria-prima de forma contínua e homogênea, independentemente de fatores ambientais e sazonais. O presente estudo objetivou o estabelecimento de culturas in vitro de H. dulcis, visando à produção de metabólitos de interesse, com vistas à avaliação do seu potencial antineoplásico sobre células K562. Foram testados protocolos para o estabelecimento de diferentes sistemas, como culturas de calos, de células em suspensão (CCS) e compact callus clusters (CCC) e ainda a avaliação do uso de elicitores na otimização de metabólitos produzidos in vitro. Foi verificado que a adição dos fitorreguladores KIN e TDZ, substituindo o BAP, não foi capaz de induzir a formação de calos friáveis, bem como a manutenção das culturas em ausência de luz. O uso do nitrato de prata promoveu a friabilidade de calos em todas as concentrações testadas, considerando-se 2,0 mg.L-1 a melhor concentração. Foram alcançadas taxas de 100% de formação de CCS tanto na presença, quanto em ausência de AgNO3. O maior acúmulo de biomassa foi verificado na concentração mais baixa de PIC (0,625 mg.L-1). A análise dos espectros de RMN indicou a presença de (+)-dihidromiricetina, (+)-galocatequina, hovenitina II, hovenosideo G, hodulosideo III, hodulosideo IV, hodulosideo I e hovenidulciosideo B1 nas culturas de calos friáveis. No estabelecimento de culturas CCC, observou-se a formação de calos compactos verdes em todas as concentrações de ANA testadas. O aumento da velocidade de rotação para 135 rpm aumentou a dispersão das células com consequente formação dos agregados celulares desejados. A seleção de linhagens celulares demonstrou ser um método eficiente na uniformização do tamanho desses agregados e tal uniformidade se manteve estável por mais de cinco subcultivos em 100% das culturas. Uma fração rica em saponinas foi obtida a partir dos agregados celulares, correspondendo a 1,46% da massa seca. A análise por RMN sugeriu a presença das saponinas Hovenosideo G e dos hovenidulciosideos A2 e B2. O uso de elicitores em cultura de calos mostrou-se adequado à produção de metabólitos secundários, sem alterações morfológicas nos mesmos. A elicitação alterou o perfil cromatográfico analisado por HPLC. Na elicitação com 5,0 mg.L-1 de extrato de levedura foi verificado um aumento de quase três vezes (12,280 3,396 equivalentes de quercetina/mg de extrato) na síntese de flavonoides. Finalmente, os estudos de ação antitumoral in vitro demonstraram citotoxicidade dos extratos de calos não elicitados de H. dulcis sobre linhagem de leucemia mieloide crônica (IC50 de 74,05 μg.mL-1.) e inibição do crescimento de tais células (K562), sugerindo o potencial antineoplásico para um produto biotecnológio (calo) desta espécie.