Vol.:(0123456789) 1 3
Bioprocess and Biosystems Engineering
https://doi.org/10.1007/s00449-019-02257-9
RESEARCH PAPER
Synthesis of 2‑ethylhexyl oleate catalyzed by Candida antarctica lipase
immobilized on a magnetic polymer support in continuous fow
Mateus V. C. da Silva
1
· Amanda B. Souza
1
· Heizir F. de Castro
1
· Leandro G. Aguiar
1
· Pedro C. de Oliveira
1
·
Larissa de Freitas
1
Received: 23 August 2019 / Accepted: 15 November 2019
© Springer-Verlag GmbH Germany, part of Springer Nature 2019
Abstract
This study investigated the synthesis of 2-ethylhexyl oleate catalyzed by Candida antarctica lipase immobilized on magnetic
poly(styrene-co-divinylbenzene) particles in a continuous packed-bed bioreactor. Runs were carried out in a solvent-free
system at 50 °C. The performance of the reactor was evaluated for substrates composed by oleic acid and 2-ethylhexanol
at fve molar ratios (1:4–4:1), determining its operation limits in terms of substrate fow rate. The system performance was
quantifed for three diferent fow rates corresponding to space-time between 3 and 12 h. For each condition, the infuence
of the space-time in the ester formation, esterifcation yield and productivity was determined. The molar ratio of acid-to-
alcohol interfered, in a remarkable way, in the formation of 2-ethylhexyl oleate and the best performance was attained for
substrate at equimolar ratio running at 12 h space-time. Under this condition, average 2-ethylhexyl oleate concentration was
471.65 ± 2.98 g L
−1
which corresponded to ester productivity of 23.16 ± 0.49 mmol g
−1
L
−1
h
−1
. This strategy also gave high
biocatalyst operational stability, revealing a half-life time of 2063 h. A model based on the ping-pong Bi–Bi mechanism was
developed to describe the kinetics of the esterifcation reaction and validated using experimental data. The goodness of ft
of the model was satisfactory (R
2
= 0.9310–0.9952).
Keywords Kinetic modeling · Esterifcation · Immobilized lipase · Magnetic polymer · Packed-bed reactor
Introduction
Emollient esters are widely used as skin softening and
moisturizing agents in creams, lotions, sunscreen products,
makeup, and antiperspirants. These components are biode-
gradable, non-toxic, and have good solubility in oils and fats
[1]. 2-Ethylhexyl oleate is an example of a commercially
important ester with applications in the cosmetics, pharma-
ceutical, food, and chemical industries [2, 3].
Currently, the vast majority of emollient esters used
in cosmetics are derived from petroleum. However, envi-
ronmentally conscious consumers have created a growing
demand for high-quality, high-purity ingredients obtained
from renewable sources, preferably through clean and sus-
tainable technologies and in accordance with local and inter-
national regulations [4, 5]. These changes necessitate the
development of novel methods to obtain emollient esters.
Lipases efectively catalyze hydrolysis, esterifcation,
interesterifcation, and transesterifcation reactions. Their
chemo-, regio-, and stereospecifcity make them promising
catalysts for the synthesis of products of commercial inter-
est. Furthermore, lipases can synthesize high-purity products
under mild pressure and temperature conditions, facilitating
purifcation steps and reducing the amount of energy spent
in the process. However, in their free form, lipases have
some disadvantages; they are difcult to recover, insoluble
in some media, and unstable in organic solvents in certain
pH and temperature ranges [6]. Enzyme immobilization has
been applied to overcome these difculties. This technique
improves the stability of enzymes to heat and extreme pH
conditions and allows their recovery, thereby reducing the
cost of enzymatic processes [7].
Electronic supplementary material The online version of this
article (https://doi.org/10.1007/s00449-019-02257-9) contains
supplementary material, which is available to authorized users.
* Larissa de Freitas
larissafreitas@usp.br
1
Department of Chemical Engineering, Engineering School
of Lorena, University of São Paulo, Lorena, SP 12602-810,
Brazil