Estudo da incorporação de diferentes tipos de argilas hidrofílicas em dispersões aquosas de poliuretanos para formação de nanocompósitos

Neste trabalho foram sintetizados nanocompósitos à base de poliuretanos em dispersão aquosa (NWPUs) e argilas hidrofílicas do tipo montimorilonita (MMT) de natureza sódica e cálcica. Os monômeros empregados na síntese foram: poli(glicol propilênico) (PPG); copolímero em bloco à base de poli(glicol etilênico) e poli(glicol propilênico) (EG-b-PG), com teor de 7% de EG; ácido dimetilolpropiônico (DMPA) e diisocianato de isoforona (IPDI). Os NWPUs tiveram as argilas, previamente deslaminadas em água e incorporadas à formulação no momento da dispersão do prepolímero. Dispersões aquosas (WPUs), sem a presença de argila, foram sintetizadas como base, nas quais foram variadas a razão NCO/OH e a proporção de copolímero em relação ao PPG. Nas formulações NWPUs, foram variados também o teor de argila em relação à massa de prepolímero e o tipo de argila sódica e cálcica. As dispersões foram avaliadas, quanto ao teor de sólidos totais, tamanho médio de partícula e viscosidade. Os filmes vazados a partir das dispersões foram caracterizados por espectrometria na região do infravermelho (FTIR), difração de raios-x (XRD) e microscopia eletrônica de varredura (SEM). A resistência térmica dos filmes foi determinada por termogravimetria (TG) e a resistência mecânica dos filmes foi avaliada por ensaios mecânicos em dinamômetro. O grau de absorção de água dos filmes também foi determinado. A formação de nanocompósitos à base de água foi confirmada pela ausência do pico de XRD, característico das argilas empregadas na maioria dos filmes analisados. As micrografias obtidas por SEM confirmam uma dispersão homogênea das argilas na matriz poliuretânica. Os filmes à base de nanocompósitos (NWPUs) apresentaram propriedades superiores às apresentadas por aqueles obtidos a partir das dispersões sem argilas (WPUs). Os revestimentos formados a partir da aplicação das dispersões aderiram à maioria dos substratos testados (metal, vidro, madeira e papel) formando superfícies homogêneas

Determination of electronic energy levels of molecules by 90° low energy electron scattering

A review of the theory of electron scattering indicates that low incident beam energies and large scattering angles are the favorable conditions for the observation of optically forbidden transitions in atoms and molecules.

An apparatus capable of yielding electron impact spectra at 90° with incident electron beam energies between 30 and 50 electron volts is described. The resolution of the instrument is about 1 electron volt.

Impact spectra of thirteen molecules have been obtained. Known forbidden transitions to the helium 2³S, the hydrogen b³Ʃ⁺_u, the nitrogen A³Ʃ⁺_u, B³π_g, a’π_g, and C³π_u, the carbon monoxide a³π, the ethylene ᾶ³B_1u, and the benzene ᾶ³B_1u states from the corresponding ground states have been observed.

In addition, singlet-triplet vertical transitions in acetylene, propyne, propadiene, norbornadiene and quadricyclene, peaking at 5.9, 5.9, 4.5, 3.8, and 4.0 ev (±0.2 ev), respectively, have been observed and assigned for the first time.

Rydberg states of diatomic and polyatomic molecules using model potentials

A simple model potential is used to calculate Rydberg series for the molecules: nitrogen, oxygen, nitric oxide, carbon monoxide, carbon dioxide, nitrogen dioxide, nitrous oxide, acetylene, formaldehyde, formic acid, diazomethane, ketene, ethylene, allene, acetaldehyde, propyne, acrolein, dimethyl ether, 1, 3-butadiene, 2-butene, and benzene. The model potential for a molecule is taken as the sum of atomic potentials, which are calibrated to atomic data and contain no further parameters. Our results agree with experimentally measured values to within 5-10% in all cases. The results of these calculations are applied to many unresolved problems connected with the above molecules. Some of the more notable of these problems are the reassignment of states in carbon monoxide, the first ionization potential of nitrogen dioxide, the interpretation of the V state in ethylene, and the mystery bands in substituted ethylenes, the identification of the R and R’ series in benzene and the determination of the orbital scheme in benzene from electron impact data.

A mathematical and experimental investigation of microcycle spectral estimates of semiconductor flicker noise

The experimental portion of this thesis tries to estimate the density of the power spectrum of very low frequency semiconductor noise, from 10^-6.3 cps to 1. cps with a greater accuracy than that achieved in previous similar attempts: it is concluded that the spectrum is 1/f^α with α approximately 1.3 over most of the frequency range, but appearing to have a value of about 1 in the lowest decade. The noise sources are, among others, the first stage circuits of a grounded input silicon epitaxial operational amplifier. This thesis also investigates a peculiar form of stationarity which seems to distinguish flicker noise from other semiconductor noise.

In order to decrease by an order of magnitude the pernicious effects of temperature drifts, semiconductor "aging", and possible mechanical failures associated with prolonged periods of data taking, 10 independent noise sources were time-multiplexed and their spectral estimates were subsequently averaged. If the sources have similar spectra, it is demonstrated that this reduces the necessary data-taking time by a factor of 10 for a given accuracy.

In view of the measured high temperature sensitivity of the noise sources, it was necessary to combine the passive attenuation of a special-material container with active control. The noise sources were placed in a copper-epoxy container of high heat capacity and medium heat conductivity, and that container was immersed in a temperature controlled circulating ethylene-glycol bath.

Other spectra of interest, estimated from data taken concurrently with the semiconductor noise data were the spectra of the bath's controlled temperature, the semiconductor surface temperature, and the power supply voltage amplitude fluctuations. A brief description of the equipment constructed to obtain the aforementioned data is included.

The analytical portion of this work is concerned with the following questions: what is the best final spectral density estimate given 10 statistically independent ones of varying quality and magnitude? How can the Blackman and Tukey algorithm which is used for spectral estimation in this work be improved upon? How can non-equidistant sampling reduce data processing cost? Should one try to remove common trands shared by supposedly statistically independent noise sources and, if so, what are the mathematical difficulties involved? What is a physically plausible mathematical model that can account for flicker noise and what are the mathematical implications on its statistical properties? Finally, the variance of the spectral estimate obtained through the Blackman/Tukey algorithm is analyzed in greater detail; the variance is shown to diverge for α ≥ 1 in an assumed power spectrum of k/|f|^α, unless the assumed spectrum is "truncated".

Análise técnica do uso de resíduos de poli (tereftalato de etileno) (PET) na indústria têxtil

O aumento no volume de rejeitos industriais e a contínua produção de resíduos de naturezas diversas causam muitas preocupações no âmbito ambiental. Neste contexto, o descarte de embalagens e garrafas de poli(tereftalato de etileno) (PET) tem se tornado um grande problema por conta da pequena atenção que se dá à sua destinação final. Assim sendo, essa pesquisa propõe a análise técnica da utilização de resíduos de PET, oriundos de reciclagem primária, como matéria-prima para a indústria têxtil. Fios de PET reciclado foram comparados aos fios comerciais de poliéster através de diversos ensaios como, por exemplo, resistência à tração e ensaios para solidificação da cor. Ao mesmo tempo, a microscopia eletrônica de varredura (MEV) foi usada para a investigação da morfologia dos fios e melhor interpretação dos resultados. Pôde ser verificado que os fios de PET reciclado apresentam satisfatório desempenho, embora a resistência mecânica e a solidez a cor à luz sejam inferiores àquelas dos fios convencionais de poliéster.

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.

一种新的芴类衍生物的三光子吸收诱导荧光和光限幅效应研究

通过对新合成的芴的一种具有对称性衍生物4-2-（7-（4-氨基苯乙烯基）-9，9-二（2-乙基己基）-9H-芴-2-）乙烯基）苯胺（BASF）的DMF溶液的研究，发现其具有很强三光子吸收频率上转换荧光发射特性，实验测出上转换荧光的波长范围是456-775nm，在510nm处的荧光强度与入射光强的三次方成正比．在0．03mol／L的浓度下就有明显的三光子吸收诱导的光限幅效应．非线性吸收系数和吸收截面分别为y=4．34×10^20 cm^3／W^2和σ3=2．4×10^-39 cm^6／W^2．

Caracterização de filmes formados por dispersões aquosas de poli(uretano-uréia)s para aplicação em membranas para permeação de gases

Entre os polímeros considerados promissores para a remoção seletiva de CO2, destacam-se aqueles que contêm os grupos glicol etilênico (EG). Nesta dissertação, foram obtidos filmes a partir de dispersões aquosas de poliuretano (PU), sintetizadas em trabalho anterior, à base de poli(glicol propilênico) (PPG), copolímero em bloco à base de poli(glicol etilênico) (PEG) e PPG (EG-b-PG), ácido dimetilolpropiônico (DMPA), diisocianato de isoforona (IPDI) e etilenodiamina (EDA). PPG, EG-b-PG e DMPA formaram as regiões flexíveis nas proporções de: PPG 100% e 0% EG-b-PG, PPG 75% e 25% EG-b-PG, PPG 50% e 50% EG-b-PG e PPG 25% e 75% EG-b-PG em termos de equivalentes-gramas. A influência da quantidade dos segmentos de PEG foi avaliada por ensaios de permeação com os gases CO2, CH4 e N2. Os filmes obtidos das dispersões foram caracterizados por espectrometria de infravermelho com transformadas de Fourier (FTIR), análise termogravimétrica (TGA), difração de raios x (DRX) e espalhamento de raios X a baixo ângulo (SAXS). Espectros de FTIR mostraram que os segmentos de EG influenciaram a frequência da banda de carbonila. Curvas de perda de massa (TG) mostraram perfis semelhantes de degradação, enquanto que as curvas derivadas apresentaram diferenças. DRX e SAXS mostraram que os segmentos de PEG promoveram uma maior ordenação na estrutura da membrana. Testes de permeação de gases mostraram que o aumento do teor de PEG aumentou o valor da permeabilidade para o CO2, indicando que os segmentos de PEG interagiram favoravelmente com este gás. Em relação ao CH4 e N2, houve uma diminuição na permeabilidade quando comparados com os valores encontrados para o CO2, sendo atribuído a perda de mobilidade segmental. Em termos de seletividade, para o par CO2/CH4 foi obtido um valor médio de 61,7 para a membrana contendo o maior teor de PEG, e o par CO2/N2 um valor médio de 121,5, sendo superior aos valores encontrados na literatura, tornando o material promissor

Estudo do efeito da adição de poli(glicol etilênico-b-glicol propilênico) na formação de dispersões aquosas poliuretânicas à base de poli(glicol propilênico)

Foram produzidas dispersões aquosas não-poluentes e inovadoras de poli(uretano-uréia) à base de poli(glicol propilênico) (PPG) e de copolímeros em bloco, poli(glicol etilênicob-glicol propilênico), (EG-b-PG) com teor de 7% de unidades de glicol etilênico. Os poli(uretano-uréia)s foram preparados, em duas etapas, pelo método do prepolímero. Na primeira etapa, foram obtidos anionômeros, sintetizados em massa, à base do copolímero EG-bPG, PPG, ácido dimetilol propiônico (DMPA) (gerador dos sítios aniônicos) e diisocianato de isoforona (IPDI). Ainda na primeira etapa, os grupos carboxílicos do DMPA foram submetidos à neutralização com trietilamina (TEA). Na segunda etapa, foi realizada a dispersão do prepolímero anionômero e, em seguida, foi conduzida a reação de extensão de cadeia com a hidrazina (HYD). Nas diferentes formulações, foram variadas a razão NCO/OH e as proporções de PPG e do copolímero em bloco EG-b-PG. Além disso, foram obtidas dispersões aquosas programadas para teores de sólidos de 40 e 50%. As dispersões foram avaliadas quanto ao teor de sólidos totais, tamanho médio de partícula e viscosidade. Os filmes, obtidos por vazamento das dispersões, foram avaliados quanto à absorção de água, termogravimetria (TG) e propriedades mecânicas (ensaio de tração). Os filmes vazados e os monômeros foram caracterizados por espectrometria na região de infravermelho (FTIR) As dispersões obtidas se mostraram adequadas para serem aplicadas como revestimento para madeira, metais e vidro

Caracterização e desenvolvimento de argilas para aplicação em nanocompósitos poliméricos

O Brasil é produtor de argilas e conta com grandes reservas deste recurso natural. Porém, grande parte da sua produção é comercializada seca e moída. O desenvolvimento de argilas para seu uso como reforço em nanocompósitos poliméricos constitui uma opção para os produtores desta matéria prima que teriam assim um produto com maior valor agregado. Este trabalho visa avaliar o potencial uso como nanocarga de duas argilas nacionais provenientes da Bacia de Taubaté, São Paulo, denominadas ALIGRA e SANTA FÉ. As frações de tamanho de partícula médio menor de 0,02 mm, obtidas por peneiramento á úmido da argila homogeneizada e seca, foram utilizadas no desenvolvimento do trabalho experimental. Os estudos de caracterização, envolvendo análise granulométrica, química, mineralógica, morfológica, térmica e textural, revelaram características muito semelhantes em ambas às argilas. Fração argila, maior de 70% em massa. Composição química conforme a definição química de uma argila e os teores de seus componentes mostram valores intermédios entre as apresentadas pelas bentonitas e argila caulinítica usadas com fins de comparação. Ressaltamse boas propriedades adsorventes. Área superficial específica BET ao redor de 120 m2/g, valor maior do que o apresentado por muitas bentonitas naturais (74,5 m2/g). Predominantemente mesoporosas, com poros, maiormente em forma de fenda, característicos da estrutura em camadas das argilas. Baixa capacidade de troca catiônica, 12 meq/100g. Difratogramas de raios-X revelaram a predominância do estratificado ilita/esmectita, caulinita e quartzo na argila ALIGRA, e de ilita, caulinita e quartzo na argila SANTA FÉ. Prosseguiu-se com a argila ALIGRA a preparação da argila organofílica. A argila organofílica foi obtida por troca catiônica com o sal quaternário de amônio: cloro cetril trimetil amônio, depois de homogeneizada em sódio com cloreto de sódio. Análises FTIR e TGA indicaram que houve inserção dos cátions orgânicos. Testes preliminares foram feitas, preparando misturas das argilas com matriz de polipropileno e usando como agente compatibilizante polipropileno enxertado com anidrido maleico. Resultados de ensaios de tração reportam algumas melhoras nas propriedades testadas com as composições preparadas com as argilas purificadas. Com as composições com argilas organofílicas somente foi melhorado o alongamento na rotura. Estudos ais aprofundados são recomendados.

复苏植物牛耳草干旱诱导的ACC氧化酶及乙烯调控的引导蛋白基因的克隆、表达与功能分析

本文以耐旱的牛耳草(Boea hygrometirica)为材料，研究了乙烯合成关键酶之一——ACC氧化酶编码基因（BhACO1）在干旱复苏过程中的诱导表达及其编码蛋白的酶活，分析了乙烯在干旱复苏过程中的积累及其对叶片复苏能力的影响和对干旱诱导基因的调控，探讨了一个受乙烯调控的干旱诱导的引导蛋白编码基因（BhDIR1）的表达及其功能。 利用cDNA微阵列技术从牛耳草干旱2h的叶片中得到一个ACC氧化酶基因片段，经5’-RACE得到全长cDNA，命名为BhACO1。BhACO1包含317个氨基酸，与其它植物中的ACC氧化酶具有80%左右的序列相似性。BhACO1基因受乙烯和干旱诱导、但ACC氧化酶抑制剂氯化钴可抑制其干旱诱导表达。BhACO1基因受ABA、2,4-D、SA、H2O2、CaCl2、EGTA及热害和盐害的诱导，但不受冷害诱导。原核表达的GST-BhACO1融合蛋白在体内体外均表现出ACC氧化酶的活性，而过量表达BhACO1的转基因植物的蛋白提取物也表现出较野生型更强的ACC氧化酶活性。 乙烯在牛耳草叶片干旱复水过程中随着时间延长而逐步积累。外源乙烯可诱导叶片黄化，但不影响叶片在复水后的复苏能力;氯化钴处理可部分地抑制乙烯合成而降低牛耳草叶片在干旱过程中乙烯的释放量，同时导致叶片失去复苏能力。与对照相比，氯化钴处理的叶片在干旱时仍可维持较低的离子渗漏水平，但复水后发生大量离子外渗，表明细胞膜完整性也遭到破坏;光系统ІІ活性下降程度在干旱时与对照相似，但复水后完全丧失。 乙烯诱导牛耳草干旱响应基因BhDohb561，BhLEA2和BhDIR1的表达，但不影响牛耳草干旱响应基因BhCML1，BhGRP1，BhSGP和BhLEA1的表达。除BhLEA1外，上述基因在干旱过程中的诱导表达均可被氯化钴预处理所抑制，尤其是BhSGP最明显。 BhDIR1在牛耳草干旱复水过程中mRNA明显地积累，乙烯、ABA、CaCl2、EGTA、H2O2、SA和热害、冷害、盐害都可诱导其表达。BhDIR1编码一个199个氨基酸的小分子量蛋白质，与松柏等植物中发现的可能参与木质素合成的引导蛋白具有约20-30%的序列相似性。与其它引导蛋白相同，BhDIR1在N’端包含一个外泌的信号肽，GFP定位分析表明BhDIR1定位于细胞膜和壁上。 上述结果表明，乙烯在牛耳草叶片耐脱水复苏反应中有不可或缺的作用，而ACC氧化酶所催化的反应是干旱诱导的乙烯合成中的关键步骤。氯化钴预处理通过抑制干旱过程中的乙烯合成，影响一系列基因的干旱诱导表达导致叶片在生理水平和细胞水平上造成了损伤，或是使牛耳草失去了在复水过程中原有的修复能力而无法恢复生命力。BhDIR1作为乙烯调控的下游靶基因之一，可能通过调控木质素的单体间的连接方式而改变木质素的物理性质来影响细胞壁的机械强度和柔韧性，减少干旱对细胞造成的机械伤害。

气体信号分子一氧化氮和乙烯的生物学功能：一氧化氮在植物盐胁迫中的作用和乙烯激活钙离子通道

一氧化氮（NO）是重要的植物信号分子，参与许多植物生理过程。以拟南芥野生型和Atnoa1突变体为材料研究了NO在植物抗盐胁迫中的作用。 T-DNA插入AtNOA1基因的第一个外显子，使Atnoa1突变体中NOS活性大幅度下降，NO释放减少。用不同浓度的NaCl对拟南芥野生型和Atnoa1突变体进行盐胁迫处理后，Atnoa1突变体中Na+离子积累较野生型多，K+离子吸收较野生型少，从而使突变体中的Na+/K+比野生型高，对突变体造成了更大的伤害。Atnoa1突变体种子萌发和幼苗生长对盐胁迫更敏感。盐胁迫处理后，Atnoa1突变体的存活率比野生型低。无论是在正常生长条件下，还是盐胁迫条件下，Atnoa1突变体中的H2O2和TBARS含量都比野生型中高，说明Atnoa1突变体对盐胁迫和氧化胁迫都比野生型更敏感。用NOS抑制剂和NO清除剂处理拟南芥野生型，减少内源NO释放量，使其在盐胁迫条件下的Na+/K+比增高。盐胁迫处理降低了野生型体内的NOS活性，减少了NOA1蛋白的表达，DAF-2DA标记的NO荧光强度减弱。用NO供体SNP处理Atnoa1突变体，可以减少盐胁迫引起的Na+/K+比增加。以上研究结果证明NOS介导的NO合成在植物抗盐胁迫中起重要作用。 乙烯作为一种植物气体激素参与植物生长发育的许多生理生化过程。植物细胞自由钙离子（[Ca2+]c）是重要信号分子，在植物应答外界信号中起非常重要的作用。外界信号通过开启植物细胞质膜的钙离子通道，使得胞外钙离子进入细胞，导致瞬间[Ca2+]c的增加，激活钙依赖型的蛋白和蛋白激酶，从而改变生理生化过程。本研究利用膜片钳和激光共聚焦显微技术，研究了外源乙烯对烟草悬浮细胞质膜Ca2+离子通道和细胞中[Ca2+]c活性的影响。乙烯供体乙烯利和乙烯合成前体ACC能够迅速诱导内向型电流，表明这些处理能开启离子通道。通过离子替代实验和离子通道的药理学分析证实乙烯利和ACC激活了一种对Ba2+, Mg2+和Ca2+等阳离子具有通透性的离子通道，La3+、Gd3+和Al3+抑制该通道的活性。乙烯受体拮抗物（1-MPP）和ACC合成酶抑制剂，能够减弱乙烯利和ACC对这种通道的活化作用，说明乙烯利和ACC是通过乙烯活化此类Ca2+离子通道。用Ca2+敏感的荧光标记物Fluo-3标记，通过激光共聚焦显微观察，发现乙烯利能够诱导烟草悬浮细胞中[Ca2+]c离子浓度的增加，而且Gd3+和BAPTA显著抑制乙烯利诱导的细胞中[Ca2+]c离子的增加。说明外源Ca2+离子通过质膜上被激活的Ca2+离子通道进入细胞，使细胞中[Ca2+]c离子浓度增加。以上结果说明，乙烯活化质膜上的Ca2+离子通道，使细胞外Ca2+离子进入细胞，导致细胞中[Ca2+]c离子浓度增加，是乙烯信号转导途径的重要步骤。

Role of transglutaminase-mediated cross-linking of protein in the temperature-dependent setting of Alaska pollack surimi

During the low temperature setting of fish paste, myosin heavy chain (MHC) is polymerized to cross-linked myosin heavy chain (CMHC), which is considered to occur by the action of endogenous transglutaminase (TGase). In this study the contribution of TGase on the setting of Alaska pollack surimi at different temperatures was studied. Alaska pollack surimi was ground with 3% NaCl, 30% h2o and with or without ethylene glycol bis (β-aminoethylether) N, N, N¹,N¹- tetra acetic acid (EGTA), an inhibitor of TGase. Among the pastes without EGTA, highest TGase activity was observed at 25°C but breaking force of the gel set at 25°C was lower than that set at 30°, 35°, and 40°C. Addition of EGTA (5m mol/kg) to the paste suppressed TGase activity at all setting temperatures from 20° to 40°C. Gelation of the pastes and cross-linking of MHC on addition of EGTA were suppressed completely at 20° and 25°C, partially at 30° and 35°C, and not at all at 40°C. The findings suggested that during the setting of Alaska pollack surimi TGase mediated cross-linking of MHC was strong at around 25°C but the thermal aggregation of MHC by non-covalent bonds was strong at above 35°C. Setting of surimi at 40°C and cross-linking of its MHC did not involve TGase.

Improving the performance of a valveless pulse combustor using unsteady fuel injection

This paper describes an experimental investigation into the effect of unsteady fuel injection on the performance of a valveless pulse combustor. Two fuel systems were used. The first delivered a steady flow of ethylene through choked nozzles, and the second delivered ethylene in discrete pulses using high-frequency fuel injectors. Both fuel systems injected directly into the combustion chamber. The high-frequency fuel injectors were phase locked to the unsteady pressure measured on the inlet pipe. The phase and opening pulse width of the injectors and the time-averaged fuel mass flow rate through the injectors were independently varied. For a given fuel mass flow rate, it is shown that the maximum pressure amplitude occurs when fuel is injected during flow reversal in the inlet pipe, i.e. flow direction is out of the combustor. The optimal fuel injection pulse width is shown to be approximately 2/9th of the cycle. It should, however, be noted that this is the shortest time in which the injectors can reliably be fully opened and closed. It is shown that by using unsteady fuel injection the mass flow rate of fuel needed to achieve a given amplitude of unsteady pressure can be reduced by up to 65% when compared with the steady fuel injection case. At low fuel mass flow rates unsteady fuel injection is shown to raise the efficiency of the combustor by a factor of 7 decreasing to a factor of 2 at high fuel mass flow rates. Copyright © 2008 by the American Institute of Aeronautics and Astronautics, Inc.

不同防冻剂对兔胚胎干细胞慢速冷冻保存的影响

干细胞冷冻保存是干细胞研究和临床应用中的必需技术.为提高兔胚胎干细胞在慢速冻存过程中的保存效果,比较了二甲基亚砜(DMSO)和乙二醇(ethylene glycol,EG)对兔胚胎干细胞冷冻保护效果.对冷冻复苏后的细胞进行台盼蓝染色,并研究其胚胎干细胞分子特性,结果表明DMSO比EG具有更好的冷冻保护效果.再在以10% DMSO为基础的防冻液中添加膜稳定剂海藻糖(trehalose)或谷氨酰胺(glutamine),细胞冷冻复苏后结果显示,谷氨酰胺对兔胚胎干细胞有明显的冷冻保护作用,使细胞存活率从71%提高到83.7%.当谷氨酰胺浓度为0、5、10、20、40 mmol/L分别加入防冻液中后,20 mmol/L的谷氨酰胺具有最佳的冷冻保护效果.以上结果得出兔胚胎干细胞慢速冷冻的防冻液改进配方为:在胚胎干细胞培养液中添加10% DMSO+20 mmol/L谷氨酰胺.