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Catalytic pyrolysis technology is one of the thermochemical platforms used to produce high quality bio-oil and chemicals from biomass feedstocks. In the catalytic pyrolysis process, the biomass is rapidly heated under inert atmosphere in the presence of an acid catalyst or zeolite to promote deoxygenation and cracking of the primary vapors into hydrocarbons and small oxygenates. This dissertation examines the utilization of conventional fluid catalytic cracking (FCC) catalyst in the fractional catalytic pyrolysis of hybrid poplar wood. The influence of Y-zeolite content, steam treatment, addition of ZSM-5 additive, process conditions (temperature, weight hourly space velocity (WHSV) and vapor residence time) and recycling of the non-condensable gases (NCG) on the product distribution and the quality of the bio-oil were investigated. The first part of the study demonstrates the influence of catalytic property of FCC catalyst on the product distribution and quality of the bio-oil. It was found that FCC catalyst with higher Y-zeolite content produces higher coke yield and lower organic liquid fraction (OLF). Conversely, FCC catalyst with lower Y-zeolite content results in lower coke yield and higher OLF. The results showed that higher Y-zeolite content extensively cracks dehydrated products from cellulose decomposition and demethoxylates phenolic compounds from lignin degradation. The Y-zeolite promoted both deoxygenation and coke forming reactions due to its high catalytic activity and large pore size. Higher Y-zeolite content increased the quality of the bio-oil with respect to higher heating value (HHV), pH, density, and viscosity. The steam treatment at 732 oC and 788 oC decreased the total BET surface area of the FCC catalyst. The findings suggest that steam treatment reduces the coking tendency of the FCC catalyst and enhances the yield of the OLF. Analysis of the bio-oils showed that the steamed FCC catalyst produces bio-oil with lower viscosity and density. Gas chromatography and 13C-NMR spectrometry suggest that steam treatment affect the catalyst selectivity in the formation of CO, CO2, H2, CH4, C2-C5 hydrocarbons and aromatic hydrocarbons. The addition of ZSM-5 additive to the FCC catalyst was found to alter the characteristic/functionality of the catalytic medium. The product slate showed decrease in coke yield and increase in OLF with increase in ZSM-5 additive. The FCC/ZSM-5 additive hybrid catalysts produced bio-oils with relatively lower viscosity and higher pH value. The formation of CO2, CH4, and H2 decreased whilst C5 and aromatic hydrocarbons increased with increase in ZSM-5 additive level. The second part of the work assesses the effect of operating conditions on the catalytic pyrolysis process. The response surface methodology study showed reaction temperature to be the most influential statistically significant independent variable on char/coke yield, concentration of non-condensable gases, carbon content, oxygen content, pH and viscosity of the bio-oils. The WHSV was the most important statistically significant independent variable that affects the yield of organic liquid and water. Adequate and statistically significant models were generated for the prediction of the responses with the exception of viscosity. Recycling of the NCG in the process was found to potentially increase the liquid yield and decrease char/coke yield. The experiments with the model fluidizing gases showed that CO/N2, CO2/N2, CO/CO2/N2 and H2/N2 increase the liquid yield and CO2/N2 decrease char/coke yield. The results showed that recycling of NCG increases the higher heating value and the pH of the bio-oil as well as decreases the viscosity and density. The concept of recycling the NCG in the catalytic cracking of biomass vapors with FCC catalyst improved the overall process. The evaluation of the reactivity of conventional FCC catalyst towards bio-based molecules provide essential direction for FCC catalyst formulation and design for the production of high quality bio-oils from catalytic pyrolysis of biomass. / Ph. D.

L'adsorption de l'anthracène et de molécules de type Diphényl-polyènes (trans-Stilbene, 1,4-Diphenyl-1,3 butadiene, 1,6-Diphenyl-1,3,5-hexatriene) a été étudiée par simulations Monte Carlo, absorption UV-visible par réflexion diffuse, diffusion Raman multiexcitation et Résonance Paramagnétique Electronique (RPE) dans des zéolithes (aluminosilicates) à canaux de type Ferrierite (M-FER), ZSM-5 (MnZSM-5) et Mordenite (M-MOR).<br />Les résultats mettent en évidence l'insertion des molécules dans les canaux. Dans le cas de cations polarisants (M = H+ et Li+) une ionisation spontanée produit la formation de paires radical cation – électron de longue durée. Au cours de la recombinaison de charges, des paires électron-trou sont mises en évidence par des techniques impulsionnelles de RPE. Dans le cas des molécules insérées sans modification chimique (M = Na+, K+, Rb+, Cs+), la photolyse UV induit des paires de radicaux dont la lente recombinaison implique des phénomènes de transferts d'électrons régis par la théorie de Marcus. L'exceptionnelle stabilité des paires de radicaux est attribuée au confinement des molécules dans les canaux, à la teneur en aluminium et à la nature des cations de la zéolithe. Ces paires de radicaux sont des intermédiaires réactionnels mis en jeu dans les processus catalytiques et de photodégradation d'hydrocarbures. Ils sont aussi impliqués dans le processus primordial de l'effet photovoltaïque.

Made available in DSpace on 2016-12-08T17:19:22Z (GMT). No. of bitstreams: 1 Rafaela de Souza Schmidt.pdf: 1614603 bytes, checksum: 4583716d044cc6f09dfcf335690ab75e (MD5) Previous issue date: 2014-01-31 / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / The synthesis of zeolites from alternative materials and low cost had great development in recent decades due to the fact of processes using conventional silicon and aluminum solutions are expensive .solutions of silicon and aluminum are extremely expensive. The synthesis can be carried out by any raw material containing predominantly silica and alumina, such as clays and rice husk. Thus, this study aims to develop an alternative methodology for the synthesis of zeolite ZSM-5, using silica extracted from rice husk and commercial metakaolin as raw materials in the composition of the mixture. The process of synthesis solution was hydrothermally sodium in the presence of TPABr and as a structural director. To assess the effect of temperature on the formation of ZSM-5, the synthesis procedure was carried out in temperature ranges between 100 and 170°C. Through the characterization of zeolitic material formed in the crystallization process, it was concluded that the methodology proposed in this work led typical crystalline phases of zeolite ZSM-5, as well as the formation of other zeolite phases. / A síntese de zeólitas a partir de materiais alternativos e de baixo custo teve grande desenvolvimento nas últimas décadas devido ao fato dos processos que utilizam soluções convencionais de silício e alumínio serem caros. A síntese pode ser realizada por qualquer matéria prima que contenha predominância de sílica e alumina, como por exemplo, argilas e casca de arroz. Sendo assim, este trabalho tem como objetivo desenvolver uma metodologia alternativa de síntese de zeólita ZSM-5, empregando sílica extraída da casca de arroz e metacaulim comercial, como matérias primas na composição da mistura reacional. O processo de síntese ocorreu hidrotérmicamente em solução sódica e na presença de TPABr como direcionador estrutural. Para avaliar o efeito da temperatura na formação da ZSM-5, o processo de síntese foi realizado em faixas de temperatura entre 100 e 170°C. Através da caracterização do material zeólítico formado no processo de cristalização, foi concluído que a metodologia proposta neste trabalho conduziu fazes cristalinas típicas de zeólita ZSM-5, bem como a formação de outras fases zeolíticas.

Submitted by Automa??o e Estat?stica (sst@bczm.ufrn.br) on 2016-05-30T22:35:15Z No. of bitstreams: 1 AnelieseLunguinhoFigueiredo_TESE.pdf: 2224810 bytes, checksum: a3cbfc32831dba5f9b8a0085f1244167 (MD5) / Approved for entry into archive by Arlan Eloi Leite Silva (eloihistoriador@yahoo.com.br) on 2016-06-01T19:31:41Z (GMT) No. of bitstreams: 1 AnelieseLunguinhoFigueiredo_TESE.pdf: 2224810 bytes, checksum: a3cbfc32831dba5f9b8a0085f1244167 (MD5) / Made available in DSpace on 2016-06-01T19:31:41Z (GMT). No. of bitstreams: 1 AnelieseLunguinhoFigueiredo_TESE.pdf: 2224810 bytes, checksum: a3cbfc32831dba5f9b8a0085f1244167 (MD5) Previous issue date: 2015-07-24 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior (CAPES) / As ze?litas s?o amplamente utilizadas pela ind?stria em processos de cat?lise, adsor??o, separa??o e troca i?nica. No entanto, a presen?a apenas de microporos limita a difus?o de mol?culas volumosas em seus canais, favorecendo a ocorr?ncia de rea??es indesej?veis devido ao longo tempo de resid?ncia dos reagentes e produtos ao serem transportados ao longo dos microporos das ze?litas. Com o intuito de superar este problema, foram estudados neste trabalho m?todos de s?ntese para a obten??o da ze?lita ZSM-5 nanocristalina com porosidade hier?rquica sintetizada na aus?ncia de direcionador org?nico de estrutura. Primeiramente foi realizada a s?ntese da ze?lita ZSM-5 atrav?s do m?todo assistido por sementes em um sistema ausente de direcionador org?nico, onde as amostras foram sintetizadas utilizando tr?s tipos diferentes de sementes: duas destas baseadas em solu??es aquosas claras contendo os precursores de ZSM-5 (n?o silanizada e silanizada) e a terceira semente baseada em uma ze?lita ZSM-5 comercial na forma de p?, a fim de direcionar na forma??o da estrutura MFI. O segundo m?todo empregado foi o processo de silaniza??o, utilizando como agente silanizante o fenilaminopropiltrimetoxisilano (PHAPTMS), com a finalidade de diminuir ou impedir o crescimento dos cristais ze?liticos da ZSM-5, favorecendo a obten??o de cristais com menores dimens?es. A s?ntese da ZSM-5 tamb?m foi realizada na aus?ncia de direcionador org?nico a 180?C por 27 horas ap?s a adi??o do PHAPTMS. Todas as amostras sintetizadas foram caracterizadas por diversas t?cnicas, dentre elas a Difra??o de Raios-X (DRX), Espectroscopia na regi?o do Infravermelho com Transformada de Fourier (FTIR), adsor??o-dessor??o de Arg?nio (Ar), Microscopia Eletr?nica (SEM e TEM) e dessor??o a temperatura programada TPD-NH3. Notou-se que o uso de sementes proporciona uma maior ?rea espec?fica BET e provoca um aumento na ?rea externa, devido ? diminui??o do tamanho dos cristais. Da mesma forma para amostra funcionalizada com o agente silanizante (HZSM-5 (PHAPTMS)), que apresentou a mais, um duplo sistema de poros, o primeiro associado ? microporosidade da ze?lita ZSM-5 (0,5 - 2 nm) e o outro relacionado ? mesoporos intercristalinos (2 - 6 nm), confirmando a obten??o da ze?lita HZSM-5 hier?rquica. Todas as amostras sintetizadas apresentaram aglomerados globulares formados por pequenas nanounidades (30 - 90 nm), com morfologia e tamanho dos cristais diferentes da ze?lita HZSM-5 utilizada como refer?ncia. Os testes catal?ticos utilizando o craqueamento do polietileno de baixa densidade (PEBD) e o processo de pir?lise do poli(etileno tereftalato) - PET provaram que a melhoria nas propriedades texturais das ze?litas sintetizadas ? vantajoso em tais processos, apresentando um desempenho superior quando comparado ? amostra de refer?ncia, fornecendo produtos que podem ser utilizados como mat?rias-primas na ind?stria petroqu?mica. / Zeolites are widely used by the industry in catalysis processes, adsorption, separation and ion exchange. However, the presence of only micropores limits the diffusion of bulky molecules in their channels, favoring the occurrence of adverse reactions due to long residence time of the reactants and products are transported through the micropores of the zeolite. In order to overcome this problem has been studied in this work synthesis methods for obtaining hierarchical nanocrystalline ZSM-5 zeolite synthesized in the absence of organic template. First it carried out a synthesis of zeolite ZSM-5 by the seed-assisted method from an organic-templatefree system, where the samples were synthesized utilizing three different types of seeds: two of these based on aqueous clear solutions containing the ZSM-5 precursors (non-silanized and silanized) and the third seed based on a commercial ZSM-5 zeolite in powder form, in order to direct the formation of the MFI structure. The second method used was the silanization process, using as silanizante agent phenylaminopropyltrimethoxysilane (PHAPTMS), in order to lessen or prevent the growth of zeolitic crystals of ZSM-5, obtaining favoring smaller crystals. The synthesis of ZSM-5 was also performed in the absence of organic template 180?C for 27 hours after addition of PHAPTMS. All synthesized samples were characterized by several techniques, among them X Ray Diffraction (XRD), Fourier Transform Infrared Spectroscopy (FTIR), Argon adsorption-desorption, Electronic Microscopy (SEM and TEM), and Temperature Programmed Desorption of Ammonia (NH3-TPD). It was noted that the use of seeds gives a higher BET surface area and causes an increase in the external surface area outside due to the decreasing size of the crystals. Similarly for sample functionalized with silanizante agent (MFI (PHAPTMS)), which is the lowest a dual system of pores, the first associated with the microporosity of the zeolite ZSM-5 (0.5 - 2 nm) and the other related to intercrystalline mesopores (2 - 6 nm), confirming the obtaining of HZSM-5 zeolite hierarchical. All samples were synthesized globular agglomerates formed by small nanounits (30 - 90 nm) with different size and morphology of crystals of zeolite HZSM-5 used as reference. The catalytic tests using the cracking of low density polyethylene (LDPE) and pyrolysis of poly(ethylene terephthalate) - PET proved that the improvement in the textural properties of the synthesized zeolite is advantageous in such processes, with a better performance when compared to the reference sample, generating products which can be useful feedstocks in the petrochemical industry.

Conselho Nacional de Desenvolvimento Científico e Tecnológico / This work aims the synthesis and study of ZSM-5 catalysts for the conversion of ethanol to light olefins, especially, using an alternative and inexpensive route. The ethanol emerges as a renewable source for the production of olefins and the ZSM-5 catalyst has important characteristics for this type of reaction such as acidity, surface area and particle size. The synthesis was carried out in hydrothermal treatment at 170 °C. Were performed two conventional synthesis with templates, using n-Butylamine and tetrapropylammonium hydroxide (TPAOH), and an third and alternative route using a nucleating gel. The catalyst characterization was performed using several techniques (XRD, BET, XRF, SEM and TGA) and was observed the formation of the ZSM-5 structure in all the synthesis methods. The catalysts were evaluated in the ethanol to olefins (ETO) reaction, and was evaluated the influence of the reaction temperature (250 to 450 °C) and SAR (SiO2/Al2O2 ratio) in the selectivity for olefins. The products analyses were made with a gas chromatograph with a FID-type detector. The ethylene yield was above to 80 % for all catalysts, and some above 90 %. Lower SAR values provided higher yields for propylene, around to 9 %. The temperature, SAR and template used in the synthesis influenced in the selectivity. In addition, was evaluated the influence of the catalyst mass, dilution and also its modification with different metals. When the mass was increase, the yield for propylene increased. The catalyst dilution with common sand provided, in some concentrations, greater propylene formation. The nucleating gel method showed to be a viable alternative for ZSM-5 synthesis and its use in the ETO reaction. / Este trabalho relata o estudo da síntese e caracterização de catalisadores ZSM-5 para seu posterior uso na reação de conversão de etanol para olefinas, especialmente utilizando uma rota alternativa mais econômica. O etanol surge como uma fonte renovável para a produção de olefinas e o catalisador ZSM-5 possui importantes características para esse tipo de reação, tais como acidez, área superficial e tamanho de partícula. A síntese foi conduzida de maneira hidrotérmica a 170 °C. Foram realizadas duas sínteses convencionais com direcionadores de estrutura, utilizando n-butilamina e hidróxido de tetrapropilamônio (TPAOH), e uma terceira rota alternativa utilizando um gel nucleante. A caracterização dos compostos sintetizados foi realizada com diversas técnicas (DRX, BET, FRX, MEV e TGA) sendo observada a formação da estrutura de ZSM-5 em todas as técnicas de síntese utilizadas. Os catalisadores foram avaliados na reação de conversão de etanol à olefinas (ETO) e foi avaliada a influência da temperatura de reação (250 a 450 °C) e SAR (SiO2/Al2O3 ratio) na seletividade das olefinas. A análise dos produtos formados foi realizada em um cromatógrafo a gás com detector tipo FID. O rendimento para eteno foi superior a 80 % em todos os catalisadores, sendo para alguns acima de 90 %. Baixos valores de SAR proporcionaram maiores rendimentos para propeno, em torno de 9 %. A temperatura, o valor de SAR e os direcionadores empregados na síntese influenciaram na seletividade. Também, foi avaliada a influência da quantidade de massa do catalisador, a diluição e também a modificação com diferentes metais (Ga, La, In) e um não metal (P). Quando a massa foi aumentada, o rendimento para propeno aumentou consideravelmente. A diluição com areia comum, em algumas concentrações, proporcionou maior formação de propeno. O método de síntese via gel nucleante mostrou ser uma alternativa viável para a síntese de ZSM-5 e seu uso como catalisador na reação ETO.

Diese Arbeit befasst sich mit der katalytischen Umsetzung von oxygenierten Kohlenwasserstoffen in einem Strömungsrohrreaktor bei 500 °C an mikroporösem Alumosilicat ZSM-5, an dem mesoporösem Alumosilicat Al-MCM-41 sowie an deren Mischphasen. Anhand der katalytischen Untersuchungen ist es möglich, für verschiedene Anforderungen an das Produktspektrum Empfehlungen an die Eigenschaften des zu verwendeten Katalysatorsystems zu formulieren. Hierfür wurden Untersuchungen zum Einfluss relevanter Syntheseprozessparameter auf die Zusammensetzung von Al-MCM-41/ZSM-5-Mischphasen vorgenommen. Die Synthese solcher Mischphasen wurde über einen 'Zwei-Template/Ein-Schritt“-Ansatz durchgeführt, der es erlaubte, die an das Katalysatorsystem gestellten Anforderungen durch eine geeignete Wahl der Syntheseparameter zu genügen. Während der Synthese der Al-MCM-41/ZSM-5-Mischphasen beobachtet man drei sich gegenseitig beeinflussenden Vorgänge, die durch, in der wässrigen Syntheselösung vorliegende, alumosilicatische Komponenten miteinander verknüpft sind: Die Auflösung und anschließende Restrukturierung einer nicht-porösen amorphen Phase, die Auflösung und Restrukturierung einer mesoporösen Al-MCM-41-Phase und die Kristallisation einer mikroporösen ZSM-5-Phase. Durch die Erhöhung des Al-Anteils im Synthesegel werden die ZSM-5-Kristallisation verlangsamt und der Schwerpunkt des Gleichgewichts dieser drei Vorgänge für einen gegebenen Reaktionszeitpunkt in Richtung der Bildung der mesoporösen Al-MCM-41-Phase verlagert. Der Einfluss des, in das jeweilige Katalysatorsystem eingebauten Aluminiums auf die katalytische Umsetzung von Oxygenaten manifestiert sich für die beiden Alumosilicate ZSM¬ 5 und Al MCM-41 auf verschiedene Weise. Eine Erhöhung des Al-Anteils in einem mikroporösen ZSM-5-Katalysatorsystem begünstigt den Verlauf von bimolekularen Reaktionen. Dies äußert sich in einem verstärkten Auftreten von Paraffin-bildenden Raktionen wie die Wasserstoff-Transfer-Reaktionen und/oder die Carboniumionen-Spaltung sowie in einer Dominanz von Aromaten-bildenen Reaktionen wie die Cyclisierung mit anschließender Dehydrierung und Aromatisierung. Dieser Effekt kann bei einer Erhöhung des Al-Anteils in einem mesoporösen Al-MCM-41-Katalysatorsystem nur im geringen Maße beobachtet werden. Jedoch nimmt mit sinkendem Si/Al-Verhältnis in beiden Katalysatorsystemen der Anteil an Produkten mit drei oder vier Kohlenstoffatomen zu. Zudem kann dabei eine beginnende Unabhängigkeit des gebildeten Produktspektrums von der Kettenlänge und der funktionellen Gruppe des umgesetzten Oxygenats beobachtet werden.:Inhaltsverzeichnis 1 Einleitung und Problemstellung 1 2 Grundlagen 4 2.1 Hydrothermale Synthese von Alumosilicaten 4 2.1.1 WÄSSRIGE CHEMIE UND HYDROTHERMALE BEHANDLUNG VON ALUMOSILICATEN 4 2.1.2 STRUKTUR UND BILDUNGSMECHANISMUS VON AL-MCM-41 5 2.1.3 STRUKTUR UND BILDUNGSMECHANISMUS VON ZSM-5 6 2.2 Katalytische Spaltung von Kohlenwasserstoffen an Alumosilicaten 9 2.2.1 NATUR UND LOKALISIERUNG VON SÄUREZENTREN 9 2.2.2 KOHLENWASSERSTOFF-POOL-MECHANISMUS UND VERKOKUNG 10 3 Experimentelles Vorgehen und analytische Messverfahren 14 3.1 Syntheseroute zur Herstellung von Al MCM 41/ZSM 5-Mischphasen, Al MCM 41 und ZSM-5 14 3.1.1 AL MCM 41/ZSM 5 MISCHPHASEN 14 3.1.2 AL-MCM-41 17 3.1.3 ZSM-5 17 3.2 Datenerhebung und -auswertung relevanter physikalisch-chemischer und festkörperanalytischer Charakterisierungsmethoden 17 3.2.1 PULVER-RÖNTGENDIFFRAKTOMETRIE 17 3.2.2 N2-PHYSISORPTION 19 3.2.3 TEMPERATUR-PROGRAMMIERTE AMMONIAK-DESORPTION 21 3.2.4 ELEMENTARANALYSE 23 3.2.5 27AL MAS NMR 24 3.2.6 THERMOGRAVIMETRISCHE ANALYSE 25 3.3 Katalytische Austestung und Analyse der Messdaten 26 3.3.1 VERSUCHSDURCHFÜHRUNG 26 3.3.2 ANALYSE UND AUSWERTUNG KATALYTISCHER MESSDATEN 27 3.3.3 DURCHGEFÜHRTE KATALYTISCHE TESTMESSUNGEN 29 4 Untersuchungen zum Bildungsmechanismus von Al MCM 41/ZSM 5-Mischphasen 33 4.1 Mechanistische Deutung 33 4.1.1 VORBETRACHTUNG 33 4.1.2 REAKTIONSABLAUF 34 4.1.3 UNTERSUCHUNG DER MESOPOROSITÄT 39 4.1.4 MORPHOLOGISCHE BETRACHTUNG 43 4.2 Wechselwirkungen der „Beeinflussungsfaktoren“ 45 4.2.1 EFFEKT VERSCHIEDENER AUTOKLAV-TYPEN 45 4.2.2 EFFEKT DES AL-ANTEILS IM SYNTHESEGEL 48 4.2.3 SYMBIOTISCHE EINFLUSSNAHME VON ALUMINIUM UND TENSIDEN 50 5 Charakterisierung verwendeter Katalysatormaterialien 52 5.1 ZSM-5 52 5.2 Al-MCM-41 57 5.3 Physikalische Mischungen aus Al-MCM-41 und ZSM-5 60 6 Katalytisches Spalten von Oxygenaten an ZSM 5 64 6.1 Katalytisches Spalten von Alkohol-Oxygenaten an ZSM 5 in Abhängigkeit des Si/Al Verhältnisses 64 6.1.1 PRODUKTANALYSE ANHAND DER KOHLENSTOFFANZAHL IM PRODUKTMOLEKÜL 65 6.1.2 PRODUKTANALYSE ANHAND EINZELNER STOFFGRUPPEN 68 6.2 Katalytisches Spalten von Carbonyl-Oxygenaten an ZSM 5 in Abhängigkeit des Si/Al Verhältnisses 71 6.2.1 PRODUKTANALYSE ANHAND DER KOHLENSTOFFANZAHL IM PRODUKTMOLEKÜL 72 6.2.2 PRODUKTANALYSE ANHAND EINZELNER STOFFGRUPPEN 76 6.3 Ableitung eines Kohlenwasserstoff-Pool Mechanismus zur Beschreibung des katalytischen Spaltens von Oxygenaten an ZSM 5 80 6.3.1 VEREINHEITLICHUNG DES OXYGENAT FEEDS ÜBER DESSEN DEOXYGENIERUNG 81 6.3.2 ASSIMILATION KURZKETTIGER OLEFINE DURCH EINEN KATALYTISCH AKTIVEN BEREICH 83 6.3.3 EINFLUSS DES PORENSYSTEMS UND AL-ANTEILS IM KATALYSATORSYSTEMS 85 6.3.4 BESCHREIBUNG DER PRODUKTBILDUNG EINZELNER STOFFGRUPPEN IN ABHÄNGIGKEIT WESENTLICHER REAKTIONSBEDINGUNGEN 87 7 Katalytisches Spalten von Triacylglyceriden an Al MCM 41 und physikalischen Mischungen aus Al-MCM-41 und ZSM-5 92 7.1 Gegenüberstellung des katalytischen Spaltens von Ethyloctanoat an Al MCM 41 und ZSM 5 in Abhängigkeit des Si/Al Verhältnisses 92 7.2 Anwendung des Kohlenwasserstoff-Pool Mechanismus zur Beschreibung des katalytischen Spaltens von Triacylglyceriden an physikalischen Mischungen aus Al MCM-41 und ZSM-5 97 7.3 Synthese-Struktur-Wirkungsprinzip 103 8 Zusammenfassung und Ausblick 106 Literatur 112 Abbildungsverzeichnis 127 Tabellenverzeichnis 139 Abkürzungsverzeichnis 141 Anhang 142 Veröffentlichungen 165 Eidesstattliche Erklärung 168

Made available in DSpace on 2014-12-17T15:42:28Z (GMT). No. of bitstreams: 1 MariaJFC_TESE.pdf: 4007652 bytes, checksum: 7bb363c54641679d79bbff5c76de539f (MD5) Previous issue date: 2013-06-03 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / The processing of heavy oil produced in Brazil is an emergency action and a strategic plan to obtain self-sufficiency and economic surpluses. Seen in these terms, it is indispensable to invest in research to obtain new catalysts for obtaining light fraction of hydrocarbons from heavy fractions of petroleum. This dissertation for the degree of Doctor of Philosophy reports the materials preparation that combine the high catalytic activity of zeolites with the greater accessibility of the mesoporosity, more particularly the HZSM-5/MCM-41 hybrid, done by synthesis processes with less environmental impact than conventional ones. Innovative methodologies were developed for the synthesis of micro-mesoporous hybrid material by dual templating mechanism and from crystalline zeolitic aluminosilicate in the absence of organic template. The synthesis of hybrid with pore bimodal distribution took place from one-single organic directing agent aimed to eliminate the use of organic templates, acids of any kind or organic solvents like templating agent of crystalline zeolitic aluminosilicate together with temperature-programmed microwave-assisted, making the experimental procedures of preparation most practical and easy, with good reproducibility and low cost. The study about crystalline zeolitic aluminosilicate in the absence of organic template, especially MFI type, is based on use of H2O and Na+ cation playing a structural directing role in place of an organic template. Advanced characterization techniques such as X-Ray Diffraction (XRD), Fourier Transform Infrared Spectroscopy (FTIR), Scanning Electron Microscopy (SEM), Highresolution Transmission Electron Microscopy (HRTEM), Adsorption of N2 and CO2, kinetic studies by Thermogravimetric Analysis (TGA) and Pyrolysis coupled to Gas Chromatography/Mass Spectrometry (Pyrolysis-GC/MS) were employed in order to evaluate the synthesized materials. Achieve the proposed objectives, has made available a set of new methodologies for the synthesis of zeolite and hybrid micro-mesoporous material, these suitable for catalytic pyrolysis of heavy oils aimed at producing light fraction / O processamento do petr?leo pesado produzido no Pa?s ? uma a??o emergencial e estrat?gica para obter a auto-sufici?ncia e super?vits econ?micos. Neste sentido, ? indispens?vel o investimento em pesquisas de novos catalisadores para obten??o de derivados leves a partir de fra??es pesadas do petr?leo. O trabalho de doutorado aqui reportado dedicouse ? prepara??o de materiais que combinem, numa ?nica estrutura, a elevada atividade catal?tica de ze?litas, com melhor acessibilidade de materiais mesoporosos, como a estrutura h?brida HZSM-5/MCM-41, utilizando processos de s?ntese com menor impacto ambiental que os convencionais. Metodologias inovadoras foram desenvolvidas para a s?ntese do catalisador h?brido micro-mesoporoso ou ze?lito-mesoporoso por mecanismo de direcionamento estrutural via duplo agente diretor org?nico e tamb?m a partir de estrutura zeol?tica sintetizada na aus?ncia total de direcionador org?nico. Esse ?ltimo, tamb?m chamado de s?ntese do h?brido com distribui??o bimodal de poros a partir de um ?nico agente diretor org?nico, visou eliminar o uso dos direcionadores org?nicos, ?cidos de qualquer natureza ou solventes org?nicos como molde estrutural da estrutura zeol?tica em conjunto com o m?todo hidrot?rmico assistido por irradia??o via micro-ondas, tornando o procedimento experimental de prepara??o pr?tico e simples, com boa reprodutibilidade e menor custo. A metodologia de prepara??o da ze?lita MFI do tipo ZSM-5 utiliza H2O e c?tions Na+ no papel de direcionamento estrutural e compensa??o de cargas na estrutura. T?cnicas relevantes de caracteriza??o, como Difra??o de Raios-X (XRD), Espectroscopia no Infravermelho com Transformada de Fourier (FTIR), Microscopia Eletr?nica de Varredura (SEM), Microscopia Eletr?nica de Transmiss?o de Alta Resolu??o (HRTEM), Adsor??o de N2 e CO2, estudos cin?ticos via An?lises Termogravim?tricas (TGA) e Pir?lise acoplada ? Cromatografia Gasosa/Espectrometria de Massas (Pyrolysis-GC/MS), foram empregadas no intuito de avaliar os materiais sintetizados. Alcan?ados os objetivos propostos, disponibilizou-se um conjunto de novas metodologias para s?ntese de catalisadores zeol?ticos e h?bridos micromesoporosos, estes adequados para pir?lise catal?tica de ?leos pesados visando ? produ??o de derivados leves

The effect of microwave radiation on the prepared 0.5Fe/ZSM-5 catalysts as a post-synthesis modification step was studied in the methanol-to-hydrocarbons process using the temperature-programmed surface reaction (TPSR) technique. This was achieved by preparing a series of 0.5Fe/ZSM-5 based catalysts under varying microwave power levels (0–700 W) and over a 10 s period, after iron impregnating the HZSM-5 zeolite (Si/Al = 30 and 80). Physicochemical properties were determined by XRD, SEM, BET, FT-IR, C3H9N-TPSR, and TGA techniques. It was found that microwave radiation induced few changes in the bulk properties of the 0.5Fe/ZSM-5 catalysts, but their surface and catalytic behavior were distinctly changed. Microwave radiation enhanced crystallinity and mesoporous growth, decreased coke and methane formation, decreased the concentration of Brønsted acidic sites, and decreased surface area and micropore volume as the microwave power level was increased from 0 to 700 W. From the TPSR profiles, it was observed that microwave radiation affects the peak intensities of the produced hydrocarbons. Application of microwave radiation shifted the desorption temperatures of the MTH process products over the HZSM-5(30) and HZSM-5(80) based catalysts to lower and higher values respectively. The MeOH-TPSR profiles showed that methanol was converted to DME and subsequently converted to aliphatic and aromatic hydrocarbons. It is reasonable to suggest that microwave radiation would be an essential post-synthesis modification step to mitigate coke formation and methane formation and increase catalyst activity and selectivity. / Chemical Engineering / M. Tech. (Chemical Engineering)

Cette étude se situe dans le cadre des recherches menées par le CEAEA sur la production massive d'hydrogène, sans émission de gaz à effet de serre, via un cycle thermo-chimique de décomposition de l'eau couplé à une source de chaleur à haute température d'origine nucléaire. Dans le cas particulier du cycle dit« Iode-Soufre», on doit extraire H2 à partir d'un mélange H2/HI/H20 très corrosif, opération pour laquelle des procédés membranaires ont été proposés. L'objectif de ce travail est le développement de membranes zéolithiques de type MFI susceptibles d'être utilisées dans ce contexte. Nous présentons les différents matériaux utilisés, la méthodologie de synthèse de couches minces de Silicalite-1 et de ZSM-5 synthétisée sans structurant organique, les techniques de caractérisation des membranes. Une étude cinétique nous a permis d'optimiser et de contrôler les conditions d'obtention de ces couches minces déposées sur des substrats tubulaires en Ti02 et plans en Al2O3-α. De nombreuses expériences de perméation ont été réalisées, pour des gaz simples (H2, He, Ar, N 2, C02, SF6) et des mélanges gazeux (H2/H20/Ar) et (H2/H20/HI/Ar). Les effets de la température, de la pression amont, de l'épaisseur et de la longueur de la couche mince ainsi que du gaz vecteur ont été étudiés en détail. Il apparaît que la présence de molécules d'H20 dans le système joue un rôle prépondérant sur la perméation des autres molécules. / In the general context of massive and "carbon free" hydrogen production studies, the aim of this work was the development of zeolitic MFI membranes for hydrogen extraction and separation. The methodology of synthesis, the membranes characterization techniques as well as the permeation experimental setup are presented. Optimization and control of the elaboration of Ti02 supported Silicalite-1 and template free ZSM-5 membranes have been reached. Details of the full kinetic study that we performed are given. Numerous permeation experiments, involving pure gas (H2, He, Ar, N2, C02, SF6) and mixtures (H2/H20/Ar) and (H2/H 20/HI/Ar) have been carried on. The effects of temperature, feed pressure, thickness and length of the membranes, as well as the role of the sweeping gas have been emphasized. In the case of gas mixtures, the presence of H20 molecules appears to be a predominant factor.