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@PhDThesis{Souza:2022:CaSuAl,
               author = "Souza, Amanda Cassiano de",
                title = "Catalisadores suportados em aluminas dopadas para 
                         decomposi{\c{c}}{\~a}o do per{\'o}xido de hidrog{\^e}nio em 
                         propulsores de sat{\'e}lites",
               school = "Instituto Nacional de Pesquisas Espaciais (INPE)",
                 year = "2022",
              address = "S{\~a}o Jos{\'e} dos Campos",
                month = "2022-08-05",
             keywords = "catalisador, {\'o}xidos mistos, per{\'o}xido de hidrog{\^e}nio, 
                         propuls{\~a}o, catalyst, mixed oxides, hydrogen peroxide, 
                         propulsion.",
             abstract = "Ap{\'o}s v{\'a}rias d{\'e}cadas de dom{\'{\i}}nio da 
                         hidrazina como propelente de propulsores de sat{\'e}lites, sua 
                         utiliza{\c{c}}{\~a}o come{\c{c}}ou a ser questionada em 
                         fun{\c{c}}{\~a}o do seu perigo {\`a} sa{\'u}de humana e ao 
                         meio ambiente. Uma das alternativas {\`a} hidrazina {\'e} o uso 
                         do per{\'o}xido de hidrog{\^e}nio (H2O2), monopropelente 
                         classificado como sendo verde, uma vez que sua 
                         decomposi{\c{c}}{\~a}o gera os compostos qu{\'{\i}}micos 
                         {\'a}gua e oxig{\^e}nio, ou seja, n{\~a}o causam impactos ao 
                         meio ambiente e {\`a} sa{\'u}de humana. Buscando agregar 
                         aspectos inovadores que possam melhorar a atividade dos 
                         catalisadores empregados na decomposi{\c{c}}{\~a}o do H2O2, o 
                         presente trabalho tem como objetivos, sintetizar uma alumina 
                         modificada, adicionando um elemento dopante, sil{\'{\i}}cio ou 
                         boro, durante a etapa de forma{\c{c}}{\~a}o do hidr{\'o}xido de 
                         alum{\'{\i}}nio, a fim de melhor as caracter{\'{\i}}sticas 
                         texturais, mec{\^a}nicas e t{\'e}rmicas da alumina. O 
                         hidr{\'o}xido precursor contendo o dopante sil{\'{\i}}cio 
                         resultou na forma{\c{c}}{\~a}o da fase cristalina boemita e, 
                         ap{\'o}s calcina{\c{c}}{\~a}o, da fase cristalina gama-alumina 
                         com elevados valores de {\'a}rea e volume de poros. A 
                         obten{\c{c}}{\~a}o de aluminas moldadas envolveu uma etapa de 
                         dispers{\~a}o das part{\'{\i}}culas, denominada de 
                         peptiza{\c{c}}{\~a}o, realizada com aux{\'{\i}}lio de agentes 
                         qu{\'{\i}}micos, etapa fundamental para a gera{\c{c}}{\~a}o de 
                         pellets com elevada resist{\^e}ncia mec{\^a}nica. Foram 
                         realizados dois tipos de processos, o convencional, denominado de 
                         peptiza{\c{c}}{\~a}o incipiente, e o alternativo, visando 
                         melhorar a resist{\^e}ncia mec{\^a}nica, denominado de 
                         peptiza{\c{c}}{\~a}o em excesso. Os pellets de hidr{\'o}xido de 
                         alum{\'{\i}}nio (antes da calcina{\c{c}}{\~a}o) e alumina 
                         (ap{\'o}s calcina{\c{c}}{\~a}o) modificados com 
                         sil{\'{\i}}cio ou boro foram submetidos {\`a} etapa de 
                         esferoidiza{\c{c}}{\~a}o, pelo m{\'e}todo de 
                         fluidiza{\c{c}}{\~a}o com ar, para obten{\c{c}}{\~a}o de 
                         part{\'{\i}}culas esferoidais, formato empregado no catalisador 
                         comercial Shell 405. O hidr{\'o}xido de alum{\'{\i}}nio 
                         contendo sil{\'{\i}}cio resultou nas part{\'{\i}}culas 
                         esferoidais com melhor rendimento. Catalisadores foram preparados 
                         contendo como fase ativa os metais, o mangan{\^e}s, o cobalto, o 
                         bismuto, o n{\'{\i}}quel e o molibd{\^e}nio. Esses metais 
                         selecionados s{\~a}o considerados mais ativos por serem 
                         c{\'a}tions de metais de transi{\c{c}}{\~a}o. Foram preparados 
                         catalisadores m{\'a}ssicos para avalia{\c{c}}{\~a}o nos testes 
                         de gota e de bancada, e catalisadores suportados na alumina 
                         contendo sil{\'{\i}}cio para avalia{\c{c}}{\~a}o no 
                         micropropulsor. Com rela{\c{c}}{\~a}o {\`a} 
                         impregna{\c{c}}{\~a}o do suporte com a fase ativa, empregou-se 
                         dois procedimentos, um tradicional, ou seja, solubilizando os 
                         metais que constituem a fase ativa em meio aquoso, e o outro, 
                         propondo uma t{\'e}cnica inovadora de impregna{\c{c}}{\~a}o, 
                         solubilizando-os em meio org{\^a}nico, denominada processo 
                         poliol. Os materiais preparados foram caracterizados pelas 
                         t{\'e}cnicas de volumetria de nitrog{\^e}nio (BET), 
                         difratometria de raios X (DRX), termogravimetria (TG), 
                         resist{\^e}ncia mec{\^a}nica por compress{\~a}o individual, 
                         densidade real (DR). Os catalisadores m{\'a}ssicos foram 
                         pr{\'e}avaliados atrav{\'e}s do teste de gota (drop test), com o 
                         gotejamento de H2O2 na superf{\'{\i}}cie do catalisador, com o 
                         objetivo de verificar a atividade do material na 
                         decomposi{\c{c}}{\~a}o do H2O2, associando essa atividade ao 
                         volume dos gases liberados em fun{\c{c}}{\~a}o do tempo. De 
                         forma qualitativa, inicialmente os testes foram monitorados por 
                         uma c{\^a}mera fotogr{\'a}fica de alta velocidade. Foi 
                         desenvolvido um teste de bancada capaz de estimar, de forma 
                         simples e r{\'a}pida, a atividade de catalisadores frente {\`a} 
                         rea{\c{c}}{\~a}o de decomposi{\c{c}}{\~a}o do H2O2 de forma 
                         quantitativa. O melhor catalisador, ou seja, o mais ativo, nos 
                         testes de bancada, contendo a fase ativa mangan{\^e}s-cobalto, 
                         foi selecionado para avalia{\c{c}}{\~a}o em testes de bancada em 
                         um sistema micropropulsivo equipado com um propulsor de 2N, que 
                         indicaram que o catalisador suportado na alumina com 
                         sil{\'{\i}}cio e preparado pelo novo m{\'e}todo, poliol, 
                         resultou em valores superiores de empuxo e press{\~a}o de 
                         c{\^a}mera. ABSTRACT: After several decades of hydrazine 
                         dominance as a propellant for satellite propellants, its use began 
                         to be questioned due to its danger to human health and the 
                         environment. One of the alternatives to hydrazine is the use of 
                         hydrogen peroxide (H2O2), a monopropellant classified as being 
                         green, since its decomposition generates the chemical compounds 
                         water and oxygen, that is, it does not cause impacts to the 
                         environment and human health. . Seeking to add innovative aspects 
                         that can improve the activity of catalysts used in the 
                         decomposition of H2O2, the present work aims to synthesize a 
                         modified alumina, adding a dopant element, silicon or boron, 
                         during the aluminum hydroxide formation step, in order to better 
                         the textural, mechanical and thermal characteristics of alumina. 
                         The precursor hydroxide containing the silicon dopant resulted in 
                         the formation of the boehmite crystalline phase and, after 
                         calcination, of the gamma-alumina crystalline phase with high 
                         values of pore area and volume. Obtaining molded alumina involved 
                         a particle dispersion step, called peptization, carried out with 
                         the aid of chemical agents, a fundamental step for the generation 
                         of pellets with high mechanical strength. Two types of processes 
                         were carried out, the conventional one, called incipient 
                         peptization, and the alternative, aiming to improve the mechanical 
                         resistance, called excess peptization. The aluminum hydroxide 
                         pellets (before calcination) and alumina (after calcination) 
                         modified with silicon or boron were subjected to the 
                         spheroidization step, by the air fluidization method, to obtain 
                         spheroidal particles, a format used in the commercial catalyst 
                         Shell 405. Aluminum hydroxide containing silicon resulted in the 
                         spheroidal particles with the best yield. Catalysts were prepared 
                         containing as active phase the metals, manganese, cobalt, bismuth, 
                         nickel and molybdenum. These selected metals are considered more 
                         active because they are transition metal cations. Mass catalysts 
                         were prepared for evaluation in the drop and bench tests, and 
                         catalysts supported on alumina containing silicon for evaluation 
                         in the micropropeller. Regarding the impregnation of the support 
                         with the active phase, two procedures were used, one traditional, 
                         that is, solubilizing the metals that constitute the active phase 
                         in an aqueous medium, and the other, proposing an innovative 
                         technique of impregnation, solubilizing them in water. organic 
                         medium, called polyol process. The prepared materials were 
                         characterized by the techniques of nitrogen volumetry (BET), X-ray 
                         diffraction (XRD), thermogravimetry (TG), mechanical strength by 
                         individual compression, real density (DR). The mass catalysts were 
                         pre-evaluated through the drop test, with the dripping of H2O2 on 
                         the surface of the catalyst, with the objective of verifying the 
                         activity of the material in the decomposition of the H2O2, 
                         associating this activity with the volume of gases released in 
                         time function. Qualitatively, initially the tests were monitored 
                         by a high-speed camera. A bench test was developed capable of 
                         estimating, in a simple and fast way, the activity of catalysts 
                         against the decomposition reaction of H2O2 in a quantitative way. 
                         The best catalyst, that is, the most active, in the bench tests, 
                         containing the manganese-cobalt active phase, was selected for 
                         evaluation in bench tests in a micropropulsive system equipped 
                         with a 2N propellant, which indicated that the catalyst supported 
                         in the alumina with silicon and prepared by the new method, 
                         polyol, resulted in superior values of thrust and chamber 
                         pressure.",
            committee = "Rodrigues, Jos{\'e} Augusto Jorge (orientador/presidente) and 
                         Nono, Maria do Carmo de Andrade (orientadora) and Machado, 
                         Jo{\~a}o Paulo Barros and Silva, Adriana Maria da and Oliveira, 
                         Ivone Regina de and Cruz, Gilberto Marques da",
         englishtitle = "Catalyst supported on aluminas doped for decomposition of hydrogen 
                         peroxide in satellite propellers",
             language = "pt",
                pages = "145",
                  ibi = "8JMKD3MGP3W34T/47GU3DB",
                  url = "http://urlib.net/ibi/8JMKD3MGP3W34T/47GU3DB",
           targetfile = "publicacao.pdf",
        urlaccessdate = "21 maio 2024"
}


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