Tesis
Produção de biodiesel etílico via catálise ácida em reator de fluxo contínuo com indução simultânea de ultrassom e microondas
Fecha
2015-10-28Registro en:
RAMOS, Ghieska Tieppo Souza. Produção de biodiesel etílico via catálise ácida em reator de fluxo contínuo com indução simultânea de ultrassom e microondas. 2015. 167 f. Dissertação (Mestrado em Química) - Universidade Federal de Mato Grosso, Instituto de Ciências Exatas e da Terra, Cuiabá, 2015.
Autor
Dall’Oglio, Evandro Luiz
http://lattes.cnpq.br/0288804659104012
Dall’Oglio, Evandro Luiz
589.765.079-91
http://lattes.cnpq.br/0288804659104012
Souza, Gabriel Luiz Cruz de
.
http://lattes.cnpq.br/2821352329397835
589.765.079-91
Kuhnen, Carlos Alberto
.
http://lattes.cnpq.br/3047763427167672
Institución
Resumen
Continuing development of a new technology for
the production of biodiesel ethyl, studies have been
focused on the use of microwave and ultrasound, as
contrary to the conventional method, where the methyl
route has a higher reaction kinetics compared to ethyl
route, reactions by microwave-assisted homogeneous
acid catalysis in ethyl route gives better results than the
methyl route. Thus, this work has perfected a monomode
prototype machined stainless steel 316L continuous flow
system, operating respectively at 2.45 GHz and 24 kHz for
the production of biodiesel ethyl assisted by microwave
and ultrasound simultaneously. In both cases the physical
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principles involved in the ways of wave propagation as
well, and the chemical characteristics of the reaction
medium aiming to maximize the effect of the wave material
interaction. Also, the prototype was combined with a
Programmed Logic Control (PLC) for control of valves
generating the microwave (magnetrons) allowing a mode
of operation continues and to seek more efficient. The use
of simultaneous ultrasonic aims at improving the
homogeneity of the reaction mixture and solve a problem
observed in earlier studies that it is the phase separation
of glycerin and biodiesel after conversion exceeding 80%,
which causes a decrease in catalytic activity of the acid
catalyst by removal of the oily phase, as well as allowing
the emergence of side reactions such as degradation of
glycerin. In the prototype, they were tested via reactions
with ethyl route soybean oil and sulfuric acid as a catalyst.
We evaluated the biodiesel conversion percentage as a
function of the power of microwave and ultrasound flow of
the reaction mixture, the proportion of catalyst in relation
to the total volume of the reactants and the molar ratio of
oil / alcohol. The percentage of biodiesel oil conversion
were determined according to standard EN 104103 by gas
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chromatography with flame ionization detection (GC /
FID).