Cholinium carboxylate ionic liquids for pretreatment of lignocellulosic materials to enhance subsequent enzymatic saccharification

The present study is the first report demonstrating that ionic liquids consisting of cholinium cations and linear carboxylate anions ([Ch][CA] ILs) can be used for pretreatment of lignocellulosic materials to enhance subsequent enzymatic saccharification. Six variants of [Ch][CA] ILs were systematically prepared by combining cholinium cations with linear monocarboxylate anions ([C_nH_2n+1–COO]⁻, n = 0–2) or dicarboxylate anions ([HOOC–C_nH_2n+1–COO]⁻, n = 0–2). These [Ch][CA] ILs were analyzed for their toxicity to yeast cell growth and their ability to pretreat kenaf powder for subsequent enzymatic saccharification. When assayed against yeast growth, the EC₅₀ for choline acetate ([Ch][OAc]) was 510 mM, almost one order of magnitude higher than that for 1-ethyl-3-methylimidazolium acetate ([Emim][OAc]). The cellulose saccharification ratio after pretreatment at 110 °C for 16 h with [Ch][OAc] (100.6%) was almost comparable with that after pretreatment with [Emim][OAc]. Therefore, [Ch][OAc] is a biocompatible alternative to [Emim][OAc] for lignocellulosic material pretreatment.     

Effect of ionic liquids,organic solvents and supercritical CO2 pretreatment on the conformation and catalytic properties of Candida rugosa lipase

The objective of this work is to assess the structure and activity of Candida rugosa lipase (CRL) pretreated with seventeen ionic liquids (ILs), five organic solvents and super-critical carbon dioxide (SC-CO₂). The results revealed that anion selection of ILs showed generally much greater effects on CRL esterification activity than cation choice, and CRL pretreated by ILs with strong water miscible properties showed very low esterification activity. The highest CRL activity treated with ILs [Hmim][PF6] was obtained with the value of 45078.0 U/g-protein. Furthermore, the CRL activities pretreated with five conventional organic solvents were also examined and the values increased with the log P decrease of organic solvents when log P was lower than 2.0. Finally, the CRL activities were respectively 1.2- and 1.3-fold higher over the untreated ones after pretreatment with sub- and super-critical CO₂ under the pressures of 6 MPa and 15 MPa at 40 °C for 20 min. Further analyses via FT-IR demonstrated that the high activity of CRL pretreated with ILs, organic solvents and SC-CO₂ was probably caused by the changes of CRL secondary structure. In conclusion, the results in this work will be helpful for us to choose the suitable reaction medium in CRL biocatalysis and biotransformation reactions.     

Enzymatic hydrolysis of racemic ibuprofen esters using Rhizomucor miehei lipase immobilized on different supports

This research describes the immobilization of Rhizomucor miehei lipase (RML) and chemically aminated RML (NH₂-RML) on different supports including octyl-sepharose (octyl-RML), activated sepharose with cyanogen bromide (CNBr-RML and CNBr-NH₂-RML), glyoxyl sepharose (Gx-RML and Gx-NH₂-RML) and glyoxyl sepharose dithiothreitol (Gx-DTT-RML and Gx-DTT-NH₂-RML). The highest immobilization yield was achieved for octyl-RML (>98%) followed by CNBr-RML (88%). Octyl-RML had the most specific activity (13.6) among all derivatives. The other preparations had moderate activities likely because of chemical reaction during covalent attachment of the enzyme. The catalytic behavior of lipase immobilized in hydrolysis reactions was investigated using methyl, ethyl, propyl, butyl and isobutyl-ibuprofen esters and the influence of the alkyl chain and the alcoholic residue of the ester were studied. Butyl ester was the most interesting ester for carrying out hydrolysis. The highest enantioselectivity of enzyme (E = 8.8) was obtained with isooctane/sodium phosphate buffer pH 7.0 at temperature of 40 °C. Increasing temperature from 40 to 50 °C caused decreasing in enantioselectivities and conversions. Also esterification of ibuprofen was carried out in solvent systems containing isooctane and two ionic liquids (ILs); [BMIM][PF₆] and [BMIM][BF₄]. Poor conversions and enantioselectivities were observed during esterification in all solvents.     

Improving the catalytic performance of porcine pancreatic lipase in the presence of [MMIm][MeSO4] with the modification of functional ionic liquids

Porcine pancreatic lipase (PPL) was chemically modified with various functional ionic liquids (ILs) to increase its catalytic performance in water-miscible IL. Catalytic activity and thermostability were tested with a p-nitrophenyl palmitate (pNPP) hydrolysis reaction. The native enzyme lost 18% of its initial activity in 0.4 M [MMIm][MeSO₄], whereas the activities of all the modified enzymes increased. The [HOOCBMIm][Cl] modification led to a 2-fold increase in activity in 0.3 M [MMIm][MeSO₄] than in aqueous. All the modified enzymes exhibited higher thermostability compared with the native enzyme at high temperature. In particular, the [HOOCBMIm][Cl] modification led to a 6-fold increase in thermostability at 60 °C. Conformational changes were confirmed by fluorescence spectroscopy and circular dichroism spectroscopy to elucidate the mechanism of catalytic performance alteration.     

Tween 80 influences the production of intracellular lipase by Schizochytrium S31 in a stirred tank reactor

Marine microorganisms are a potential source of enzymes with structural stability, high activity at low temperature and unique substrate selectivity. Thraustochytrids are marine heterotrophic microbes, well known for the production of omega-3 fatty acids. In this study the effect of Tween 80 as a carbon source was investigated with regard to biomass, lipase and lipid productivity in Schizochytrium sp. S31. Tween 80 (1%) and 120 h of incubation were the optimum condition period for biomass, lipid and lipase productivity in a stirred tank reactor. The yields obtained were 0.9 g L⁻¹ of biomass, 300 mg g⁻¹ of lipid and 39 U/g of lipase activity. Sonication was optimised in terms of time and acoustic power to maximise the yield of extracted lipase. The extracted lipase from Schizochytrium S31 was observed to hydrolyse long chain polyunsaturated fatty acids DHA and EPA.     

Continuous succinic acid production by Actinobacillus succinogenes in a biofilm reactor: Steady-state metabolic flux variation

Continuous anaerobic fermentations were performed in a novel external-recycle, biofilm reactor using d-glucose and CO₂ as carbon substrates. Succinic acid (SA) yields were found to be an increasing function of glucose consumption with the succinic acid to acetic acid ratio increasing from 2.4 g g⁻¹ at a glucose consumption of 10 g L⁻¹, to 5.7 g g⁻¹ at a glucose consumption of 50 g L⁻¹. The formic acid to acetic acid ratio decreased from an equimolar value (0.77 g g⁻¹) at a glucose consumption of 10 g L⁻¹ to a value close to zero at 50 g L⁻¹. The highest SA yield on glucose and highest SA titre obtained were 0.91 g g⁻¹ and 48.5 g L⁻¹ respectively. Metabolic flux analysis based on the established C₃ and C₄ metabolic pathways of Actinobacillus succinogenes revealed that the increase in the succinate to acetate ratio could not be attributed to the decrease in formic acid and that an additional source of NADH was present. The fraction of unaccounted NADH increased with glucose consumption, suggesting that additional reducing power is present in the medium or is provided by the activation of an alternative metabolic pathway.     

Preliminary diagnostic reference levels for endoscopic retrograde cholangio-pancreatography in Greece

The main objective of this study was to determine the preliminary Diagnostic Reference Levels (DRLs) in terms of Kerma Area Product (KAP) and fluoroscopy time (Tf) during Endoscopic Retrograde Cholangio-Pancreatography (ERCP) procedures. Additionally, an investigation was conducted to explore the statistical relation between KAP and Tf.Data from a set of 200 randomly selected patients treated in 4 large hospitals in Greece (50 patients per hospital) were analyzed in order to obtain preliminary DRLs for KAP and Tf during therapeutic ERCP procedures. Non-parametric statistic tests were performed in order to determine a statistically significant relation between KAP and Tf.The resulting third quartiles for KAP and Tf for hospitals (A, B, C and D) were found as followed: KAP_A = 10.7 Gy cm², Tf_A = 4.9 min; KAP_B = 7.5 Gy cm², Tf_B = 5.0 min; KAP_C = 19.0 Gy cm², Tf_C = 7.3 min; KAP_D = 52.4 Gy cm², Tf_D = 15.8 min. The third quartiles, calculated for the total 200 cases sample, are: KAP = 18.8 Gy cm² and Tf = 8.2 min. For 3 out of 4 hospitals and for the total sample, p-values of statistical indices (correlation of KAP and Tf) are less than 0.001, while for the Hospital A p-values are ranging from 0.07 to 0.08. Using curve fitting, we finally determine that the relation of Tf and KAP is deriving from a power equation (KAP = Tf^1.282) with R² = 0.85.The suggested Preliminary DRLs (deriving from the third quartiles of the total sample) for Greece are: KAP = 19 Gy cm² and Tf = 8 min, while the relation between KAP and Tf is efficiently described by a power equation.     

Immobilization of acidic lipase derived from Pseudomonas gessardii onto mesoporous activated carbon for the hydrolysis of olive oil

Mesoporous activated carbon (MAC) derived from rice husk is used for the immobilization of acidic lipase (ALIP) produced from Pseudomonas gessardii. The purified acidic lipase had the specific activity and molecular weight of 1473 U/mg and 94 kDa respectively. To determine the optimum conditions for the immobilization of lipase onto MAC, the experiments were carried out by varying the time (10–180 min), pH (2–8), temperature (10–50 °C) and the initial lipase activity (49 × 10³, 98 × 10³, 147 × 10³ and 196 × 10³ U/l in acetate buffer). The optimum conditions for immobilization of acidic lipase were found to be: time—120 min; pH 3.5; temperature—30 °C, which resulted in achieving a maximum immobilization of 1834 U/g. The thermal stability of the immobilized lipase was comparatively higher than that in its free form. The free and immobilized enzyme kinetic parameters (K_m and V_max) were found using Michaelis–Menten enzyme kinetics. The K_m values for free enzyme and immobilized one were 0.655 and 0.243 mM respectively. The immobilization of acidic lipase onto MAC was confirmed using Fourier Transform-Infrared Spectroscopy, X-ray diffraction analysis and scanning electron microscopy.     

Effect of the aeration rate and agitation speed on β-carotene production and morphology of Blakeslea trispora in a stirred tank reactor: mathematical modeling

The effect of aeration rate and agitation speed on β-carotene production and morphology of Blakeslea trispora in a stirred tank reactor was investigated. B. trispora formed hyphae, zygophores and zygospores during the fermentation. The zygospores were the morphological form responsible for β-carotene production. Both aeration and agitation significantly affected β-carotene concentration, productivity, biomass and the volumetric mass transfer coefficient (K_La). The highest β-carotene concentration (1.5 kg m⁻³) and the highest productivity (0.08 kg m⁻³ per day) were obtained at low impeller speed (150 rpm) and high aeration rate (1.5 vvm). Also, maximum productivity (0.08 kg m⁻³ per day) and biomass dry weight (26.4 kg m⁻³) were achieved at high agitation speed (500 rpm) and moderate aeration rate (1.0 vvm). Conversely, the highest value of K_La (0.33 s⁻¹) was observed at high agitation speed (500 rpm) and high aeration rate (1.5 vvm). The experiments were arranged according to a central composite statistical design. Response surface methodology was used to describe the effect of impeller speed and aeration rate on the most important fermentation parameters. In all cases, the fit of the model was found to be good. All fermentation parameters (except biomass concentration) were strongly affected by the interactions among the operation variables. β-Carotene concentration and productivity were significantly influenced by the aeration, agitation, and by the positive or negative quadratic effect of the aeration rate. Biomass concentration was principally related to the aeration rate, agitation speed, and the positive or negative quadratic effect of the impeller speed and aeration rate, respectively. Finally, the volumetric mass transfer coefficient was characterized by the significant effect of the agitation speed, while the aeration rate had a small effect on K_La.     

Pancreatic α-amylase and lipase inhibitory activity of polyphenolic compounds present in the extract of black chokeberry (Aronia melanocarpa L.)

The aim of this study was to investigate the effect of black chokeberry (Aronia melanocarpa L.) extract on the activity of porcine pancreatic α-amylase and lipase. An in vitro study demonstrated that three kinds of chokeberry extracts: methanolic, water and acetic caused inhibition of α-amylase and lipase. The methanolic and acetic extracts exhibited the highest inhibitory activities against α-amylase with the IC₅₀ values of 10.31 ± 0.04 mg/ml and pancreatic lipase 83.45 ± 0.50 mg/ml, respectively. In order to identify the compounds which may be the potential inhibitors of α-amylase and lipase, chokeberry extract was analyzed by preparative reverse phase chromatography and high performance liquid chromatography–mass spectrometry (HPLC–MS). These studies have shown that both anthocyanins and phenolic acids are compounds which inhibit the ability of the reaction catalyzed by α-amylase and lipase. The most effective inhibitor of pancreatic α-amylase was chlorogenic acid (IC₅₀ = 0.57 ± 0.16 mg/ml). In the group of anthocyanins the most potent inhibitor of α-amylase was cyanidin-3-glucoside (IC₅₀ = 1.74 ± 0.04 mg/ml), which also showed an ability to inhibit the reaction catalyzed by pancreatic lipase (IC₅₀ = 1.17 ± 0.05 mg/ml). These findings seem to indicate the use of chokeberry as a functional food component, contributing to its anti-obesity activities.     

Lipase-catalyzed enantioselective acylation of 3-benzyloxypropane-1,2-diol in supercritical carbon dioxide

Lipase-catalyzed acylation of 3-benzyloxypropane-1,2-diol with vinyl acetate as acyl donor using different lipases [porcine pancreas lipase (PPL), Lipase AK “Amano”, Lipase PS “Amano”, and crude enzymes from Trichoderma reesei RUT-C30, Thermoascus thermophilus (NRRL5208), Talaromyces emersonii (NRLL3221)] was studied in supercritical carbon dioxide (scCO₂). In the reactions catalyzed by different lipases different amounts of monoacetate and diacetate products along with minor amounts of cyclic acetals forming from the diol and acetaldehyde were obtained.Application of Lipase AK led to the highest conversion (84.7%) and the highest enantiomeric excess values (ee_monoacetates = 38%, ee_diacetate = 85%). Effect of water content of scCO₂ on the productivity and the enantiomer selectivity of the reactions with Lipase AK was also investigated.     

High hydrostatic pressure increased stability and activity of immobilized lipase in hexane

Lipases are important to high value product synthesis, modification, and enhancement. However, they are often unstable above 40 °C. While most current applications of high hydrostatic pressure (HHP) are for inactivating deleterious enzymes, there is evidence that HHP can stabilize and increase activity of some enzymes. This study examines the apparent kinetics of immobilized lipase-catalyzed synthesis of isoamyl acetate at HHP in hexane. HHP reduced thermal inactivation of lipase by up to 152% after 4 h at 80 °C and 400 MPa when compared to incubations at low pressure. No significant differences were found in activation energy (E_a) at different pressures, irrespectively of the pressurization and heating sequence, and were between 35.7 ± 3.5 and 47.8 ± 8.2 kJ mol^?1, depending on the method. In all methods utilized, activity at 63.5 and 80 °C at 400 MPa was greater (from about 20 to 96% increase) than at low pressure. Activity increased by 110% at low pressure versus a 239% increase at 350 MPa when the temperature was increased from 40 to 80 °C. Increasing pressure up to 350 MPa increased lipase activity while pressures greater than 350 MPa maintained or decreased lipase activity. Activation volume (ΔV^≠) appeared negative between ambient pressure and 200 MPa in contrast to a positive ΔV^≠ between 300 and 600 MPa. Apparent ΔV^≠ was 14.3 ± 1.7 or 15.2 ± 2.2 cm³ mol^?1 at 40 or 80 °C, respectively, between 300 and 500 MPa.     

Butanol recovery from aqueous solution into ionic liquids by liquid–liquid extraction

Biobutanol has currently attracted considerable attention as an alternative biofuel to the petroleum-derived fuel due to several advantages including high energy content, low water absorption and easy application to the existing gasoline infrastructure. However, its production has still faced many obstacles to overcome including lack of energy-efficient butanol separation process from fermentation broth. To solve this issue, the extraction behavior of butanol from aqueous media into a variety of imidazolium-based ionic liquids (ILs) was investigated by liquid–liquid extraction. To understand the effect of ILs properties, the solvent characteristics of ILs such as mutual solubility of feed solvent (water) and extraction solvent (IL), distribution coefficient of butanol between water and IL, selectivity, and extraction efficiency were correlated with hydrophobicity and polarity of ILs. The butanol distribution between ILs and water strongly depends on the hydrophobicity of anions of ILs followed by the hydrophobicity of cations of ILs. On the other hand, butanol extraction efficiency and selectivity depend on the polarity of ILs. Considering extraction efficiency and selectivity, [Tf₂N]-based ILs among the tested ILs showed to be the best extract solvent for the recovery of butanol from aqueous media. Among the studied ILs, [Omim][Tf₂N] showed the highest butanol distribution coefficient (1.939), selectivity (132) and extraction efficiency (74%) at 323.15 K, respectively.     

Lipase-catalyzed acylation of lily polysaccharide in ionic liquid-containing systems

A comparative study was made of immobilized Burkholderia cepacia lipase (PSL-C)-catalyzed acylation of lily polysaccharide (LP) with vinyl acetate in organic solvents, ionic liquids (ILs) and IL-containing systems. The degree of substitution (DS) of the modified LP was used to evaluate the extent of acylation and thus enzymatic activity. In this manner, an eco-friendly solvent, 2-methyltetrahydrofuran (MeTHF), was found to be the most suitable organic reaction medium. However, compared to MeTHF, enhanced enzyme activity was observed when 1-butyl-3-methylimidazolium tetrafluorobrate ([C₄MIm][BF₄]) was used as the solvent. To further enhance the DS of the modified LP product, co-solvent mixtures of [C₄MIm][BF₄] and MeTHF were investigated. Among the various MeTHF–[C₄MIm][BF₄] systems examined, 20% (v/v) MeTHF–[C₄MIm][BF₄] produced the highest DS. In this reaction medium, the optimal water activity, reaction temperature and time were 0.33, 55 °C and 18 h, respectively, producing a product DS as high as 0.67. The PSL-C enzyme exhibited a much higher stability in the IL-containing system. Additionally, PSL-C-catalyzed acylation of LP was highly regioselective, causing acylation of only C6OH.     

Synthesis of geranyl acetate in non-aqueous media using immobilized Pseudomonas cepacia lipase on biodegradable polymer film: Kinetic modelling and chain length effect study

Pseudomonas cepacia lipase (PCL) was immobilized on ternary blend biodegradable polymer made up of polylactic acid (PLA), chitosan (CH), and polyvinyl alcohol (PVA). Immobilized biocatalyst was characterized using scanning electron microscopy (SEM), Fourier transform infrared spectroscopy (FTIR), % water content, protein and lipase activity assay. The lipase activity assay showed enhanced activity of immobilized lipase than crude lipase. Higher half life time (t_1/2) and lower deactivation rate constant (K_d) was found for the n-hexane among various tested solvent. Influence of various reaction parameters on enzyme activity were studied in detail. When geraniol (1 mmol) and vinyl acetate (4 mmol) in toluene (3 mL) were reacted with 50 mg immobilized lipase at 55 °C; then 99% geraniol was converted to geranyl acetate after 3 h. Various kinetic parameters such as r_max, K_i(A), K_m(A), K_m(B) were determined using non-linear regression analysis for ternary-complex and Bi–Bi ping-pong mechanism. The kinetic study showed that reaction followed ternary-complex mechanism with inhibition by geraniol. Activation energy (Ea) was found to be lower for immobilized lipase (13.76 kCal/mol) than crude lipase (19.9 kCal/mol) indicating better catalytic efficiency of immobilized lipase. Immobilized biocatalyst demonstrated 4 fold increased catalytic activity than crude lipase and recycled five times.     

Immobilization of Candida rugosa lipase on electrospun cellulose nanofiber membrane

A biocatalyst with high activity retention of lipase was fabricated by the covalent immobilization of Candida rugosa lipase on a cellulose nanofiber membrane. This nanofiber membrane was composed of nonwoven fibers with 200 nm nominal fiber diameter. It was prepared by electrospinning of cellulose acetate (CA) and then modified with alkaline hydrolysis to convert the nanofiber surface into regenerated cellulose (RC). The nanofiber membrane was further oxidized by NaIO₄. Aldehyde groups were simultaneously generated on the nanofiber surface for coupling with lipase. Response surface methodology (RSM) was applied to model and optimize the modification conditions, namely NaIO₄ content (2–10 mg/mL), reaction time (2–10 h), reaction temperature (25–35 °C) and reaction pH (5.5–6.5). Well-correlating models were established for the residual activity of the immobilized enzyme (R² = 0.9228 and 0.8950). We found an enzymatic activity of 29.6 U/g of the biocatalyst was obtained with optimum operational conditions. The immobilized lipase exhibited significantly higher thermal stability and durability than equivalent free enzyme.     

Characterization of the lipase immobilized on Mg–Al hydrotalcite for biodiesel

Immobilization of Saccharomyces cerevisiae lipase by physical adsorption on Mg–Al hydrotalcite with a Mg/Al molar ratio of 4.0 led to a markedly improved performance of the enzyme. The immobilized lipase retained activity over wider ranges of temperature and pH than those of the free lipase. The immobilized lipase retained more than 95% relative activity at 50 °C, while the free lipase retained about 88%. The kinetic constants of the immobilized and free lipases were also determined. The apparent activation energies (E_a) of the free and immobilized lipases were estimated to be 6.96 and 2.42 kJ mol^?1, while the apparent inactivation energies (E_d) of free and immobilized lipases were 6.51 and 6.27 kJ mol^?1, respectively. So the stability of the immobilized lipase was higher than that of free lipase. The water content of the oil must be kept below 2.0 wt% and free fatty acid content of the oil must be kept below 3.5 mg KOH g [oil]^?1 in order to get the best conversion. This immobilization method was found to be satisfactory to produce a stable and functioning biocatalyst which could maintain high reactivity for repeating 10 batches with ester conversion above 81.3%.     

Immobilized Candida antarctica lipase B on ZnO nanowires/macroporous silica composites for catalyzing chiral resolution of (R,S)-2-octanol

ZnO nanowires were successfully introduced into a macroporous SiO₂ by in situ hydrothermal growth in 3D pores. The obtained composites were characterized by SEM and XRD, and used as supports to immobilize Candida antarctica lipase B (CALB) through adsorption. The high specific surface area (233 m²/g) and strong electrostatic interaction resulted that the average loading amount of the composite supports (196.8 mg/g) was 3–4 times of that of macroporous SiO₂ and approximate to that of a silica-based mesoporous material. Both adsorption capacity and the activity of the CALB immobilized on the composite supports almost kept unchanged as the samples were soaked in buffer solution for 48 h. The chiral resolution of 2-octanol was catalyzed by immobilized CALB. A maximum molar conversion of 49.1% was achieved with 99% enantiomeric excess of (R)-2-octanol acetate under the optimal condition: a reaction using 1.0 mol/L (R,S)-2-octanol, 2.0 mol/L vinyl acetate and 4.0 wt.% water content at 60 °C for 8 h. After fifteen recycles the immobilized lipase could retain 96.9% of relative activity and 93.8% of relative enantioselectivity.     

The effect of glycerol mixed substrate on the heterologous production of a Rhizopus oryzae lipase in Pichia pastoris system

A recombinant Rhizopus oryzae lipase producing Mut^s Pichia pastoris strain was used as a model organism to study the effect of mixed substrates (glycerol and methanol) on the specific product productivity. Different fed-batch cultivations were performed under three constant specific growth rates (0.02, 0.05 and 0.1 h⁻¹), maintaining a constant methanol concentration of 2 g l⁻¹.At the lowest μ tested (0.02 h⁻¹), the specific productivity was 1.23 and 1.61 fold higher and the specific methanol consumption rate (q_sMeOH) was 3 and 3.5 fold higher than values obtained when μ was 0.05 and 0.1 h⁻¹, respectively. This implies a relation between the q_sMeOH and the specific productivity, yielding higher specific productivities whenever the consumption of methanol is higher. Although glycerol was maintained under limiting conditions in all μ tested, when the relation between the μ_Gly and μ_MeOH was larger than 4, an important decrease on the maximal activity value was observed.Finally, a comparison under the same conditions using glycerol or sorbitol as co-substrates was also performed, obtaining better specific productivity when sorbitol was used. In addition, protease activity was detected when glycerol was used as co-substrate.     

Catalytic performance of cross-linked enzyme aggregates of Penicillium expansum lipase and their use as catalyst for biodiesel production

Cross-linked enzyme aggregates (CLEAs) of lipase from Penicillium expansum (PEL) were prepared directly from fermentation broth, a more practical and economically viable procedure than the generally used methods that require purified or partially purified enzymes for CLEA preparation. A systematic study of the activity and stability of PEL-CLEAs was undertaken in aqueous solution, organic solvents, and ionic liquids (ILs). Immobilization of the enzyme resulted in a significantly enhanced stability in aqueous solution with regard to pH and temperature. PEL-CLEAs showed an improved activity in the IL [BMIm][PF₆] relative to that observed in hexane, both keeping increased with temperature (up to 90 °C in the IL and 60 °C in hexane). The effect of water content and water activity in these two nonaqueous media showed similar patterns as for the uncrosslinked enzyme. The half life of the CLEAs was higher in hydrophobic organic solvents (hexane and chloroform) than in aqueous solution, and presented a sigmoid relationship with the log P of the organic solvent tested. PEL-CLEAs catalyzed biodiesel production from microalgal oil in the IL [BMIm][PF₆] with a conversion of 85.7%, demonstrating that they can be taken as a promising catalyst for this application.