The kinetic study on lipase-catalyzed transesterification of α-cyano-3-phenoxybenzyl alcohol in organic media

Optically active form of α-cyano-3-phenoxybenzyl alcohol (CPBA), building block of pyrethroid insecticides, was synthesized as its acetate by the combination of anion-exchange resin-catalyzed transcyanation between m-phenoxybenzaldehyde and acetone cyanohydrin, and lipase-catalyzed enantioselective transesterification of the resulting cyanohydrin with vinyl acetate. Through a screening of enzymes, Alcaligenes sp. lipase showed the highest activity and the conversion exceeded 50%. Effects of solvents and temperatures on this reaction were studied. Among four kinds of solvent, diisopropyl ether was a best choice. The optimal temperature was 50 °C. Although the external diffusion limitation could be excluded by raising the rotational speed, internal diffusion could not be ignored, since the enzyme was an immobilized one on the particles with a considerably large diameter. The e.e. values of CPBA ester were measured by polarimeter and NMR.     

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.     

Improved activity and stability of Rhizopus oryzae lipase via immobilization for citronellol ester synthesis in supercritical carbon dioxide

In present work, Rhizopus oryzae lipase immobilized on a film prepared using blend of hydroxylpropyl methyl cellulose (HPMC) and polyvinyl alcohol (PVA) was investigated for synthesis of citronellol esters with supercritical carbon dioxide (Sc-CO₂) as a reaction medium. The transesterification reaction was optimized for various reaction parameters like effect of molar ratio, acyl donor, time, temperature, enzyme concentration, effect of pressure and co-solvent to achieve the maximum yield of desired product. The results obtained signify remarkable increment (about eightfold) in the yield of citronellol acetate (91%) as compared to that of free lipase (11%) in Sc-CO₂. The developed biocatalytic methodology provides a substantial advantage of low biocatalyst loading (1.5%, w/v), lower reaction temperature (45 °C) and lower pressure (8 MPa) as compared to previous reports. The immobilization method has significantly enhanced the operational stability of lipase for ester synthesis under Sc-CO₂ conditions. The developed methodology was successfully applied for synthesis of three different industrially important citronellol esters namely citronellol acetate (91%), citronellol butyrate (98%), citronellol laurate (99%) with excellent yields using vinyl esters as acyl donor under Sc-CO₂ conditions. In addition, the immobilized biocatalyst was effectively recycled for three consecutive recycles.     

Biosynthesis of sucrose-6-acetate catalyzed by surfactant-coated Candida rugosa lipase immobilized on sol–gel supports

Sucrose-6-acetate is an important intermediate in the preparation of sucralose (a finest sweetener). In our study, Candida rugosa lipase coated with surfactant was firstly immobilized on sol–gel supports. Then, the immobilized enzyme was used in the regioselective synthesis of sucrose-6-acetate by transesterification of sucrose and vinyl acetate. The screening results revealed that Tween 80 was an ideal surfactant to coat lipase immobilized in sol–gel and exhibited the highest yield of sucrose-6-acetate. Other factors that influenced the yield during the preparation process were also studied. Under optimal conditions, the yield of sucrose-6-acetate could reach up to 78.68 %, while free lipase was easily inactivated in polar solvent. Thermal and operational stabilities were also improved significantly. Surfactant-coated lipase immobilized in sol–gel remained stable when the temperature was higher than 60 °C. Moreover, they could maintain high catalytic activity after six recycles. This strategy is economical, convenient and promising for the food industry.     

Lipase‐Catalyzed Kinetic Resolution of (±)‐1‐(2‐Furyl) Ethanol in Nonaqueous Media

S‐1‐(2‐Furyl) ethanol serves as an important chiral building block for the preparation of various natural products, fine chemicals, and is widely used in the chemical and pharmaceutical industries. In this work, lipase‐catalyzed kinetic resolution of (R/S)‐1‐(2‐furyl) ethanol using different acyl donors was investigated. Vinyl esters are good acyl donors vis‐à‐vis alkyl esters for kinetic resolution. Among them, vinyl acetate was found to be the best acyl donor. Different immobilized lipases such as Rhizomucor miehei lipase, Thermomyces lanuginosus lipase, and Candida antarctica lipase B were evaluated for this reaction, among which C. antarctica lipase B, immobilized on acrylic resin (Novozym 435), was found to be the best catalyst in n‐heptane as solvent. The effect of various parameters was studied in a systematic manner. Maximum conversion of 47% and enantiomeric excess of the substrate (ee_s) of 89% were obtained in 2 h using 5 mg of enzyme loading with an equimolar ratio of alcohol to vinyl acetate at 60°C at a speed of 300 rpm in a batch reactor. From the analysis of progress curve and initial rate data, it was concluded that the reaction followed the ordered bi–bi mechanism with dead‐end ester inhibition. Kinetic parameters were obtained by using nonlinear regression. This process is more economical, green, and easily scalable than the chemical processes. Chirality 26:286–292, 2014. © 2014 Wiley Periodicals, Inc.     

A spectrophotometric transesterification-based assay for lipases in organic solvent

A new method to evaluate lipase activities in nonaqueous conditions using vinyl ester absorbance at ultraviolet (UV) wavelengths is described. The model reaction is the transesterification between vinyl stearate and pentanol in hexane at 30 °C or in decane at 50 °C. The conversion of vinyl stearate into pentyl stearate is monitored through decreasing UV absorbance at 200 nm. Six commercial lipases were tested with this method, and results were compared with gas chromatography (GC) quantification and a classical spectrophotometric method using p-nitrophenyl palmitate. Results from the new spectrophotometric assay are similar both to results from GC quantification (R² = 0.999) and to results from p-nitrophenyl palmitate (R² = 0.989). The proposed method is able to evaluate both high activity from immobilized lipases such as immobilized Candida antarctica B lipase (3060 ± 350 U g⁻¹) and low activity from crude enzymatic extracts such as Carica papaya dried latex (0.1 ± 0.04 U g⁻¹). The method has also been used to measure kinetic parameters of C. antarctica B lipase for vinyl stearate and the correlation between its synthesis activity and its concentration. The method has also proved to be effective in studying the acyl selectivity of a lipase by comparing its activities with increasing chain lengths of vinyl esters.     

Kinetic modeling of immobilized-lipase catalyzed transesterification of n-octanol with vinyl acetate in non-aqueous media

Organic esters are employed as solvents, fragrance, flavors, and precursors in a variety of industries. Particularly, aliphatic esters are greatly used in flavor industry, mainly as fixatives and modifiers, and aromatic esters in fragrance compositions. Esters are produced by a variety of methods among which esterification and transesterification with acid catalysts under reflux conditions are prominent. The use of biocatalysts provides an opportunity for carrying out reactions under milder conditions leading to better quality products suitable in fragrance and flavor industry. Transesterification of n-octanol with vinyl acetate was studied at 30 °C as a model reaction by employing different lipases as catalysts such as Psedomonas species lipase immobilized on diatomite, free Candida rugosa lipase. Novozym 435 (lipase B from Candida antarctica; immobilized on macro-porous polyacrylic resin beads) and Lipozyme IM 20 (Mucor miehei lipase immobilized on anionic resin). Novozym 435 was found to be the most active catalyst in heptane as a solvent. A conversion of 82% with 100% selectivity of n-octyl acetate was obtained at 30 °C in 90 min using equimolar quantities of the reactants with 0.833 g l⁻¹ of Novozym 435. Transesterification of other alcohols such as n-decanol, benzyl alcohol, cinnamyl alcohol, 2-ethyl-1-hexanol, 1-phenyl ethyl alcohol, and 2-phenyl ethyl alcohol was also studied with vinyl acetate. The analysis of the initial rate data and progress curve data showed that the reaction obeys the ternary complex bi–bi mechanism with inhibition by n-octanol. The experimental and theoretical values matched very well.

The order of transesterification reactivity of vinyl acetate with various alcohols in presence of Novozym 435 under otherwise identical conditions at 30 °C was found to be as follows:

n-octanol>n-decanol>benzylalcohol>cinnamylalcohol>2-ethyl-1-hexanol>2-phenylethylalcohol>1-phenylethylalcohol.

     

Efficient regioselective acylation of andrographolide catalyzed by immobilized Burkholderia cepacia lipase

For the first time, PSL-C, an immobilized lipase from Burkholderia cepacia, was successfully applied to the regioselective acylation of andrographolide by vinyl acetate in acetone. FT-IR spectra demonstrated the occurrence of acylation reaction. The ¹³C NMR, ESI-MS and elemental analysis confirmed that the 14-acetylandrographolide was formed exclusively. Water activity and reaction temperature had a significant effect on the initial rate and the substrate conversion, but little effect on the regioselectivity of the reaction. The optimal water activity and reaction temperature were 0.11 and 50 °C, respectively. Under these conditions, the initial rate and substrate conversion were 50.2 mM h⁻¹ and 99.0%, respectively, after a reaction time of around 4 h. Besides, immobilized lipase also displayed higher operational stability and 83.5% of its original activity was maintained after being reused for eight batches.     

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.     

Immobilization of Pseudomonas cepacia lipase onto electrospun polyacrylonitrile fibers through physical adsorption and application to transesterification in nonaqueous solvent

The lipase of Pseudomonas cepacia was immobilized onto electrospun polyacrylonitrile (PAN) fibers and used for the conversion of (S)-glycidol with vinyl n-butyrate to glycidyl n-butyrate in isooctane. The rate of reaction with the adsorbed lipase was 23-fold higher than the initial material. After 10 recyclings, the initial reaction rate was 80% of the original rate. This system of enzyme immobilization is therefore suitable for carrying out transesterification reactions in nonaqueous solvents.     

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.     

Geranyl acetate synthesis catalyzed by Thermomyces lanuginosus lipase immobilized on electrospun polyacrylonitrile nanofiber membrane

Isolated Thermomyces lanuginosus lipase (TLL) was immobilized by different protocols on the polyacrylonitrile nanofibers membrane. The conditions for immobilization of TLL were optimized by investigating effect of protein concentration, time and temperature on the extent of immobilization. The effect of immobilization on the catalytic activity and stability of lipase was studied thoroughly. The immobilized TLL was used as biocatalyst for geranyl acetate synthesis with geraniol and vinyl acetate as substrates and their performance was compared with free enzyme. The TLL immobilized by physical adsorption shows higher transesterification and hydrolytic activities than that of covalently linked or native TLL. There was 32 and 9 fold increase in transesterification activity of TLL immobilized by adsorption and covalent bonding, while hydrolytic activity increases only by 3.6 and 1.8 fold respectively. The optimum conditions for immobilization in both the cases were immobilization time 90–150 min, temperature 45 °C and protein concentration of 2 mg/ml. The percentage conversion of ester was more than 90% and 66% in case of physically adsorbed and covalently bonded enzyme respectively as compared to native one. However, covalently immobilized TLL shows higher operational stability than native and physically adsorbed TLL.     

Immobilized Pseudomonas sp. lipase: A powerful biocatalyst for asymmetric acylation of (±)-2-amino-1-phenylethanols with vinyl acetate

Pseudomonas sp. lipase was immobilized onto glutaraldehyde-activated Florisil^® support via Schiff base formation and stabilized by reducing Schiff base with sodium cyanoborohydride. The immobilization performance was evaluated in terms of bound protein per gram of support (%) and recovered activity (%). A 4-factor and 3-level Box–Behnken design was applied for the acylation of (±)-2-(propylamino)-1-phenylethanol, a model substrate, with vinyl acetate and the asymmetric acylations of other (±)-2-amino-1-phenylethanols with different alkyl substituents onto nitrogen atom such as (±)-2-(methylamino)-1-phenylethanol, (±)-2-(ethylamino)-1-phenylethanol, (±)-2-(butylamino)-1-phenylethanol and (±)-2-(hexylamino)-1-phenylethanol were performed under the optimized conditions. The optimal conditions were bulk water content of 1.8%, reaction temperature of 51.5 °C, initial molar ratio of vinyl acetate to amino alcohol of 1.92, and immobilized lipase loading of 47 mg mL^?1. (R)-enantiomers of tested amino alcohols were preferentially acylated and the reaction purely took place on the hydroxyl group of 2-amino-1-phenylethanols. The increase of alkyl chain length substituted onto nitrogen atom caused an increase in the acylation yield and ee values of (S)-enantiomers. Enantiomeric ratio values were >200 for all the reactions. Our results demonstrate that the immobilized lipase is a promising biocatalyst for the preparation of (S)-2-amino-1-phenylethanols and their corresponding (R)-esters via O-selective acylation of (±)-2-amino-1-phenylethanols with vinyl acetate.     

Kinetic modelling of the production of methyl oleate by Celite® supported lipase sol–gels

This study illustrates the benefits of Celite^® supported lipase sol–gels for the transesterification of triolein to produce methyl oleate. A ping–pong bi–bi kinetic model was developed and validated taking into account the inhibition effects of methanol and glycerol as well as the effect of temperature. Although initial reaction rate models are useful for predicting the kinetics in the absence of products, a kinetic model beyond the initial conditions that considers glycerol inhibition is important. The model developed was consistent with the experimental data (R² = 0.95) predicting an increase in methyl oleate production with increasing methanol concentration up to an optimal range of 1.3 M to 2.0 M depending on the temperature. In general, increasing the temperature increased the initial reaction rate for the immobilized lipase over the temperature range of 40–60 °C. Based on the kinetic constants, the maximum velocity of the reverse reaction is about 25% slower than that of the forward reaction and glycerol inhibition has a more significant effect on the reaction kinetics than methanol inhibition. The model developed would be useful for understanding the effects of methanol and glycerol inhibition as well as temperature on the production of methyl oleate using lipase-mediated enzymatic transesterification.     

Purification and Characterization of a DNA Topoisomerase I from Bifidobacterium breve

The monoacylation of (η⁶-1,2-benzenedimethanol)tricarbonylchromium (2) by vinyl acetate, palmitate and benzoate, alcoholysis of the corresponding diesters of 2 in n-butanol, and acylation of (η⁶-benzyl alcohol) tricarbonylchromium by (±)-vinyl 2-phenoxypropanoate and 2-phenylpropanoate were accomplished with lipase P (from P. fluorescens) and lipase CC (from C. cylindracea) to give optically active organometallic esters. Their configurations indicated that the stereoselectivity of each of these two lipases was in marked contrast. An active site model for them is proposed.     

Kinetics of enzymatic transesterification and thermal deactivation using immobilized Burkholderia lipase as catalyst

The most effective way of enzymatic synthesis of biodiesel is through lipase-catalyzed transesterification, while its performance and economic feasibility should still be improved. In this study, lipase produced by an isolated Burkholderia sp. was immobilized on microsize Celite materials functionally modified with long alkyl groups. The specific activity of the immobilized lipase was 1,154 U/g. The methanolysis of olive oil catalyzed by the immobilized lipase obeyed Ping Pong Bi Bi model with an estimated V _max, K _m,TG, K _m,M and K _i,M value of 0.61 mol/(L min), 7.93 mol/L, 1.01 mol/L, and 0.24 mol/L, respectively. The activation energy of the enzymatic reaction is estimated as 15.51 kJ/mol. The immobilized lipase exhibits high thermal stability with thermal deactivation energy of 83 kJ/mol and a long half-life. The enthalpy, Gibb’s free energy, and entropy of the immobilized lipase were in the range of 80.02–80.35 kJ/mol, 88.35–90.13 kJ/mol, and ?28.22 to ?25.11 J/(mol K), respectively.     

Improvement of activity and stability of Rhizomucor miehei lipase by immobilization on nanoporous aluminium oxide and potassium sulfate microcrystals and their applications in the synthesis of aroma esters

In this study, Rhizomucor miehei lipase (RML) was immobilized on the hexagonally-ordered nanoporous aluminium oxide membranes (RML-Al₂O₃-NP) by adsorption and as protein-coated microcrystals (RML-PCMCs) by simultaneously precipitating RML on micron-sized potassium sulfate crystals (K₂SO₄) in pre-chilled acetone. The hydrolytic activities of immobilized lipase preparations were investigated in terms of p-nitrophenyl palmitate hydrolysis and their esterification activities were examined for the synthesis of some aroma esters such as butyl acetate, isoamyl acetate, hexyl acetate, heptyl acetate, and geranyl acetate. The immobilization yields were 33.8 and 25.1%, respectively for RML immobilized on Al₂O₃-NP membranes and potassium sulfate crystals. The catalytic efficiency ratios of RML-Al₂O₃-NP and RML-PCMCs were 2.3- and 3.9-fold higher than that of the free lipase, respectively in terms of hydrolytic activity. The free lipase was stabilized as 4.1- and 10.5-fold, respectively at 40 and 50?°C when immobilized on Al₂O₃-NP. The corresponding stabilization factors were 4.6- and 12.8-fold higher for RML-PCMCs. RML-Al₂O₃-NP and RML-PCMCs maintained 84 and 86% of their initial hydrolytic activities, respectively after 10 reuses. Of the synthesized aroma esters, the highest yield was obtained for the geranyl acetate. After 4?h reaction time, no geraniol was detected in the preparative-scale (196?g/L) synthesis of geranyl acetate for both the immobilized lipases when the initial geraniol amount, vinyl acetate amount, RML-PCMCs amount, and reaction temperature values were 1?mmol, 3?mmol, 100?mg (or 300?mg RML-Al₂O₃-NP), and 50?°C, respectively. These results show that the immobilization of R. miehei lipase by adsorption on nanoporous aluminium oxide and as protein-coated microcrystals leads to the obtention of highly stable, catalytically more active, and reusable lipase preparations.     

A sensitive colorimetric high-throughput screening method for lipase synthetic activity assay

A sensitive and practical high-throughput screening method for assaying lipase synthetic activity is described. Lipase-catalyzed transesterification between vinyl acetate and n-butanol in n-hexane was chosen as a model reaction. The released acetaldehyde was determined by the colorimetric method using 3-methyl-2-benzothialinone (MBTH) derivatization. In comparison with other methods, the major advantages of this process include high sensitivity, simple detection, inexpensive reagents, and low requirements for instruments.     

Kinetics of lipase recovery from the aqueous phase of biodiesel production by macroporous resin adsorption and reuse of the adsorbed lipase for biodiesel preparation

A commercial macroporous resin (D3520) was screened for lipase recovery by adsorption from the aqueous phase of biodiesel production. The influences of several factors on the adsorption kinetics were investigated. It was found that the kinetic behavior of lipase adsorption by macroporous resin could be well described by pseudo-first-order model. Temperature had no significant effects on lipase adsorption, while resin-to-protein ratio (R) significantly affected both rate constant (k₁) and equilibrium adsorption capacity (Q_e). No lipase was adsorbed when mixing (shaking) was not performed; however, protein recovery reached 98% after the adsorption was conducted at 200 rpm for 5 h in a shaker. The presence of methanol and glycerol showed significant negative influence on lipase adsorption kinetics. Particularly, increasing glycerol concentration could dramatically decrease k₁ but not impact Q_e. Biodiesel was found to dramatically decrease Q_e even present at a concentration as low as 0.02%, while k₁ was found to increase with biodiesel concentration. The adsorbed lipase showed a relatively stable catalytic activity in tert-butanol system, but poor stability in solvent-free system when used for biodiesel preparation. Oil and biodiesel were also found to adsorb onto resin during transesterification in solvent-free system. Therefore, the resin had to be washed by anhydrous methanol before re-used for lipase recovery.     

Application of a Burkholderia cepacia lipase-immobilized silica monolith micro-bioreactor to continuous-flow kinetic resolution for transesterification of (R, S)-1-phenylethanol

Burkholderia cepacia lipase was immobilized in silicates forming from n-butyl-substituted precursors within a silica monolith from methyl-substituted precursors. The resultant preparation gave about 12 times higher rates of transesterification of (R, S)-1-phenylethanol with vinyl acetate and an approximately two-fold increase in the enantioselectivity toward (R)-1-phenylethanol, as compared to a non-immobilized counterpart. The highest enzymatic activity and enantioselectivity (reaching 250) were found at a low water activity of 0.11. The continuous-flow kinetic resolution of (R, S)-1-phenylethanol was successfully conducted using lipase-immobilized silica monolith micro-bioreactors with various inside diameters ranging from 0.25 to 1.6 mm. The reactor performance during continuous operation was consistent with the prediction from the batch reactor. A steady state conversion of 40% and enantiomeric excess more than 98% were maintained over a time period of 15 days.