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Mathematical Modeling of Biodiesel Production under Intense Agitation

  • Aliakbar Roosta EMAIL logo , Jafar Javanmardi and Elham Sadat Behineh
Published/Copyright: October 15, 2015

Abstract

In this study, a new approach is proposed to investigate the kinetics of sunflower oil and rapeseed oil transesterification in the presence of potassium hydroxide. Transesterification is a heterogeneous process which affected by a number of parameters, that are not readily available in the literature, such as mass transfer coefficients, partition coefficients, and specific surface area of the dispersed phase. However, under intense agitation condition, mass transfer restrictions may be neglected, and the two phases are supposed to remain in thermodynamic equilibrium, during the process. Therefore, a model was developed independent of the mass transfer coefficient and specific surface area, which is reliable for the intense agitation condition. According to the results, the model is valid at least for mixing rates over 500 rpm. The results of the model were used to study the effects of temperature, methanol-to-oil ratio, and catalyst concentration on the biodiesel conversion. Biodiesel production rate increases with increasing temperature, although rapeseed oil transesterification is more temperature dependent. The results show that the maximum amount of catalyst concentration is less than 1% (by weight); however, the optimum value depends on the operating temperature. The optimum value of the methanol-to-oil-ratio decreases with increasing temperature. Thus, at higher temperatures, less amount of methanol and catalyst are required, which leads to easier purification of biodiesel.

Nomenclature

Aj

frequency factor of Arrhenius equation (L mol−1 min−1)

C

concentration (mol L−1)

Ea

activation energy (kJ mol−1)

kj

reaction rate constant of reaction j (L mol−1 min−1)

R

gas constant (kJ mol−1 K−1)

T

temperature (K)

t

time (min)

øi

partition coefficient of component i

Abbreviation
A

alcohol

AAD

average absolute deviation

DG

diglyceride

E

ester

FAME

fatty acid methyl ester

G

glycerol

LLE

liquid liquid equilibrium

MeOH

methanol

MG

monoglyceride

TG

triglyceride

Subscription
o

oil phase

m

methanol phase

References

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Published Online: 2015-10-15
Published in Print: 2016-2-1

©2016 by De Gruyter

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