Catalisadores Cu/Al2O3 promovidos com Co e Zn aplicados à gaseificação de etanol em meio contendo água em condições supercríticas

• Ano de defesa: 2018
• Autor(a) principal: Mourão, Lucas Clementino
• Orientador(a): Alonso, Christian Gonçalves
• Banca de defesa: Oliveira, Sérgio Botelho de, Colmati Júnior, Flávio
• Tipo de documento: Dissertação
• Tipo de acesso: Acesso aberto
• Idioma: por
• Instituição de defesa: Universidade Federal de Goiás
• Programa de Pós-Graduação: Programa de Pós-graduação em Química (IQ)
• Departamento: Instituto de Química - IQ (RG)
• País: Brasil
• Palavras-chave em Português: Gaseificação de biomassa com água supercrítica; Gaseificação de biomassa; Etanol; Catálise heterogênea; Produção de hidrogênio
• Palavras-chave em Inglês: Biomass gasification with supercritical water; Biomass gasification; Ethanol; Heterogeneous catalysis; Hydrogen production
• Área do conhecimento CNPq: CIENCIAS EXATAS E DA TERRA::QUIMICA
• Link de acesso: http://repositorio.bc.ufg.br/tede/handle/tede/8837

The great environmental concern, coupled with the risk of depletion of non-renewable raw material, has driven the search for new sustainable technologies with major concern to the reduction of pollutant emissions. Hydrogen, a chemical of enormous importance to industrial plants, stands out as a clean and renewable energy source. This chemical is commonly produced from non-renewable sources, such as natural gas reforming. Due to specific reaction conditions, the supercritical water gasification of wet biomass is a promising way for the production of hydrogen and others high added value fuel gases. Ethanol is an attractive material because it is renewable, has low toxicity compared to other resources and has high hydrogen content in its molecule. In order to become this technology viable, a decisive point is the development of a catalyst aiming at cost reductions and high selectivity to the products of interest. In this work, ethanol gasification was carried out in supercritical water with heterogeneous catalysts. The tests were performed on an Inconel Alloy 625 tubular reactor under the following operating conditions: temperatures of 400, 450, 500, 550, 600 and 650 ºC, pressure of 250 bar, 5 g loading of heterogeneous catalyst, reactor feed: ethanol/water molar ratio of 1:10 and mass flow rate of 5 g/min. The catalysts were synthesized by wet impregnation method using aqueous solutions of Cu, Co and Zn nitrates as precursors for the active phase and spherical pellets of Al 2 O 3 as catalytic support. The catalysts and the catalytic support were characterized by Thermogravimetry and Differential Thermal Analysis (TG/DTA), X-Ray Fluorescence (XRF), Scanning Electron Microscopy (SEM), textural analysis by Adsorption/Desorption Isotherms of N 2 at 77 K and X-Ray Diffraction (XRD). The gasification results indicated that H 2 production was mainly due to ethanol dehydrogenation. The catalysts showed higher conversions than observed for catalytic support only. The CuAl catalyst showed higher H 2 selectivity as well as higher H 2 molar flow at 650 °C. The CoZnAl catalyst showed a high tendency for C 2 H 4 formation at any reaction temperature, especially at 650 °C.