Navegando por Assunto "Craqueamento"

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Acesso aberto (Open Access)
Aplicação de destilados provenientes do bio- óleo de pirólise de resíduos de gordura animal no asfalto diluído de petróleo
(Universidade Federal do Pará, 2024-08-12) VALENTE, Alex Lopes; MACHADO, Nélio Teixeira; http://lattes.cnpq.bhttp://lattes.cnpq.br/1500327307736428r/5698208558551065; https://orcid.org/0009-0002-4461-7611; BERNAR, Lucas Pinto
Waste animal fats (WAF) can be converted into distillate fractions similar to petroleum solvents and used as biofuels or in other applications through pyrolysis and fractional distillation. The distillate fractions from the pyrolysis of triglycerides exhibit adequate viscosity and volatility compared to petroleum-derived fuels but show acid values between 60-140 mg KOH/g, preventing their direct use as biofuels without considerable purification of the distilled fractions. Diluted petroleum asphalt (DPA), used for priming soil in the construction of flexible pavement, requires adequate viscosity, volatility, and penetration, and the distillate fractions from WAF pyrolysis oil can be used as partial or full substitutes for the standard solvent (kerosene) in DPA production. The aim of this study was to test the compliance of DPAs prepared by substituting kerosene with bio-oil fractions from WAF according to DPA standards. First, WAF is obtained from meat waste through the rendering process. Then, WAF is subjected to pyrolysis in a semi-batch fixed-bed reactor (2L), and the resulting bio-oil is fractionally distilled into gasoline, kerosene, and diesel fractions. The pyrolysis process is analyzed concerning the type of reactor used, with a focus on the influence of temperature and reaction time, as well as the distillation profile. The distilled fractions are characterized by density, viscosity, and acid value before being used in the preparation of DPAs by partial and/or total (0-40% by weight) substitution of standard kerosene. The mixtures were tested for kinematic and Saybolt-Furol viscosity, flash point, and penetration, according to road pavement standards. The results showed that the kerosene and diesel fractions from WAF can be adequately used in the preparation of DPAs as a total substitute for the petroleum kerosene typically used.
Acesso aberto (Open Access)
Craqueamento termocatalítico da borra de neutralização do óleo de palma (Elaeis guineensis) em escala piloto
(Universidade Federal do Pará, 2013-06-21) ABREU, Deise Hellen Soares de; MACHADO, Nelio Teixeira; http://lattes.cnpq.br/5698208558551065; BORGES, Luiz Eduardo Pizarro; http://lattes.cnpq.br/8756886156388456
The byproducts of oil refining industries and biodiesel, as the dregs of neutralization are quite extensive and due to their low economic value and purity are a problem for these industries in the culling and disposal, are of fundamental interest for the use of this research reject. Therefore, this work aims to investigate a viable, economic and environmental fate of this byproduct using Termocatalítico Cracking Process of Neutralization Sludge Palm Oil (Elaeis guineensis Jaqc) pilot scale using 5, 10 and 15% sodium carbonate (Na2CO3) as catalyst and final temperatures of 440 ° C and 420 ° C. The sludge was obtained by the neutralization process and subjected to a dehydration and characterized as the catalyst was dried in an oven and characterized in relation to the X-ray diffraction, Thermal Gravimetric Analysis (TGA) and Differential Thermal Analysis (TDA). Five tests were performed in termocatalítico cracking Cracking Pilot Plant (THERMTEK / FEQ / UFPA) which consists in a reactor with mechanical agitation and capacity 125 liters, and the dynamics of the process and distillation of cracking. The organic liquid product (PLO), samples of the dynamics of the process and the distillation fractions were characterized according to each standard required by ANP N°65 and analyzed by IR and NMR. After analysis of the results showed that the efficiency of the process increases with temperature and catalyst and the feedstock provides products of low acidity and good characteristics for use as fuel. By analyzing the thermodynamic realized that some of the process parameters such as viscosity, flash point and density decrease with increasing time and temperature, forming lighter hydrocarbons. Regarding distillation fractions in the heavier tracks resemble diesel oil in most of the parameters required by the ANP Nº 65.
Acesso aberto (Open Access)
Decomposição catalítica do glicerol em fase vapor usando a perovskita cecuxni1-xo3 (x=0;0.25) como precursor catalítico
(Universidade Federal do Pará, 2017-03-09) ESTRADA, Marcial Antonio Fuentes; FRANÇA, Luiz Ferreira de; http://lattes.cnpq.br/6545345391702172; RIBEIRO, Nielson Fernando da Paixão; http://lattes.cnpq.br/0755443458423442
The utilization of the fuels fossils like main source of energy has carried to the generation of countless environmental and economic problems, creating the need of diversification of the energetic matrix. In Brazil, country with vast territorial extension and agroindustry very established stands out the production of biofuels, such as: ethanol and biodiesel. Particularly, the production of biodiesel with the increasing governmental incentives exponentially has its production increased to each year placing Brazil in prominence in the worldwide scene of biofuels. In the process of transesterification of vegetal oils with a primary alcohol, beyond biodiesel, the rude glycerin in a ratio of 10% is generated 11% in volume. The bio refining of the deriving glycerin of the manufacture of biodiesel, becomes the production of biodiesel economically more viable, leading to the formation of products with raised aggregate values. For this reason, the present work has as main objective the valuation of the chain of production of biodiesel for the transformation of glycerol to the products of bigger value added through reaction catalytic decomposition of glycerol using perovskitas of the CeNi1-xCuxO3 type (x=0 and 0,25) as you will catalyze. The gotten results had shown that the use of high temperature (500 °C) favors the gas production of synthesis with approach relation H2/CO of 1, this occur for the strong craqueamento of the molecule of glycerol, At 410 ° C and inert reaction atmosphere, hydroxyacetone (acetol) was the major product exhibiting selectivity in the range of 22-28% depending on the catalyst used. The effect of the addition of hydrogen on the reaction load was investigated and its insertion promoted the hydrogenation of the hydroxyacetone, leading to an increase in selectivity for 1,2-propanediol whose selectivity varied in the range of 4-9% depending on the catalyst.
Acesso aberto (Open Access)
Estudo da obtenção de biocombustíveis a partir da rota tecnológica de craqueamento utilizando carbonato de sódio e lama vermelha como catalisadores
(Universidade Federal do Pará, 2013-12-26) OLIVEIRA, Romero Moreira de; MOTA, Silvio Alex Pereira da; http://lattes.cnpq.br/2688995977218366; MACHADO, Nelio Teixeira; http://lattes.cnpq.br/5698208558551065
In this paper the crude distillation process of the liquid organic product obtained in the catalytic cracking of oil palm (Elaeis guineensis, Jacq) was studied in pilot scale , using the sodium carbonate (Na2CO3) and red mud catalysts by varying the percentage of catalyst in 10% m/m and 15% m/m for the raw material used , an operating temperature of 450ºC in order to obtain fractions of biofuels (bio-gasoline, bio-kerosene and bio-oil) similar to fuels derived from being fixed oil. The catalysts were subjected to a dehydration pre-treatment for 2 hours in an oven at 300°C, subsequently the XRD, IR and TG were performed. Regarding raw materials, physical and chemical analysis, aiming to characterize palm oil were performed. The organic liquid products (PLOs) were subjected to unit operations of separation, decanting and simple filtration bench scale should then be performed physical-chemical and compositional analyzes. The temples were distilled in a Vigreux column six (06) stages, and the condensed fractions were collected according to the ranges of the distillation of gasoline (60ºC - 190ºC) , kerosene (190ºC - 235ºC ) and diesel (235°C - 370°C), later to be characterized. There was a better catalyst efficiency for sodium carbonate 15% w/w as reducing the acid value about 1.7 mgKOH/g , and a conversion of 97% by weight of the oil in PLO was noted also, by increasing the amount of catalyst that favors the obtaining of an end product with better quality. The red mud on the other hand, showed yields of up to 64% m/m products with a low acidity of about 62.90 mgKOH/g, comparing this result with literature data. Based on the final results verified the efficiency of catalysts, the catalyst which sodium carbonate gave products with low acidity and good characteristics for use as fuel.