N. Guajardo and P. Domínguez de María
Molecular Catalysis 485 (2020) 110813
Fig. 5. Effect of water content on the conversion in the esterification to obtain
α-MBG. Reaction conditions: 60 °C, 6 h of reaction, 100 mg of biocatalyst (Nov-
Fig. 6. Kinetics of enzymatic esterification to produce α-MBG using Cyrene™as
a reaction media. Reaction conditions: 48 h of reaction, 333 mg of biocatalyst
4
35), 3 mL of reaction volume, 50 mM benzoic acid and 50 mM glycerol.
(Nov-435), 10 mL of reaction volume, molar ratio benzoic acid/ glycerol = 1/
20 and 60 °C. (●) 50 mM benzoic acid; (□) 10 mM benzoic acid.
/
glycerol) the conversion increased by approximately 6 % with respect
to the 50/50 mM ratio (benzoic acid / glycerol). Following classic
premises of an esterification, this may be due to the hygroscopic effect
of glycerol, which might reduce the available water, shifting the es-
terification to the product formation [29]. Nonetheless, in this case
another aspect that may play a role is the (partial) formation of a Cy-
gnet-type solvent between Cyrene and glycerol (see Fig. 1), which
might modify the apparent LogP of the newly solvent phase (Cyrene,
Cyrene geminal diol, Cygnet-glycerol), and would then create a more
hydrophobic media, which could be beneficial for the lipase synthetic
performance. The gradient-like distribution was evidenced by Costa
Pacheco et al. [27], with studies conducted with Cyrene-water mix-
tures. The enzymatic reactive system of our work appears to be more
complicated, as glycerol and benzoic acid are also present.
Triggered by the changes observed in the conversion, the effect of
water was subsequently assessed in the reaction. To this end, different
amounts of phosphate buffer (pH 7) were added to the Cyrene solvent,
in the range of 0–30 % (v/v) (Fig. 5). As depicted in Fig. 5, the reaction
displayed its optimum performance at an addition of 0–2 % phosphate
buffer (v/v) and decreased significantly at higher amounts. Several
aspects may be playing a role in these results. Firstly, the lipase may
need some water to keep its active structure, which would explain why
some water addition is beneficial (Fig. 4). Secondly, Cyrene is hygro-
scopic, and may probably absorb some of the added water, leading to
some geminal-diol solvent system, which may exert some beneficial
effect for the lipase (Fig. 1). Thirdly, a higher amount of water (> 2 %
v/v) may probably influence the esterification equilibrium, shifting it
back to the substrate side (glycerol and benzoic acid). The reaction
mechanism is an enzymatic hydrolysis reaction, in which the enzyme
catalyzes the breakdown of the linkages generating glycerol, benzoic
acid and water. With respect to Cyrene when forming derivatives with
water, it would act as water sink, suppressing (partly) the hydrolysis
reaction.
Fig. 7. Operational stability of the biocatalysts A) Nov-435 and B) CALB-CLEA.
Reaction conditions: 24 h reaction, 67 mg of biocatalyst, reaction volume 2 mL,
10 mM benzoic acid, 200 mM glycerol molar ratio substrates 1:20.
In a subsequent set of experiments, the reaction was studied in terms
of productivities, using different amounts of benzoic acid (10 and
reactors keeping the same amount of biocatalyst by volume of reaction
media. Before starting the next batch, the biocatalysts were washed
with 25 mM phosphate buffer pH 7. Remarkably, the Nov-435 deriva-
tive loses its operational stability after the first cycle, whereas the
CALB-CLEA remain active over several cycles, in which activity is
gradually lost (ca. half of it after 6 cycles). Apart from the expected
desorption of the enzyme and support dissolution in the Nov-435, the
low LogP of Cyrene may play a deleterious role [41]. Interestingly, the
CLEA derivatives seem to be more resistant to the solvent, presumably
due to their covalent bonding [37].
50 mM). Results are depicted in Fig. 6. At low concentrations of benzoic
acid (10 mM), full conversion was achieved in less than 48 h, ac-
−
1
−1
counting for a (still suboptimal) productivity of ∼3 g product L
d
.
Remarkably, the enzyme resulted active in the solvent system and with
5
0 mM of benzoic acid, and the enzymatic performance remained at a
−
1
constant rate for at least 50 h, accumulating 10 g product L
case.
in that
To further assess the operational stability in Cyrene, the enzymatic
esterification was carried out in sequential batch reactors, using the
commercially available, immobilized CAL-B (Nov-435), as well as
crosslinked aggregates of Lipase B from Candida antarctica (CALB-
CLEA) (Fig. 7). Operational stability was carried out in sequential batch
3.2. Cyrene™ as cosolvent in hydrolysis reaction
Once the potential of Cyrene as solvent for non-conventional media
4