Submitted by Rodrigo Martins Cruz (rodrigo.cruz@ufvjm.edu.br) on 2015-02-19T13:03:29Z No. of bitstreams: 5 lindomar.pdf: 4197857 bytes, checksum: 529e21e13238b7b71e5ddffb7f4e7b91 (MD5) license_url: 52 bytes, checksum: 3d480ae6c91e310daba2020f8787d6f9 (MD5) license_text: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) license_rdf: 23898 bytes, checksum: e363e809996cf46ada20da1accfcd9c7 (MD5) license.txt: 2111 bytes, checksum: f5c843397da71f5d32b775fd8c4cbf56 (MD5) / Approved for entry into archive by Rodrigo Martins Cruz (rodrigo.cruz@ufvjm.edu.br) on 2015-02-20T09:29:04Z (GMT) No. of bitstreams: 5 lindomar.pdf: 4197857 bytes, checksum: 529e21e13238b7b71e5ddffb7f4e7b91 (MD5) license_url: 52 bytes, checksum: 3d480ae6c91e310daba2020f8787d6f9 (MD5) license_text: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) license_rdf: 23898 bytes, checksum: e363e809996cf46ada20da1accfcd9c7 (MD5) license.txt: 2111 bytes, checksum: f5c843397da71f5d32b775fd8c4cbf56 (MD5) / Made available in DSpace on 2015-02-20T09:29:04Z (GMT). No. of bitstreams: 5 lindomar.pdf: 4197857 bytes, checksum: 529e21e13238b7b71e5ddffb7f4e7b91 (MD5) license_url: 52 bytes, checksum: 3d480ae6c91e310daba2020f8787d6f9 (MD5) license_text: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) license_rdf: 23898 bytes, checksum: e363e809996cf46ada20da1accfcd9c7 (MD5) license.txt: 2111 bytes, checksum: f5c843397da71f5d32b775fd8c4cbf56 (MD5) Previous issue date: 2013-12-17 / Eletrodos constitu?dos de ?-PbO2 foram preparados via eletrodeposi??o, mediante inclus?o dos ?ons Fe3+ e F- na mistura precursora, usando como substratos tela de a?o (ASTM 316) e tecido de carbono, visando a produ??o eletroqu?mica de oz?nio (PEO) em um reator filtro-prensa conduzida na aus?ncia de eletr?lito l?quido. A an?lise das micrografias de MEV para ambos substratos revelaram que em baixas concentra??es dos dopantes houve a forma??o de gr?os bem definidos com uma ?rea superficial uniforme. A an?lise de Raios-X para ambos substratos revelou o desfavorecimento da forma??o da fase ?-PbO2 para a maioria da concentra??o dos dopantes. Estudos cronopotenciom?tricos evidenciaram a estabilidade dos anodos quando sujeitados a intensa evolu??o de gases. Para o eletrodo dopado com 1 mM do ?on Fe3+, a efici?ncia de corrente da PEO foram de 10% e 9,5% com uma velocidade de gera??o de oz?nio de 1,35 g h-1 e 1,40 g h-1 para os substratos de tela de a?o e de tecido de carbono, respectivamente. Os resultados encontrados s?o promissores indicando uma viabilidade do uso desses eletrodos para aplica??o no tratamento de ?gua, por isso, empregou-se o oz?nio produzido eletroquimicamente para tratar ?gua residu?ria proveniente da produ??o de biodiesel na planta piloto da UFVJM. O tratamento oxidativo da ?gua residu?ria foi conduzido num reator em coluna de bolhas via rea??o direta (oz?nio molecular), indireta (radical hidroxila) e mista (O3/HO?) manipulando-se o pH do meio reacional.A caracteriza??o do efluente ozonizado foi efetuada monitorando-se o processo de degrada??o da mat?ria org?nica dissolvida via espectrofotometria. A cin?tica do processo de degrada??o seguiu o modelo de pseudo-primeira ordem. Foi verificado que a constante cin?tica sofre varia??o com o tempo de ozoniza??o revelando, portanto, uma varia??o da recalcitr?ncia com o tempo de rea??o. A demanda de energia requerida no processo de ozoniza??o foi caracterizada por uma energia el?trica por ordem (EEO) de 139 kW h m-3 ordem-1. / Disserta??o (Mestrado) ? Programa de P?s-Gradua??o em Qu?mica, Universidade Federal dos Vales do Jequitinhonha e Mucuri, 2013. / ABSTRACT Electrodes comprised of ?-PbO2 were prepared by electrodeposition, by moans of the inclusion of Fe3+ and F- ions in the precursor mixture, using as substrates steel screen (ASTM 316) and carbon cloth in order to produce ozone in an filter-press electrochemical reactor conducted in the absence of liquid electrolyte. The analysis of SEM micrographs revealed that for both substrates at low dopants concentrations resulted in the formation of well-defined grains with a uniform surface area. X-rays analysis for both substrates showed the inhibition of formation of the ?-PbO2 phase for most of the dopant concentration. Cronopotenciometric studies revealed a good stability of the anodes when they were subjected to the intense gas evolution. For the electrode doped with 1 mM Fe3+, the current efficiency of EOP were 10% and 9.5% for an ozone generation rate of 1.35 g h-1 and 1.40 g h -1 using the steel screen and carbon cloth substrates, respectively. These results are promising, indicating a feasibility of using these electrodes for application in water purification, so the electrochemical ozone produced was applied to treat residuary water obtained from the biodiesel produced in the pilot plant of UFVJM. The oxidative chemical treatment of wastewater was conducted in a bubble column reactor via direct (molecular ozone), indirect (hydroxyl radical) and mixed (O3/HO?) oxidation reaction thrush manipulating the pH of the reaction medium. The characterization of ozonated effluent was assessed by means of monitoring the degradation of the dissolved organic matter using spectrophotometry. The kinetics of the degradation process followed a pseudo-first order model. It was found that the rate constant changes on the ozonation time thus indicating a recalcitrance variation with the reaction time. The energy demand required in the ozonation process was described by an electric energy per order (EEO) of 139 kW h m-3 order-1.