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

Comparação in vitro do desgaste dental em função da dureza de três diferentes tipos de materiais antagonistas

O objetivo deste estudo foi comparar in vitro o desgaste dental de pré-molares (PM) e molares (M) e sua relação com o valor de dureza Vickers dos materiais utilizados como antagonistas em uma máquina de abrasão simulada para provocar o desgaste nos dentes testados. Os materiais antagonistas utilizados foram VeraBond II (liga de Ni-Cr), Solidex (resina composta) e IPS Empress 2 (cerâmica). Para cada ensaio de dureza, foram preparados seis corpos-de-prova de cada material, os quais foram polidos sob refrigeração, com ciclo de 20 min para cada granulação. Num microdurômetro (HMV-2), foram realizadas três mossas por quadrante, cada uma sob carga de 19,614 N por 30 s, totalizando 12 mossas de base quadrada com ângulo de 136 entre os planos. O teste de abrasão foi realizado numa máquina simuladora de abrasão, freqüência de 265 ciclos/min e 4,4 Hz, com um percurso do antagonista de 10 mm à velocidade de 88 mm/s. Cada dente foi testado em oposição a um antagonista (foram 6 pares dente/material para cada grupo), em água deionizada, sob carga de 5 N, por 150 min, num total de 39.750 ciclos. Foram utilizados dezenove dentes 1 pré-molares, dezenove 3 molares e confeccionados doze antagonistas em cada material em forma de pastilha. Cada grupo de seis dentes foi testado em oposição a seis antagonistas do mesmo material. Ademais, um dente 1 pré-molar (PM) e um dente 3 molar (M) foram testados em oposição ao Plexiglass. Com relação ao desgaste do esmalte dentário (PM+M) segundo o material antagonista, o teste de Kruskal-Wallis evidenciou diferença significativa com p-valor < 0,001 e o teste de Mann-Whitney evidenciou diferença significativa nas comparações PM+M/resina X PM+M/metal (p-valor < 0,001), PM+M/resina X PM+M/cerâmica (p-valor < 0,001) e PM+M/metal X PM+M/cerâmica (p-valor = 0,002). A análise isolada, considerando pré-molares e molares separadamente, encontrou diferença significativa em relação ao desgaste do esmalte dentário no teste de Kruskall-Wallis, porém não detectou diferença significativa no teste de comparação múltipla Mann-Whitney quando comparou o desgaste sofrido pelo PM/metal em relação ao PM/cerâmica. Em relação à dureza Vickers detectou-se diferença significativa da dureza dos materiais no teste de Kruskall-Wallis (p-valor < 0,001) e também no teste de Mann-Whitney nas comparações múltiplas com p-valor = 0,002. Comparando-se a dureza com a perfilometria, observou-se uma correlação estatisticamente significativa (p ≤ 0,05) na correlação negativa (ρ= -0,829) entre a dureza do metal como material antagonista e o desgaste do esmalte dentário do dente molar. Os resultados sugeriram que todo material restaurador indireto estudado causou desgaste ao esmalte dentário quando submetido a forças de simulação de abrasão com carga. Embora tenha sido observada correlação entre dureza e resistência à abrasão, essa correlação foi pouco significativa.

Estudio de caso de Organización de Empresas : la comunicación como base del cambio en Bide Onera

Nuestro propósito con este trabajo es analizar la realidad organizacional de una empresa real: Bide Onera. Para ello hemos analizado la motivación, comunicación, liderazgo y trabajo en equipo, realizando finalmente unas propuestas de mejora que podrían solucionar los problemas de esta organización.

Maestras de Educación Infantil: identidad y cambio educativo

Este libro recoge parte de los resultados de un proyecto de investigación titulado “La Construcción de la Identidad docente del profesorado de educación infantil en la Formación y primeros años de trabajo”.

Ciudades y cambio de época : discursos sobre políticas urbanas y crisis en España : políticas urbanas en el escenario 2015 (CSO2011-28850)

Esta publicación forma parte del proyecto de investigación POLURB 20151, y tiene como objetivo general analizar las transformaciones que han experimentado y experimentan las principales ciudades españolas en la actualidad, concediendo una especial atención a las consecuencias de la actual crisis económica. El objetivo final del proyecto es proponer un nuevo marco analítico de las políticas urbanas, poniendo en valor un conjunto de nuevas experiencias que sirvan para ilustrar y ejemplificar nuevas políticas urbanas en la España del cambio de época. Es bien sabido que las crisis capitalistas representan momentos de reestructuración económica (o de "destrucción creativa") que permiten resolver los episodios de sobreacumulación. Pero los cambios nunca se sitúan solamente en la esfera de la producción, sino que también van acompañados de cambios en la esfera de la regulación para encubrir o apuntalar nuevas fracturas y desigualdades. Además, estos cambios son asimismo ventanas de oportunidad para nuevas iniciativas y políticas públicas, así como también para nuevos movimientos sociales y políticos que pueden aprovechar los nuevos escenarios que se abren. Pueden, por tanto, suponer espacios y momentos para la aparición de innovación urbana, sea en la forma de nuevas iniciativas o por la aparición de nuevos actores. Ante esta situación nos preguntamos ¿Qué rasgos presentan estos cambios, oportunidades e iniciativas en las ciudades españolas?, ¿qué suponen de nuevo respecto a las prácticas comunes anteriores a la crisis?

ANÁLISIS DEL EFECTO DEL CAMBIO DE LA DISTRIBUCIÓN DE CLASES MEDIANTE MÉTODOS DE REMUESTREO INTELIGENTE EN ÁRBOLES DE CLASIFICACIÓN SIMPLES Y CONSOLIDADOS

En los trabajos expuestos en esta memoria de tesis, hemos analizado elefecto que tienen sobre la capacidad de aprendizaje de diferentes algoritmosde clasificación los cambios en la distribución de clases, teniendo encuenta para ello, diferentes métodos de remuestreo de datos.En concreto se ha analizado este efecto en el conocido algoritmo deconstrucción de árboles de clasificación propuesto por Quinlan, el algoritmoC4.5, y en el algoritmo de construcción de árboles consolidados, elalgoritmo CTC, propuesto por el grupo de investigación ALDAPA de laUniversidad del País Vasco que, basado en el mismo C4.5, obtiene un árbol declasificación pero basado en un conjunto de muestras.Así mismo, planteamos cómo encontrar la distribución de clases más adecuadapara un algoritmo de clasificación y método de remuestreo concretos.

El amor como campo de reflexión, aprendizaje y cambio en las mujeres

Este trabajo analiza la manera en que las experiencias amorosas de las mujeres generan aprendizajes vitales que pueden provocar cambios en su manera de entender y vivir los vínculos amorosos. Para ello, se han estudiado las experiencias de 5 mujeres que, a través de sus vivencias, han cuestionado aspectos de la identidad de género en la que habían sido socializadas, han desmontado mitos sobre el amor romántico que tenían interiorizados, y han extraído aprendizajes que les han llevado a modificar su perspectiva y a introducir cambios en sus prácticas amorosas.

Spin-related phenomena in magnetic and spin-orbit couppled bose-einstein condensates

129 p.

ADAPTECC : Un juego de Rol sobre la Adaptación al Cambio Climático

El Juego de la Adaptación al Cambio Climático (ADAPTECC) es un juego de Rol diseñado para que los participantes experimenten las dificultades que surgen, tanto a nivel local como a nivel regional, cuando las autoridades correspondientes tienen que adoptar medidas de adaptación. La adaptación requiere anticipar los efectos adversos del Cambio Climático (CC) y tomar medidas para prevenir y minimizar el daño debido a los impactos del CC. Cada jugador se introduce en el rol de un alcalde o concejal de un municipio afectado por el CC, que debe decidir sobre las estrategias y medidas de adaptación de su municipio, o bien en el rol de un miembro del Departamento de Medio Ambiente de la región que debe repartir el presupuesto para adaptación entre los diferentes municipios. Al finalizar el juego, los participantes tendrán una mejor comprensión de los retos que plantea la adaptación al CC.

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.

Análisis de los nuevos tipos de fondos de inversión en España

Evaluación de la gestión y la performance de los nuevos Fondos de Inversión en España.

Plan de Marketing para Chocolates Valor S.A. 2015-2016

[ES] El presente trabajo es un plan de marketing para que la empresa Chocolates Valor S.A. lo implemente durante los años 2015-2016. El objetivo principal de este proyecto es aplicar los conocimientos obtenidos a lo largo de la carrera a una empresa real. Chocolates Valor es una empresa con amplia presencia en el mercado nacional y una fuerte imagen de marca. A pesar de ello, y como todas las empresas, tiene sus debilidades y no está explotando todas las oportunidades ofrecidas por el mercado. En la actualidad, la empresa cuenta con una imagen muy asociada al lujo y a un poder adquisitivo alto pero, en un entorno de crisis en el que el precio es un factor clave en la decisión de compra y los jóvenes tienen una gran importancia en el consumo, es necesario considerar la posibilidad de un cambio de posicionamiento y redireccionamiento hacia otros/ nuevos segmentos. A pesar de que Chocolates Valor diferencia dos tipos de clientes (consumidores y canal Horeca), en este trabajo solo se va a considerar el primero ya que el plan de marketing realizado está orientado exclusivamente al consumidor final.

Raíces estéticas de la música cubana, antecedentes de la canción popular, variantes y tipos (1800-1934): un estudio intercultural

192 p.

Acerca del posible y derivado carácter tecnológico de ciertos tipos óseos debitados: los casos de muescas, «écaillés» y retocadores

[ES] Los análisis efectuados sobre una serie de tipos óseos debitados (muescas, "écaillés" y retocadores) pertenecientes a los niveles musteroides y auriñacoides de los yacimientos de Gatzarria (Pays de Soule, Pyrénées Atlantiques) y Abeilles (Montmaurin, Haute Garonne) posibilitan sugerir hipótesis relativas a su causalidad. En este sentido, una gran parte del efectivo global examinado pudiera relacionarse directamente con determinados tratamientos tecnológicos de fractura, talla y retoque.

Efeito da temperatura de secagem de dois tipos de silano e da supressão ou redução do tempo de condicionamento com ácido hidrofluorídrico na resistência de união entre uma cerâmica de dissilicato de lítio e um cimento resinoso

Este estudo avaliou o efeito de diferentes métodos de silanização e aplicação do ácido hidrofluorídrico (HF) sobre a resistência à microtração de uma cerâmica de dissilicato de lítio a um cimento resinoso. Quarenta blocos de IPS e.max Press /Ivoclar Vivadent (5x5x6mm) foram cimentados a blocos de resina Z250/3M ESPE (5x5x6mm) usando o cimento resinoso RelyX ARC/3M ESPE de acordo com os seguintes métodos de tratamento superficial: G1: 20s de ácido fluorídrico (HF) + silano não hidrolisado Primer-Activactor/Dentsply (SNH) seco à temperatura ambiente; G2: 20s HF + silano pré-hidrolisado RelyX Ceramic-Primer/3M ESPE (SPH) seco à temperatura ambiente; G3: 10s HF + SNH seco com ar quente (50oC-2min); G4: 10sHF + SPH seco com ar quente (50oC-2min); G5: sem ácido, SNH seco com ar quente (50oC-2min); G6: sem ácido, SPH seco com ar quente (50oC-2min); G7: sem ácido, SNH seco à temperatura ambiente; G8: sem ácido, SPH seco à temperatura ambiente. Antes de cada método de silanização, os blocos cerâmicos receberam acabamento com lixas de carbeto de silício (220-600) e limpeza com ácido fosfórico 37% (1min). A cimentação foi realizada com carga vertical de 1kg por 10min. Os conjuntos de cerâmica/cimento/resina foram armazenados em água destilada (37C) por 24 horas e depois seccionados em máquina de corte Isomet 1000 a fim de obter palitos (n = 40) de 1mm2 de área da seção transversal, que foram submetidos ao teste de microtração em máquina de ensaio universal Emic (v = 0,5mm/min). O modo de fratura foi avaliado em microscópio eletrônico de varredura. A análise estatística foi realizada utilizando ANOVA / Dunnett (p-valor = 0,000). As médias MPa e desvio padrão foram: G1-21,5 (8,9) BC; G2-30,5 (7,2) A; G3-19.4 (9.1) BC; G4-24,0 (9,0) B; G5-8.1 (3.2) D; G6 -18,0 (6,2) C; G7-7.8 (2,6) D; G8-6.3 (2,5) D. Grupos 2, 3, 4 e 6 não tiveram falhas prematuras dos palitos contra os grupos 1, 5, 7 e 8, que apresentaram 2,2; 44,4; 75,6 e 33,3% de perdas prematuras, respectivamente. O teste de correlação foi realizado apresentando significância estatística, com valor de -0,736 (p-valor = 0,000), mostrando que, a medida que o percentual de perda prematura aumenta, a média da MPa diminui. Quanto ao modo de fratura, observou-se 44,97% de falhas do tipo mista, 51,70% de falhas do tipo adesiva, 3,33% de falhas do tipo coesiva do cimento. Quando é realizada a supressão do condicionamento com HF como pré-tratamento da superfície cerâmica IPS e.max Press, a aplicação de silano SPH, associada ao seu tratamento térmico, deve ser o método de silanização recomendado, embora os valores mais elevados de resistência de união tenham sido os obtidos quando utilizado o condicionamento com HF por 20s. Quando é realizada a redução do tempo de condicionamento com HF para 10s, a aplicação do silano (SPH ou SNH) deve ser sempre associada ao seu tratamento térmico. O SNH só deve ser usado se as superfícies das cerâmicas IPS e.max Press forem tratadas com HF.