Navegando por Assunto "Craqueamento catalítico"

Agora exibindo 1 - 4 de 4

Acesso aberto (Open Access)
Estudo da aplicação da lama vermelha como catalisador na reação de craqueamento térmico catalítico de resíduos de caixas de gordura
(Universidade Federal do Pará, 2015-07-02) EID, Janaina Guedes; BORGES, Luiz Eduardo Pizarro; http://lattes.cnpq.br/8756886156388456; MACHADO, Nelio Teixeira; http://lattes.cnpq.br/5698208558551065
This study aimed to evaluate the use of residual fat taken from retaining grease traps as an alternative raw material in the biofuel production process. The catalytic process of thermal cracking of the residual fat was carried out in bench scale and pilot using the red mud (LV) calcined at 1000 ° C as catalyst at different concentrations (5%, 10% and 15%). Organic liquids (PLO's) obtained in the cracking experiments were distilled in a bench unit, which was the production of hydrocarbon fractions in bands of light green diesel and heavy green diesel. Thus, PLO'se fractions were characterized by carrying out physicochemical and compositional analysis where the results turned out to be compared according to the specifications established by the standard of ANP No. 65 for diesel S10. The produced in the PLO counter and cracking unit using the pilot content of 5% catalyst (LV calcined at 1000 ° C) when compared with experiments using concentrations of 10% and 15% of LV showed the best results for the acid value, kinematic viscosity and density, confirming that this experiment had one of the best yields of the process and significant results regarding the physicochemical and compositional analysis. Distillation processes of the PLO's done in the distillation unit in Bench Scale showed good yields for hydrocarbon fractions in heavy green diesel range. The heavy green diesel fractions obtained after distillation of the PLO produced with 5% catalyst content showed significant yield and the best physicochemical results of all fractions obtained in this study, especially with regard to the acid value. It was confirmed through analysis of the Infrared, nuclear magnetic resonance, and gas chromatography coupled to a mass spectrometer the presence of hydrocarbons in the composition of the organic liquids.
Acesso aberto (Open Access)
Estudo do processo de craqueamento termocatalítico da borra de neutralização do óleo de palma para produção de biocombustível
(Universidade Federal do Pará, 2015-04-17) SANTOS, Marcelo Costa; BORGES, Luiz Eduardo Pizarro; http://lattes.cnpq.br/8756886156388456; MACHADO, Nélio Teixeira; http://lattes.cnpq.br/5698208558551065
The Soap phase residue derived from refining vegetable oils are agro-industrial residues obtained after the neutralization stage of vegetable oils, which are aggregate low-value material, in addition to being an environmental liability for agribusiness thus is becoming increasingly attractive the use of these residues as raw material for generation bio-fuels. This work studies the neutralization sludge of palm oil as an alternative raw material, from the point of view, economic and environmental to the process of catalytic and Thermic-catalytic cracking. Initially were carried experiments of Thermic and catalytic cracking of the neutralization sludge and palm oil (in one reactor) and catalytic tests (the second reactor coupled in the first decarboxylation) both in bench scale; experiments were perfomed of the thermic-catalytic and catalytic (only in semi-pilot scale) of the neutralization sludge in the semi-pilot and pilot scale using different types of catalysts (Na2CO3, CaCO3, activated alumina, zeolite HY, HZSM-5, and FCC). The organic liquid product (OLP) obtained and the fractions obtained from the distillation in bench and pilot scale were characterized and compared with the current standard. The results obtained in laboratory scale have shown that the activated alumina catalyst provided the highest yield in wet basis (83.70%), with palm oil as raw material, however, the bio-fuel obtained Na2CO3 had a better quality how much the physicochemical characteristics. . In the semi-pilot scale, the highest yield was the thermal experiment of the sludge (78.36%), followed by the experiment with 5% activated alumina (71.47%), but the use of Na2CO3 showed better quality in the how much the physicochemical characteristics.The experiments in the pilot scale showed the highest yield (71%) obtained with 15% Na2CO3 at a temperature of 440 ° C. The results of the chromatographic analysis of this OLP obtained in the pilot scale confirmed that the percentage increase in the catalyst enabled the formation of a OLP rich in hydrocarbonate (91.22%) containing aliphatic, olefinic, naphthenic, aromatic and low amounts of oxygenates (8 , 78%). While in the distillation of PLO of the Experiment 5 makes possible to get fractions rich in hydrocarbons and without oxygenates compounds.
Acesso aberto (Open Access)
Estudo do processo de craqueamento termocatalítico do óleo de palma (Elaeis guineensis) com lama vermelha calcinada e alumina ativada em reatores de bancada e batelada
(Universidade Federal do Pará, 2015-05-29) LOURENÇO, Rafael Martins; BORGES, Luiz Eduardo Pizarro; http://lattes.cnpq.br/8756886156388456; MACHADO, Nelio Teixeira; http://lattes.cnpq.br/5698208558551065
In the present work was to study the thermal catalytic cracking process palm oil for biofuel production. In the development of this study were performed in crackings Bench and Semipilot. Initially, basic catalysts in cracking tests were performed (Red Mud; Red Mud Calcined at 550 ° C; Red Mud Calcined at 800C; Red Mud Calcined at 1000 ° C; Activated Alumina (AA) with NaOH 20% solution and Activated Alumina (AA) NaOH solution 30%) and acid (not activated alumina) in bench scale using as raw palm oil. Before the mentioned catalysts are used in thermal catalytics crackings, they were subjected to the following tests: Fourier Transform Infrared (FT-IR); Scanning Electron Microscopy (SEM); X-ray Diffraction (XRD) and BET in order to characterize them. The results of the bench scale showed that the cracked products Gross (PCB's) achieved in thermal catalytics oil crackings using as a catalyst 15% Red Mud Calcined at 800 ° C and 15% AA by NaOH 20% solution, had a significant reduction in their Acidity Index (IA's) compared to the IA's of heat and thermal catalytics crackings used with other catalysts. In Semipilot Scale the thermal catalytics crackings were developed with the best results obtained, Bench Scale, between the Red Mud’s Calcined or not in different concentrations (15% of Red Mud Calcined 800 ° C) and between the Activated Aluminas or not at various concentrations (AA with 15% NaOH solution at 20%) compared to IA's, in addition to the thermal cracking which was also reproduced on the scale. Some of the products obtained in Semipilot Scale was submitted to distillation in Bench Scale to obtain fractions corresponding to the tracks: gasoline, kerosene, light diesel and heavy diesel. The RMN analysis of 13C, held on the heat crackings and diesel thermal catalytic with 15% Red Mud Calcined at 800 °C proves that they are basically formed from long chain fatty acids. Moreover, the GC-MS performed in the cut of gasoline range (40 °C- 175 °C) showed that the three gasolines analyzed showed the formation of paraffinic hydrocarbons, olefinic and naphthenic.
Acesso aberto (Open Access)
Produção de biocombustíveis em diferentes escalas via craqueamento térmico catalítico de resíduos de caixa de gordura com catalisador Na2CO3
(Universidade Federal do Pará, 2015-07-03) CORRÊA, Onésimo Amorim; BORGES, Luiz Eduardo Pizarro; http://lattes.cnpq.br/8756886156388456; MACHADO, Nelio Teixeira; http://lattes.cnpq.br/5698208558551065
This paper presents the residual fat taken from retaining grease traps as a potential feedstock for the production of alternative and renewable fuels. The residual oil was used as filler in experiments catalytic thermal cracking countertop units, Semi-pilot and pilot. Different levels of sodium carbonate (5%, 10% and 15%) were used as a catalyst in the catalytic thermal craqueamneto experiments. Organic liquids (PLO's) obtained in the cracking experiments were distilled in distillation units in bench and pilot scale. Distillation processes resulted in the development of hydrocarbon fractions in kerosene bands, light and heavy diesel. The PLO's with the green light and heavy diesel fractions were characterized according to the specifications established by the standard of ANP 65 for diesel S10. The green kerosene fractions were characterized according to the specifications established by the standard of ANP 37 for petroleum-based kerosene. The results showed that the PLO's had low values for the acid value, moreover, it was confirmed that the use of different percentages of catalyst ash in the three scales of production contributed to obtaining promising results in terms of yield and physico -chemical and compositional, indicating the efficiency of this basic catalyst. The results also showed that the fractions of green kerosene, heavy and light green diesel had low levels of free fatty acids, significant income and physical and chemical characteristics in line with their respective standards. The experiments using the percentage of 10% sodium carbonate as catalyst showed the highest incomes, lower levels of acidity and the best results of physicochemical and compositional characterization of all the tests in this study. The PLO produced using the level of 10% of sodium carbonate showed a total of 78.98% of hydrocarbons in the composition, while the green kerosene obtained after distillation of the same PLO showed 92.64% total hydrocarbons in its composition, these results were confirmed by analysis as FT-IR, RMN and GC-MS.