Development of an amphiphilic matrix for immobilization of <Emphasis Type="Italic">Candida antartica</Emphasis> lipase B for biodiesel production

Biodiesel has been greatly interested as an alternative fuel and is produced by a transesterification reaction of oil with alcohol. Recently, microbial lipases have been used for biodiesel production. Among the microbial lipase, immobilized Candida antartica lipase B (CALB) is the most widely used. However, CALB is unstable and shows low catalytic efficiency in the reaction media because the reaction media contains a high concentration of methanol and the lipase is also inhibited by the by-product glycerol. In this study, to overcome these limitations, we developed an amphiphilic matrix to immobilize CALB. The immobilized lipase in an amphiphilic matrix with 80% ethyltrimethoxysilane (ETMS) in tetramethoxysilane (TMOS) and pretreated with oil showed the highest specific activity and biodiesel conversion ratio; about 90% biodiesel conversion in 24 h at an initial molar ratio of 1: 1 (oil: methanol) with stepwise methanol feeding in order to adjust the net molar ratio to be 1: 3.     

Improvement in lipase-catalyzed methanolysis of triacylglycerols for biodiesel production using a solvent engineering method

A solvent engineering strategy was applied to the lipase-catalyzed methanolysis of triacylglycerols for biodiesel production. The effect of different pure organic solvents and co-solvent mixtures on the methanolysis was compared. The substrate conversions in the co-solvent mixtures were all higher than those of the corresponding pure organic solvents. Further study showed that addition of co-solvent decreased the values of |log P_interface − log P_substrate| and thus led to a faster reaction. The more the values of |log P_interface − log P_substrate| decreased, the faster the reaction proceeded and the higher the conversion attained. Different co-solvent ratio was further investigated. The co-solvent mixture of 25% t-pentanol:75% isooctane (v/v) was optimal, with which both the negative effects caused by excessive methanol and by-product glycerol could be eliminated. There was no obvious loss in lipase activity even after being repeatedly used for 60 cycles (720 h) with this co-solvent mixture as reaction medium. Other lipases and lipase combinations can also catalyze methanolysis in this co-solvent mixture. Furthermore, other vegetable oils were also explored for biodiesel production in this co-solvent mixture and it had been found that this co-solvent mixture media has extensive applicability.     

Biocatalytic synthesis of vitamin A palmitate using immobilized lipase produced by recombinant Pichia pastoris

In this work, the Candida antarctica lipase B (CALB), produced by recombinant Pichia pastoris , was immobilized and used to synthesize vitamin A palmitate by transesterification of vitamin A acetate and palmitic acid in organic solvent. The reaction conditions including the type of solvent, temperature, rotation speed, particle size, and molar ratio between the two substrates were investigated. It turned out that the macroporous resin HPD826 serving as a carrier showed the highest activity (ca. 9200 U g^?1) among all the screened carriers. It was found that the transesterification kinetic of the immobilized CALB followed the ping pong Bi‐Bi mechanism and the reaction product acetic acid inhibited the enzymatic reaction with an inhibition factor of 2.823 mmol L^?1. The conversion ability of the immobilized CALB was 54.3% after 15 cycles. In conclusion, the present work provides a green route for vitamin A palmitate production using immobilized CALB to catalyze the transesterification of vitamin A acetate and palmitic acid.     

Synthesis of fatty acid ethyl esters with conventional and microwave heating systems using the free lipase B from Candida antarctica

Free Candida antarctica lipase B (Lipozyme, CALB L^®) was used to produce fatty acid ethyl esters (FAEE) from refined soybean oil in solvent-free media using the conventional (CHS) and microwave (MHS) heating systems. Statistical analyses (95% confidence level) for both reaction products, FAEE and free fatty acids (FFA), were performed. An increase in ethanol:oil molar ratio decreased the catalytic performance of CALB L (p?<?.05). The best conditions using the microwave radiation were a molar ratio of ethanol:oil of 3:1, a water content of 20.3?wt.% and an enzyme loading of 3?wt.% and this resulted in a total ester content of 64.7% in 15?min, while the same condition using the conventional heating gave only 21.4%. Moreover, the reaction equilibrium was reached 16 times faster with microwave than with conventional heating. High ethanol:oil molar ratios had a negative effect on FAEE synthesis with both CHS and MHS, probably due to the partial inactivation of the enzymes. MHS improved the reaction performance of CALB L, but other process parameters will have to be optimized to enhance the resulting FAEE yields. The recovery and reuse of CALB L using a MHS was demonstrated. Hence, the use of microwave radiation under the conditions applied in this study was not detrimental to the catalytic performance of CALB L for at least one reuse.     

Preparative scale enantioseparation of flurbiprofen by lipase-catalysed reaction

Effects of reaction media, alcohols and water on the enzyme activity of the immobilised Candida antarctica lipase were investigated for the separation of racemic flurbiprofen by an esterification reaction catalysed by immobilised enzyme in organic media. The S-enantiomer of flurbiprofen was directly resolved by the immobilised lipase esterification reaction in acetonitrile. Ping-Pong Bi–Bi kinetics were found to fit the initial reaction well of all the experimental runs. Model parameters for the reaction kinetics were evaluated from experiments at relatively low substrate concentrations, have shown to be applicable for preparative separation scale at high concentrations. Finally, the gram-scale production of single enantiomer with the optical purity of 93% e.e. was obtained.     

Improvement in lipase-catalyzed methanolysis of triacylglycerols for biodiesel production using a solvent engineering method

A solvent engineering strategy was applied to the lipase-catalyzed methanolysis of triacylglycerols for biodiesel production. The effect of different pure organic solvents and co-solvent mixtures on the methanolysis was compared. The substrate conversions in the co-solvent mixtures were all higher than those of the corresponding pure organic solvents. Further study showed that addition of co-solvent decreased the values of |log P_interface − log P_substrate| and thus led to a faster reaction. The more the values of |log P_interface − log P_substrate| decreased, the faster the reaction proceeded and the higher the conversion attained. Different co-solvent ratio was further investigated. The co-solvent mixture of 25% t-pentanol:75% isooctane (v/v) was optimal, with which both the negative effects caused by excessive methanol and by-product glycerol could be eliminated. There was no obvious loss in lipase activity even after being repeatedly used for 60 cycles (720 h) with this co-solvent mixture as reaction medium. Other lipases and lipase combinations can also catalyze methanolysis in this co-solvent mixture. Furthermore, other vegetable oils were also explored for biodiesel production in this co-solvent mixture and it had been found that this co-solvent mixture media has extensive applicability.     

Optimization of (R,S)-1-phenylethanol kinetic resolution over Candida antarctica lipase B in ionic liquids

The kinetic resolution of racemates constitutes one major route to manufacture optically pure compounds. The enzymatic kinetic resolution of (R,S)-1-phenylethanol over Candida antarctica lipase B (CALB) by using vinyl acetate as the acyl donor in the acylation reaction was chosen as model reaction. A systematic screening and optimization of the reaction parameters, such as enzyme, ionic liquid and substrates concentrations with respect to the final product concentration, were performed. The enantioselectivity of immobilized CALB commercial preparation, Novozym 435, was assayed in several ionic liquids as reaction media. In particular, three different ionic liquids: (i) 1-butyl-3-methylimidazolium hexafluorophosphate [bmim][PF₆], (ii) 1-butyl-3-methylimidazolium tetrafluoroborate [bmim][BF₄] and (iii) 1-ethyl-3-methylimidazolium triflimide [emim][NTf₂] were tested. At 6.6% (w/w) of Novozym 435, dispersed in 9.520 M of [bmim][PF₆] at 313.15 K, using an equimolar ratio of vinyl acetate/(R,S)-1-phenylethanol after 3 h of bioconversion, the highest possible conversion (50%) was reached with enantiomeric excess for substrate higher than 99%.     

Lipase catalysed synthesis of sugar ester in organic solvents

Summary The synthesis of sugar esters catalysed by lipase in organic solvents was studied. Immobilized Candida and Mucor miehei lipase catalysed the synthesis of fructose and glucose esters of stearic acid in tertiary butyl alcohol with yields of 10 to 24 %. In the presence of phenyl or butyl boronic acid synthesis of glucose ester was achieved in hexane, heptane, benzene and toluene. The only positive reaction on disaccharides was found with palatinose.     

Development of yeast cells displaying <Emphasis Type="Italic">Candida antarctica</Emphasis> lipase B and their application to ester synthesis reaction

We isolated the lipase B from Candida antarctica CBS 6678 (CALB CBS6678) and successfully constructed CALB-displaying yeast whole-cell biocatalysts using the Flo1p short (FS) anchor system. For the display of CALB on a yeast cell surface, the newly isolated CALB CBS6678 exhibited higher hydrolytic and ester synthesis activities than the well-known CALB, which is registered in GenBank (Z30645). A protease accessibility assay using papain as a protease showed that a large part of CALB, approximately 75%, was localized on an easily accessible part of the yeast cell surface. A comparison of the lipase hydrolytic activities of yeast whole cells displaying only mature CALB (CALB) and those displaying mature CALB with a Pro region (ProCALB) revealed that mature CALB is preferable for yeast cell surface display using the Flo1p anchor system. Lyophilized yeast whole cells displaying CALB were applied to an ester synthesis reaction at 60°C using adipic acid and n-butanol as substrates. The amount of dibutyl adipate (DBA) produced increased with the reaction time until 144 h. This indicated that CALB displayed on the yeast cell surface retained activity under the reaction conditions.     

Kinetic resolution of drug intermediates catalyzed by lipase B from Candida antarctica immobilized on immobead‐350

Novozyme 435, which is a commercial immobilized lipase B from Candida antarctica (CALB), has been proven to be inadequate for the kinetic resolution of rac‐indanyl acetate. As it has been previously described that different immobilization protocols may greatly alter lipase features, in this work, CALB was covalently immobilized on epoxy Immobead‐350 (IB‐350) and on glyoxyl‐agarose to ascertain if better kinetic resolution would result. Afterwards, all CALB biocatalysts were utilized in the hydrolytic resolution of rac‐indanyl acetate and rac‐(chloromethyl)‐2‐(o‐methoxyphenoxy) ethyl acetate. After optimization of the immobilization protocol on IB‐350, its loading capacity was 150 mg protein/g dried support. Furthermore, the CALB‐IB‐350 thermal and solvent stabilities were higher than that of the soluble enzyme (e.g., by a 14‐fold factor at pH 5–70°C and by a 11‐fold factor in dioxane 30%–65°C) and that of the glyoxyl‐agarose‐CALB (e.g., by a 12‐fold factor at pH 10–50°C and by a 21‐fold factor in dioxane 30%–65°C). The CALB‐IB‐350 preparation (with 98% immobilization yield and activity versus p‐nitrophenyl butyrate of 6.26 ± 0.2 U/g) was used in the hydrolysis of rac‐indanyl acetate using a biocatalyst/substrate ratio of 2:1 and a pH value of 7.0 at 30°C for 24 h. The conversion obtained was 48% and the enantiomeric excess of the product (e.e._p) was 97%. These values were much higher than the ones obtained with Novozyme 435, 13% and 26% of conversion and e.e.p, respectively. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:878–889, 2018     

Lipase-catalyzed esterification of conjugated linoleic acid with <Emphasis Type="SmallCaps">l</Emphasis>-carnitine in solvent-free system and acetonitrile

Lipase-catalyzed esterification of conjugated linoleic acid (CLA) with l-carnitine in solvent-free system and acetonitrile was studied. Three lipases (Novzym 435, Amamo AY30 and Amano AYS) have been assayed as suitable biocatalysts in the reaction. It was found that Amano AY30 was the most effective biocatalyst in both solvent-free system and acetonitrile. The conversion rate varied from 8.05 to 60.9% in terms of reaction conditions such as the amount of lipase, the presence of water, the amount of molecular sieves and reaction time. The conversions of substrate in solvent-free system were higher than that in acetonitrile. When the substrates were 1 mmol CLA and 1 mmol l-carnitine, the maximum conversion (60.9%) was obtained in solvent-free system with 150 mg lipase AY30, 50% water content and 150 mg molecular sieves at the reaction time of 24 h. A novel CLA ester product was successfully isolated and characterized by ESI-MS and ¹H NMR.     

The atypical lipase B from Candida antarctica is better adapted for organic media than the typical lipase from Thermomyces lanuginosa

Candida antarctica lipase B (CALB) and Thermomyces lanuginosa lipase (TLL) were evaluated as catalysts in different reaction media using hydrolysis of tributyrin as model reaction. In o/w emulsions, the enzymes were used in the free form and for use in monophasic organic media, the lipases were adsorbed on porous polypropylene (Accurel EP-100). In monophasic organic media, the highest specific activity of both lipases was obtained in pure tributyrin at a water activity of >0.5 and at an enzyme loading of 10 mg/g support. With tributyrin emulsified in water, the specific activities were 2780 micromol min(-1) mg(-1) for TLL and 535 micromol min(-1) mg(-1) for CALB. Under optimal conditions in pure tributyrin, CALB expressed 49% of the activity in emulsion (264 micromol min(-1) mg(-1)) while TLL expressed only 9.2% (256 micromol min(-1) mg(-1)) of its activity in emulsion. This large decrease is probably due to the structure of TLL, which is a typical lipase with a large lid domain. Conversion between open and closed conformers of TLL involves large internal movements and catalysis probably requires more protein mobility in TLL than in CALB, which does not have a typical lid region. Furthermore, TLL lost more activity than CALB when the water activity was reduced below 0.5, which could be due to further reduction in protein mobility.     

Enzymatic synthesis of ethyl esters from waste oil using mixtures of lipases in a plug‐flow packed‐bed continuous reactor

This work describes the continuous synthesis of ethyl esters via enzymatic catalysis on a packed‐bed continuous reactor, using mixtures of immobilized lipases (combi‐lipases) of Candida antarctica (CALB), Thermomyces lanuginosus (TLL), and Rhizomucor miehei (RML). The influence of the addition of glass beads to the reactor bed, evaluation of the use of different solvents, and flow rate on reaction conditions was studied. All experiments were conducted using the best combination of lipases according to the fatty acid composition of the waste oil (combi‐lipase composition: 40% of TLL, 35% of CALB, and 25% of RML) and soybean oil (combi‐lipase composition: 22.5% of TLL, 50% of CALB, and 27.5% of RML). The best general reaction conditions were found to be using tert‐butanol as solvent, and the flow rate of 0.08 mL min^?1. The combi‐lipase reactors operating at steady state for over 30 days (720 h), kept conversion yields of ～50%, with average productivity of 1.94 g_{ethyl esters} h^?1, regardless of the type of oil in use. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:952–959, 2018     

Cross-linked enzyme aggregates of recombinant Candida antarctica lipase B for the efficient synthesis of olvanil,a nonpungent capsaicin analogue

Despite the proven therapeutic role of capsaicin in human health, its usage is still hampered by its high pungency. In this sense, nonpungent capsaicin analogues as olvanil are a feasible alternative to the unpleasant sensations produced by capsaicin while maintaining a similar pharmacological profile. Olvanil can be obtained by a lipase-catalyzed chemoenzymatic process. In the present work, recombinant Candida antarctica lipase B (CALB) was expressed in Pichia pastoris and subsequently immobilized by cross-linked enzyme aggregate (CLEA) methodology for the synthesis of olvanil. The CALB-CLEAs were obtained directly from the fermentation broth of P. pastoris without any purification step in order to assess the role of the contaminant proteins of the crude extract as co-feeders. The CALB-CLEAs were also bioimprinted to enhance the catalytic performance in olvanil synthesis. When CALB was precipitated with isopropanol, the obtained CALB-CLEAs exhibited the highest activity in the synthesis of olvanil, regardless of the glutaraldehyde concentration. The maximum product synthesis was found at 72 hr obtaining 6.8 g L⁻¹ of olvanil with a reaction yield of 16%. When CALB was bioimprinted with olvanil, the synthesis was enhanced 1.3 times, reaching 10.7 g L⁻¹ of olvanil at 72 hr of reaction with a reaction yield of 25%. Scanning electron microscopy images indicated different morphologies of the CLEAs depending on the precipitating agent and the template used for bioimprinting. Recombinant CALB-CLEAs obtained directly from the fermentation broth are a suitable alternative to commercial enzymatic preparations for the synthesis of olvanil in organic medium.     

Synthesis of cinnamyl acetate catalysed by highly reusable cotton-immobilized Pseudomonas fluorescens lipase

Cinnamyl acetate as an important fragrance ingredient could be synthesized by lipase-catalysed transesterification in organic systems, but enzyme proteins tended to denature and inactivate for no water lubrication. To improve the non-aqueous stability of lipases, absorbent cotton was taken as an alternative “water” phase to stabilize enzyme proteins. In a mass ratio of 1:1, Pseudomonas fluorescens lipase was immobilized on cotton fibres by physical absorption in a column glass bottle, forming a facile cotton-lipase bioreactor in which the transesterification between cinnamyl alcohol and vinyl acetate processed efficiently. From the molar conversions after reaction for 2?h at 37?°C and 160?rpm, the ability of cotton-lipase to transform substrate was more than 5-folds of native lipase. And even in static state and at 4?°C, the conversion of reaction catalysed by cotton-PFL had 11-fold increase relative to native lipase after 8?h. Recycles showed that the cotton-lipase had an extra-long half-life of activity (t_1/2?=?693?h) and a negligible decay rate in the ability to transform substrate (D_r?=?0.08% h^?1). All these showed that this lipase had been effectively activated and stabilized by cotton fibres for the numerous hydroxyl groups and fluffy structure.     

Esterification degree of fructose laurate exerted by Candida antarctica lipase B in organic solvents

Sugar esters of fatty acids have many applications as biocompatible and biodegradable emulsifiers, which are determined by their degrees of esterification (DE). Direct esterification of fructose with lauric acid in organic media used commercial immobilized Candida antarctica lipase B (CALB) was investigated for DE. Significant difference of DE was observed between 2-methyl-2-butanol (2M2B) and methyl ethyl ketone (MEK), as di-ester/mono-ester molar ratio of 1.05:1 in 2M2B and 2.79:1 in MEK. Fourier transform infrared (FTIR) spectra showed that the secondary structure of the enzyme binding mono-ester presented distinct difference in 2M2B and MEK. Contents of β-turn and antiparallel β-sheet of CALB in 2M2B were 26.9% and 16.2%, respectively, but 19.1% and 13.2% in MEK. To understand the relationship between the conformational changes and differences of DE, mono-ester and fatty acid were directly employed for synthesis of di-ester. The maximum initial velocity of di-ester synthesis in MEK was 0.59 mmol g (enzyme)⁻¹ h⁻¹, which was 2.19-fold as greater as that in 2M2B, indicating that CALB conformation in MEK was preferred for the synthesis of di-ester. These results demonstrated that the conformation of CALB binding mono-ester affected by organic solvents essentially determined DE.     

Kinetic study on the inhibition of xanthine oxidase by acylated derivatives of flavonoids synthesised enzymatically

Studies have reported that flavonoids inhibit xanthine oxidase (XO) activity; however, poor solubility and stability in lipophilic media limit their bioavailability and applications. This study evaluated the kinetic parameters of XO inhibition and partition coefficients of flavonoid esters biosynthesised from hesperidin, naringin, and rutin via enzymatic acylation with hexanoic, octanoic, decanoic, lauric, and oleic acids catalysed by Candida antarctica lipase B (CALB). Quantitative determination by ultra-high performance liquid chromatography–mass spectrometry (UHPLC–MS) showed higher conversion yields (%) for naringin and rutin esters using acyl donors with 8C and 10C. Rutin decanoate had higher partition coefficients (0.95), and naringin octanoate and naringin decanoate showed greater inhibitory effects on XO (IC₅₀ of 110.35 and 117.51?μM, respectively). Kinetic analysis showed significant differences (p?K_m values, whereas the values for V_max were the same, implying the competitive nature of XO inhibition.     

Immobilized CALB Catalyzed Transesterification of Soybean Oil and Phytosterol

Candida antarctica lipase B (CALB) was immobilized on Fe₃O₄/SiO_x-g-P(GMA) polymer carrier to catalyzed the transesterification of soybean oil and phytosterol. The enzyme loading of the obtained particles was 98.7 mg/g supports and the enzyme activity was 1226.5 U/g. The average particle size was 100.5?±?1.30 nm and the magnetization was 15.80 emu/g. The immobilized enzyme showed higher activities at a wider range of pH and temperatures. Its optimum reaction temperature was up to 50 °C; increased by 5 °C compared to the free enzyme. The obtained magnetic immobilized Fe₃O₄/SiO_x-g-P(GMA) lipase was nanoscale. First-grade soybean oils were used as a substrate. System pH was adjusted to 7.0. The optimal reaction temperature was 50 °C and the reaction time was 3 h. The phytosterol concentration of 5% and immobilized CALB of 2% were obtained. The conversion rate of transesterification reaction between soybean oil and phytosterol was 86.2%. The use of magnets can quickly separate the immobilized enzymes from the substrates. The relative activity of the immobilized enzymes was 83.0% when reused seven times. The prepared immobilized CALB can improve efficiently enzyme activity and reutilization.     

Lipase catalysed synthesis of N-trans-feruloyltyramine and a quantitative HPLC-UV method for analysis

Abstract

N-trans feruloyltyramine amide was successfully synthesized from 4-hydroxy-3-methoxycinnamic acid and tyramine hydrochloride in a one-step lipase catalysed reaction. The use of immobilized lipase, lipozyme TL IM as the catalyst in the reaction allowed simple isolation of the enzyme from the products and other components in the reaction mixture. N-feruloyltyramine amide was characterized using Fourier Transform Infrared (FTIR) Spectroscopy, Proton Nuclear Magnetic Resonance (1H NMR) and elemental analysis. Under optimized conditions 93.5% yield was obtained when the process was carried out for 48 h using a molar ratio of cinnamic acid:tyramine HCl, 6:1 at 40°C. In addition, a rapid simple and sensitive HPLC-UV method was developed for the determination of N-feruloyltyramine using an ^®Rp-8 endcapped column. The optimum mobile phase used was acetonitrile:disodium hydrogen phosphate, 30:70(v/v.). N-feruloyltyramine amide was detected at a retention time of 12 min. The calibration curve was linear over the range of 5.27–12.30 × 10^?4 M with correlation factor r =?0.9958. Consequently, the method was considered valid for quantitative analysis samples of N-trans-feruloyltyramine amide.     

Highly regioselective enzymatic synthesis of 5′-O-stearate of 1-β-D-arabinofuranosylcytosine in binary organic solvent mixtures

In this paper, highly regioselective enzymatic acylations of 1-β-D-arabinofuranosylcytosine (ara-C) with vinyl stearate (VS) in binary organic solvents were explored for the preparation of 5′-O-stearate of ara-C with potential antitumor activity. Twelve kinds of hydrolases were tested for the regioselective acylation reaction and the immobilized Candida antarctica lipase B (Novozym 435) showed the highest regioselectivity (>99.9%) towards the 5′-OH of ara-C. A comparative study showed that the lipase had much higher catalytic activity in the binary mixture of hexane and pyridine than in other tested co-solvent systems. To better understand lipase-mediated acylation conducted in the best binary organic solvent system, the effects of hydrophobic solvent content, molar ratio of VS to ara-C, initial water activity, and reaction temperature on the acylation reaction were studied. It was found that the most suitable hexane content, VS–ara-C molar ratio, initial water activity, and reaction temperature were shown to be 25% (v/v), 20:1, 0.07, and 50°C, respectively. Under these reaction conditions, the initial reaction rate, the maximum substrate conversion, and regioselectivity were as high as 86.0 mmol·L⁻¹h⁻¹, 96.6%, and >99.9%, respectively. The product of Novozym 435-catalyzed acylation was characterized by Carbon-13(¹³C) NMR and confirmed to be 5′-O-stearate of ara-C.