3.1.1. Optimization of the Binding
The soluble lipase preparations used for the study showed different hydrolytic activity against the
pNPP substrate. Namely, at 1 mg/mL concentration, the lipases of
A. niger,
R. niveus,
R. oryzae,
R. miehei, and
C. rugosa demonstrated volumetric activities of 7.15, 212.2, 1697, 2231 and 2703 U/mL, respectively, under the standard enzyme activity assay (pH 7.0, 30 °C). As seen, the activity of
A. niger lipase was much lower than that of the other enzymes tested, which may be due to the fact that the pH optimum of
Aspergillus lipases is mostly in the acidic range [
35]. Consistent with this,
A. niger lipase was also tested at a lower pH, i.e., at pH 5.5 and 4.5, resulting in 113.6 and 238.5 U/mL activities, respectively. Therefore, the acetate buffer condition of pH 4.5 was considered standard for
A. niger lipase in future reactions.
Physical and chemical state, and molecular size of the enzyme can also affect the immobilization [
24]. With this context, molecular weights of ~45, ~83, ~43, ~67, and ~31 kDa were documented for the
A. niger,
R. niveus,
R. oryzae,
C. rugosa, and
R. miehei lipases by the manufacturer (Sigma-Aldrich) and Urrutia et al. [
36]. The spherical molecular diameter of
R. miehei lipase was reported at around 3.5 nm [
37], which corresponds to that value (~50 Å, 5 nm) typical of lipases [
12]. Although the diameter of lipase molecules can double in an aqueous environment, their average diameter still ensures that lipase molecules can penetrate the pores and cover the available surface area of the Accurel MP 1000 support.
Many synthetic materials and polymers have been reported as effective support for lipase immobilization, as highlighted in the recent study by Guajardo [
38]. Among these, Accurel MP 1000 is notable for its scalability and porous structure. Practical applications of lipases immobilized on widely used supports are summarized in the study of Mokhtar et al. [
39]. Accurel MP 1000–lipase complexes, for instance, were used for the production of pharmacological derivatives [
17], emollient esters [
19], and structured lipids [
20].
The immobilization started with an ethanolic solution (50%,
v/
v) pretreatment of the polypropylene support. Ethanol can enhance the effectiveness of immobilization, since it facilitates the penetration of lipases within the pores of Accurel, and removes the air from the support particles, which is favorable for adsorption [
14,
28,
39]. Because the soluble enzyme preparations used have different hydrolytic activities, they were loaded onto a constant amount of support (200 mg), but at different concentrations ranging from 0.001 to 1 mg/mL for
R. oryzae,
R. miehei, and
C. rugosa, and from 0.01 to 1 mg/mL for
A. niger and
R. niveus lipases (
Table 1). The protein content of the commercial preparations was very low, that is, 1 mg/mL enzyme solutions contained only 21.8 to 143 µg/mL protein (
Table 1). According to Gitlesen et al. [
40], the commercial lipase preparations generally consist of about 10% of protein, i.e., a small fraction of the total mass is protein and only a part of this protein fraction is lipase. Kilcawley et al. [
41] examined several commercially available peptidase and lipase preparations and found a low protein content for these preparations with respect to lipases between 0.5% and 11.1% on a dry weight basis. Commercial lipase and other enzyme preparations may contain many other materials which presumably play a role in the production process or in the stabilization of enzymes [
41]. Sabbani et al. [
12] and de Menezes et al. [
19] also reported that the commercially available
C. rugosa lipase preparation contains other proteins, polypeptides and polysaccharides beside the lipase protein, which could also influence the selectivity and catalytic activity of the enzyme. Although targeted enzyme protein isolation has not been performed in our current study, chromatographic purification of enzyme proteins can prevent these components from affecting immobilization and enzyme activity.
In our study, the protein content of the supernatant was also monitored during immobilization. Although different enzyme powder loads were tested (see
Table 1), changes in protein concentration were studied for the highest enzyme concentration applied (1 mg/mL) (
Table 2). For all enzymes studied, a decreasing trend in protein concentration of supernatants can be registered during immobilization process (
Table 2). After incubation for 24 h, immobilization yields of 83%, 66%, 47% and 72% were achieved for
R. niveus,
A. niger,
R. miehei and
C. rugosa lipases, respectively. In
R. oryzae, an immobilization yield of 79% was obtained after only 2 h of incubation. For comparison, loading of
C. rugosa,
C. parapsilosis and
R. oryzae lipases onto Accurel MP 1000 support resulted in 100% [
19], 80% [
18,
28] and 34.71% [
29] immobilization yields, respectively, after about 18–24 h incubation. In other studies, protein adsorption rates of 36.76%, 35.4%, and 5.1% were observed for commercial porcine pancreatic lipase, and
Rhizopus arrhizus and
R. miehei fungal lipases, respectively, while binding to Accurel MP 1000 [
42,
43]. However, due to the low protein concentration in the lipase solutions (see
Table 1), examination of the adsorption was confined to monitor the residual activity of the supernatant during immobilization.
By varying the initial enzyme concentration, significant differences were found in both the rate and efficiency of immobilization (
Table 1 and
Figure 1). In general, at lower enzyme powder concentrations, the binding rate was very high in 15–30 min, while it was much lower at higher concentrations (0.1–1 mg/mL). In
R. oryzae lipase, no residual activity was detected in the supernatant after 90 min of incubation at all enzyme concentrations applied due to the very rapid adsorption that occurred (
Figure 1A). The immobilization of the other enzymes tested was slower, especially at concentration of 1 mg/mL where intensive adsorption can be observed in the earlier stage of incubation, then the intensity decreased significantly in the later period. For example, immobilization efficiency of 85% (15% residual activity) and 75% (25% residual activity) can be observed after 120 min incubation for the
R. niveus and
A. niger lipases, respectively, at 1 mg/mL powder concentration (
Figure 1B,C), while the complete immobilization of these enzymes required of about 360 min incubation (
Table 1). In
R. miehei and
C. rugosa lipases, more than 80% of immobilization efficiency was detected after 120 min of incubation at the highest enzyme powder concentration (
Figure 1D,E), but considerable binding was not detected during the subsequent incubation period. After 24 h of incubation, immobilization efficiency of 93% and 97% were reached for
R. miehei and
C. rugosa lipases, respectively, when the initial powder concentration of the lipase solution was 1 mg/mL (
Table 1).
A higher concentration of the initial powder solution resulted in a higher immobilized activity (
Table 1). However, as the initial concentration of enzyme powder increased, the activity yield decreased substantially. In
Rhizopus lipases, for example, high activity yield (121.2% and 115.2%) was detected at the lowest initial enzyme concentrations, while low activity yield (2.39% and 3.87%) was identified at 1 mg/mL loading powder concentration. For
A. niger,
R. miehei, and
C. rugosa lipases, activity yield decreased to a lesser extent by 15.33–65.81%, by increasing the initial enzyme concentrations from 0.001 or 0.01 to 1 mg/mL. Relatively high immobilized activities of 25.07 and 21.18 U/mg support were found for
R. miehei and
C. rugosa lipases when the concentration of 1 mg/mL of enzyme solutions was used.
A possible reason for the decrease in the adsorption rate and low activity yield at high initial enzyme concentrations can be the saturation of the support during immobilization. As the number of available binding sites decreases, the initially rapid binding rate slows, leading to slower subsequent adsorption. This may result in the formation of a second enzyme layer on the support. Consequently, despite the potentially high amount of active immobilized enzyme, only moderate activity can be observed for the enzyme-support complex [
7]. In addition, mass transfer (diffusion) limitations may arise due to high enzyme loading on the support, which can also contribute to reduced activity, as reported by Salis et al. [
44]. The additional components, i.e., protein and sugar, which are present in commercial enzyme preparations, can also decrease the activity yield at higher concentration through adsorption to hydrophobic support and competitively occupy the binding sites.
To test the activity loss of soluble lipases during immobilization conditions, they were incubated at standard reaction conditions (see
Section 2.3) used for immobilized enzyme preparation. Soluble lipases of
A. niger,
C. rugosa, and
R. niveus were relatively stable, retaining more than 70% of their initial activity, while enzymes from
R. oryzae and
R. miehei retained 37.33% and 59.36% of their initial activity, respectively, after 4 h incubation under standard immobilization condition. The instability of the soluble
R. oryzae enzyme may explain both the rapid decline in residual activity in the supernatant (
Figure 1A) and the low bound activity observed for the immobilized enzyme. At low concentrations, each enzyme adsorbed rapidly (
Figure 1A–E); therefore, the loss of activity was not significant in terms of activity yield due to short incubation period. However, this factor may contribute to the reduced activity yield observed at higher initial enzyme concentrations, where longer incubation is typically required.
Interestingly, in contrast to the soluble enzyme, which exhibited optimal activity in acidic conditions, the immobilized
A. niger lipase showed approximately 30–40% lower activity at pH 4.5 compared to pH 7.0. A shift in the pH optimum toward a slightly alkaline region following immobilization has been reported in several studies and is commonly attributed to changes in the electrostatic environment of the enzyme upon binding to the support [
45,
46]. Consequently, in subsequent experiments, the activities of the immobilized enzyme preparations were consistently measured at pH 7.0 as well.
3.1.2. Effect of pH and Temperature on Adsorption
It is well established that the physical adsorption of lipases onto hydrophobic supports is highly influenced by the ionizing properties of the buffer system; specifically, low ionic strength tends to favor lipase binding [
47]. In this study, we focused on the effects of pH and temperature on the rate and efficiency of enzyme adsorption. Standard immobilization conditions were set at pH 7.0 and 25 °C for all enzymes, except for
A. niger lipase, which was tested at pH 4.5. Initial enzyme concentrations were 0.1 mg/mL for
Rhizopus and
A. niger lipases, and 0.01 mg/mL for
R. miehei and
C. rugosa lipases.
The adsorption rates of
R. oryzae,
R. niveus and
C. rugosa lipases at pH 8.5 were comparable to those at the standard pH (7.0), while adsorption at pH 5.5 proceeded more slowly (
Table 3). Despite similar binding rates, immobilized activity for these enzymes was markedly lower when immobilization occurred under either acidic or alkaline conditions. Notably, immobilization at pH 8.5 led to a substantial decrease (37.3–77.3%) in bound activity. Similarly,
R. miehei lipase displayed reduced bound activity (62.51%) at pH 8.5, while a notable improvement (about 44% increase) in activity was observed when immobilization was conducted at pH 5.5 (
Table 3). A strong preference for acidic conditions was also showed for the
A. niger lipase. When immobilized at pH 7.0, the resulting biocatalyst retained only 12% of the relative activity observed at pH 4.5.
It was reported that the pH during immobilization may affect both the reactivity of the enzyme toward the support and the orientation of the enzyme on the support after the adsorption [
25]. While hydrophobic interactions are important driving forces in the adsorption of lipase onto supports such as EP-100 (the former name of Accurel MP 1000) [
40], ionic interactions also play a significant role, making the pH of the working buffer used for adsorption another critical parameter. It was also reported that optimal adsorption often occurs near the isoelectric point (pI) of the enzyme [
13].
Regarding temperature, our results showed that it primarily influenced the rate of adsorption rather than the final bound activity. At 5 °C, complete enzyme binding required 15–30 min longer than at room temperature; however, in most cases, the final immobilized activity was similar or only slightly reduced. An exception was observed with
R. miehei lipase, which exhibited nearly double the bound activity when immobilized at 5 °C compared to 25 °C, under pH 7.0 condition (see
Table 3). This enhanced activity may be due to slower enzyme inactivation at lower temperatures. While reduced temperature generally slows the adsorption kinetics, the observed increase in bound activity for
R. miehei lipase suggests an enzyme-specific stabilization effect during low-temperature immobilization.
3.1.3. Glutaraldehyde Treatment of Immobilized Enzymes
Immobilized lipases were treated with varying concentrations (1%, 2%, or 3%) of glutaraldehyde to crosslink the adsorbed lipase molecules on the support surface. The aim of this experiment was to evaluate the effect of glutaraldehyde chemical modification on the stability and activity of the biocatalysts. Following glutaraldehyde treatment, the enzymatic activities of the biocatalysts were measured. As controls, parallel immobilized samples were incubated under identical conditions in buffer without glutaraldehyde.
As shown in
Table 4, a slight reduction in enzymatic activity was observed for all enzymes regardless of the glutaraldehyde concentration when compared to the initial biocatalysts (considered as 100% activity). The greatest activity loss was observed in the
A. niger lipase preparation resulting in about 60% residual activity (
p < 0.05), while
R. niveus lipase exhibited the least sensitivity towards the incubation, retaining about 90% of its original activity.
Our results indicate that the observed loss of activity may not be attributed solely to the presence of glutaraldehyde. In
A. niger and
R. miehei lipases, for instance, control experiments revealed that significant (
p < 0.05) activity loss also occurred after 1 h of incubation in glutaraldehyde-free phosphate buffer (pH 7.0, 25 °C) compared to initial biocatalysts (
Table 4), suggesting that part of the activity decrease may be due to shear stress or destabilization caused by prolonged stirring in aqueous medium. For
R. oryzae/
R. niveus/
C. rugosa lipase–Accurel complexes, this decrease in lipolytic activity was not significant (
p > 0.05) (
Table 4). Additionally, in all enzymes tested, there was no significant reduction (
p > 0.05) in residual activities after glutaraldehyde treatment as compared to control incubation, implying that glutaraldehyde may partially stabilize the enzyme conformation and offset activity losses caused by incubation conditions. Although we have not yet investigated the presence of such bonds in the biocatalysts produced, this stabilizing effect is likely due to the formation of covalent bonds between the free amino groups of lysine residues, either within the enzyme or between adjacent enzyme molecules, via Schiff base formation [
48]. Such crosslinking can reduce enzyme leaching and enhance structural rigidity, thereby contributing to improved retention of activity under operational conditions. This observation is consistent with findings by Zaak et al. [
49], who reported residual activities of 63–97% for lipase and phospholipase octyl-Sepharose preparations following 1 h treatment with 0.1% (
v/
v) glutaraldehyde. Glutaraldehyde treatment of octyl-agarose beads also resulted in stable lipase biocatalysts in the study of Abellanas-Perez et al. [
50], but the effect was strongly depended on the enzyme load applied for the immobilization. In cases of lowly loaded biocatalysts (1 mg/g), a slight increase in enzyme activity was observed following glutaraldehyde treatment [
50]. For comparison, enzyme loadings between 0.5 mg/g (0.01 mg/mL) and 5 mg/g (0.1 mg/mL) were used in our corresponding studies depending on the tested enzyme (see
Table 4 footnote). Glutaraldehyde has been shown to impart significant structural stability to other immobilized enzymes such as β-galactosidases by forming covalent bridges, resulting in enhanced operational and thermal stability [
51,
52]. Potential industrial applications of lipase–Accurel MP 1000 biocatalysts subjected to crosslinking with glutaraldehyde were documented for the production of milk fat substitutes [
18], biodiesel [
28] and ethyl lactate [
29].
Based on the retained activity profiles, a glutaraldehyde concentration of 1% and 2% was selected for further treatments of R. miehei, and R. niveus and C. rugosa lipases, respectively, while 3% was found to be most suitable for R. oryzae and A. niger preparations.