Submitted by Automa??o e Estat?stica (sst@bczm.ufrn.br) on 2016-02-22T21:48:48Z No. of bitstreams: 1 CarlosAntonioDeAlbuquerquePinheiro_DISSERT.pdf: 22871335 bytes, checksum: ce4b9e60852cadad85bb17326e4f1ca4 (MD5) / Approved for entry into archive by Arlan Eloi Leite Silva (eloihistoriador@yahoo.com.br) on 2016-02-23T23:43:04Z (GMT) No. of bitstreams: 1 CarlosAntonioDeAlbuquerquePinheiro_DISSERT.pdf: 22871335 bytes, checksum: ce4b9e60852cadad85bb17326e4f1ca4 (MD5) / Made available in DSpace on 2016-02-23T23:43:04Z (GMT). No. of bitstreams: 1 CarlosAntonioDeAlbuquerquePinheiro_DISSERT.pdf: 22871335 bytes, checksum: ce4b9e60852cadad85bb17326e4f1ca4 (MD5) Previous issue date: 2014-09-25 / Este trabalho descreve a s?ntese e aplica??o de catalisadores de ferro homog?neos e heterogeneizados na rea??o de alquila??o do tolueno com propeno, empregando planejamento de experimentos. O complexo homog?neo foi obtido atrav?s da s?ntese do ligante org?nico seguida da complexa??o de cloreto de ferro(II). Quanto aos complexos heterogeneizados, inicialmente foram sintetizados suportes inorg?nicos (SBA-15, MCM-41 e Al-MCM41). Em seguida sintetizou-se novamente o ligante org?nico, que atrav?s de funcionaliza??o com o cloropropiltrimetoxisilano (CPTMS), foi ancorado ao suporte previamente calcinado. A estes ligantes ancorados, foi complexado cloreto de ferro(II), previamente solubilizado em tetrahidrofurano (THF). A caracteriza??o do ligante org?nico foi realizada atrav?s de resson?ncia magn?tica nuclear (RMN) e espectroscopia na regi?o do infravermelho (IV). Os suportes foram caracterizados por difra??o de raios-x (DRX), an?lises texturais por adsor??o/dessor??o de nitrog?nio (antes e depois do ancoramento), an?lise de termogravimetria (TG) e espectroscopia na regi?o do infravermelho (IV). A quantidade de metal foi quantificado atrav?s de espectrofotometria de absor??o at?mica (AAS). Os complexos foram testados em rea??es catal?ticas empregando-se sesquicloreto de etilalum?- nio (EASC) como co-catalisador, respons?vel pela ativa??o do complexo catal?tico, em reator de a?o, sob agita??o mec?nica. As condi??es reacionais variaram entre 4 e 36 ?C, para diversas raz?es alum?nio/ferro, sempre sob 6 atmosferas de press?o de propeno e com 30 minutos de tempo reacional. Os produtos das rea??es catal?ticas foram analisados atrav?s de cromatografia gasosa (CG). Os catalisadores se mostraram ativos tanto em meio homog?neo como heterogeneizados nos suportes. O complexo catal?tico homog?neo apresentou frequ?ncia de rota??o (FR) de at? 8,63 ?103 ? h ?1 , enquanto que, em algumas condi??es, os complexos ancorados apresentaram melhores resultados, com FR de at? 8,08 ?103 ? h ?1 . Adicionalmente, foi poss?vel determinar uma equa??o, para o sistema homog?neo, que relaciona a quantidade de produto em fun??o da temperatura reacional e da raz?o alum?nio/ferro. / This work describes the synthesis and aplication of homogeneous and heterogenized iron catalysts in the alkylation reaction of toluene with propene, empolying experimental design. The homogenous complex was obtained trough the synthesis of the organic ligand folowed by the complexation of the iron(II) chloride. As to the heterogenized complexes, first were synthetized the inorganic supports (SBA-15, MCM-41 and Al-MCM-41). Then, it was synthetized the ligand again, that through funcionalization with chloropropyltrimethoxysilane (CPTMS), was anchored on the support previously calcinated. To these anchored ligands, was complexed the iron(II) chloride, previously solubilizated in tetrahydrofuran (THF). The organic ligand characterization was accomplished trough nuclear magnetic resonance (NMR) and Infrared spectroscopy (IV). The supports were characterized with x-ray diffraction (DRX), texture analysis with nitrogen adsorption/desorption (before and after the anchoring), termogravimetric analysis (TG) and infrared (IV). The metalic content was quantified trough the atomic absorption spectrophotometry (AAS). The complexes were tested in catalytic reactions emolying ethylaluminium sesquichloride (EASC) as co-catalyst in steel reactor, under mecanic stirring. The reaction conditions ranged from 4 to 36 ?C, with many aluminum/iron ratios. The catalysts were actives in homogeneous and heterogenized ways. The homogenous catalytic complex showed a maximum turnover frequency (TOF) of 8.63 ?103 ? h ?1 , while, in some conditions, the anchored complexes showed better results, with TOF of until 8.08 ?103 ? h ?1 . Aditionally, it was possible to determine an equation, to the homogenous catalyst, that describes the product quantity in function of reacional temperature and aluminum/iron ratio.