Navegando por Autor "SANTOS, Wenderson Gomes dos"

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Craqueamento termocatalítico do óleo de fritura residual
(Universidade Federal do Pará, 2013-06-20) SANTOS, Wenderson Gomes dos; MACHADO, Nelio Teixeira; http://lattes.cnpq.br/5698208558551065; BORGES, Luiz Eduardo Pizarro; http://lattes.cnpq.br/8756886156388456
This paper studied the cracking process termocatalítico the frying oil in bench and pilot scales, varying the percentage of sodium carbonate catalyst 5 and 10% m / m of raw material used and temperature of 440 º C. The objective was to obtain hydrocarbon mixtures rich in diesel fraction. The frying oil was neutralized and dried characterized in relation to the Acid Value, Saponification, Viscosity, Density and Refractive Index. After cracking, the liquid product obtained was purified by decanting the aqueous phase and simple filtration bench scale. This product was fractionated by fractional distillation and condensate were collected in a separating funnel according to the distillation range of gasoline (40ºC-175ºC), kerosene (175ºC-235ºC), light diesel (235°C-305°C) and heavy diesel (305°C-400°C). Were characterized both physical as chemical composition of the liquid products and their fractions. We also carried out the evolution of the cracking process in pilot scale, with the behavior of physical characteristics and chemical composition of the product formed during the cracking process. The results showed that the catalyst sodium carbonate supplied products of low acidity and good characteristics for use as fuel. The variation in the percentage of catalyst significantly influences the physical and chemical composition of both the product and its fractions. It was found also that the cracking termocatalítico the frying oil promotes the formation of hydrocarbons in rich fraction of diesel (19.16% and 41.18% light diesel heavy diesel to the test with 10% Na2CO3 and 13, 53% light and heavy diesel 52.73% for the test with 5% Na2CO3 ). The time intervals generate the final cracking fuel with low acid content and physicochemical properties according to the specified standard mineral diesel.
Acesso aberto (Open Access)
Estudo do processo de produção de bio-combustíveis via pirólise de resíduos de pneus
(Universidade Federal do Pará, 2019-10-24) SANTOS, Wenderson Gomes dos; DUVOISIN JÚNIOR, Sérgio; http://lattes.cnpq.br/1737235899259374; MACHADO, Nélio Teixeira; http://lattes.cnpq.br/5698208558551065
In this study, the pyrolysis process of waste tires was analyzed in the laboratory and pilot scales. In the lower scale, the temperature variation, the type of catalyst commercially obtained (CaCO3, Na2CO3 and Ca(OH)2), the type of catalyst synthesized / treated from industrial waste (LV 1M HCl, LV 2M HCl and zeolite of kaolin) and the concentration of the NaOH solution impregnated into the tire (0.5, 1 and 2M) in the yields and compositions of the tire pyrolysis oil (TPO). In the larger scale, the evolution of the physicochemical and compositional properties of the TPO’s during the thermal cracking process (T = 400 °C, T = 450 °C and T = 500 °C) was evaluated in order to obtain a liquid product with characteristics of fossil fuels and / or compounds of high commercial value. The results showed that the yield of the TPO's are influenced by the increase in process temperature, by the type of catalyst and by the chemical treatment in the raw material. Being the process at 500 °C and with kaolin zeolite as the catalyst which most optimized the process for the yield and production of aliphatic compounds in the TPO. The use of catalysts led to the reduction of aromatic compounds and sulfur compounds in the liquid fraction. On the smaller scale, the behavior of the aliphatic compounds in thermocatalytic processes and chemical impregnation of the raw material was strongly influenced by the composition of d-limonene in the oils of pyrolysis of tires. The results of the pilot scale allowed us to conclude that there were variations in the physicochemical and rheological properties during the cracking process, but tend to stabilize in 65 minutes of process, presenting low acidity and low viscosity. The main substances identified throughout the process were d-limonene, BTX (benzene, toluene and xylenes) and cymenes. In the fractionation of TPO’s, the fraction of gasoline (C8 to C10) and kerosene (C8 to C17) are essentially hydrocarbons, while light diesel (C15 to C21) and heavy diesel (C17 to C23) by heteroaromatics. It is also concluded that sulfur and halogen compounds tend to be separated from the light diesel range.