Solvent-free synthesis of glyceryl ferulate using a commercial microbial lipase

A process was optimized for the enzymatic synthesis of glyceryl ferulate with a yield of up to 96% using a vacuum-rotary evaporation strategy under following conditions: 15 mmol glycerol, 1.5 mmol ethyl ferulate, 170 mg Candida antarctica lipase, at 60°C for 10 h and under a vacuum of 10 mm Hg. The immobilized lipase can be used 10 times.     

Enzymatic conversion of sunflower oil to biodiesel in a solvent-free system: Process optimization and the immobilized system stability

The feasibility of using the commercial immobilized lipase from Candida antarctica (Novozyme 435) to synthesize biodiesel from sunflower oil in a solvent-free system has been proved. Using methanol as an acyl acceptor and the response surface methodology as an optimization technique, the optimal conditions for the transesterification has been found to be: 45 ^oC, 3% of enzyme based on oil weight, 3:1 methanol to oil molar ratio and with no added water in the system. Under these conditions, >99% of oil conversion to fatty acid methyl ester (FAME) has been achieved after 50 h of reaction, but the activity of the immobilized lipase decreased markedly over the course of repeated runs. In order to improve the enzyme stability, several alternative acyl acceptors have been tested for biodiesel production under solvent-free conditions. The use of methyl acetate seems to be of great interest, resulting in high FAME yield (95.65%) and increasing the half-life of the immobilized lipase by about 20.1 times as compared to methanol. The reaction has also been verified in the industrially feasible reaction system including both a batch stirred tank reactor and a packed bed reactor. Although satisfactory performance in the batch stirred tank reactor has been achieved, the kinetics in a packed bed reactor system seems to have a slightly better profile (93.6 ± 3.75% FAME yield after 8–10 h), corresponding to the volumetric productivity of 48.5 g/(dm³ h). The packed bed reactor has operated for up to 72 h with almost no loss in productivity, implying that the proposed process and the immobilized system could provide a promising solution for the biodiesel synthesis at the industrial scale.     

Chemometric analysis of lipase-catalyzed synthesis of xylitol esters in a solvent-free system

Immobilized Candida antarctica lipase B-catalyzed esterification of xylitol and two fatty acids (capric and caproic acid) were studied in a solvent-free system. The Taguchi orthogonal array method based on three-level-four-variables with nine experiments was applied for the analysis and optimization of the reaction parameters including time, substrate molar ratio, amount of enzyme, and amount of molecular sieve. The obtained conversion was higher in the esterification of xylitol and capric acid with longer chain length. The optimum conditions derived via the Taguchi approach for the synthesis of xylitol caprate and xylitol caproate were reaction time, 29 and 18 h; substrate molar ratio, 0.3 and 1.0; enzyme amount, 0.20 and 0.05 g, and molecular sieve amount of 0.03 g, respectively. The good correlation between the predicted conversions (74.18% and 61.23%) and the actual values (74.05% and 60.5%) shows that the model derived from the Taguchi orthogonal array can be used for optimization and better understanding of the effect of reaction parameters on the enzymatic synthesis of xylitol esters in a solvent-free system.     

Modelling and experimental studies on lipase-catalyzed isoamyl acetate synthesis in a microreactor

A lipase-catalyzed synthesis of isoamyl acetate was studied in a continuously operated pressure-driven microreactor. The esterification of isoamyl alcohol and acetic acid occurred at the interface between n-hexane and an aqueous phase with dissolved lipase B from Candida antarctica. By adjusting flow rates of both phases, a parallel laminar flow with liquid–liquid boundary in the middle of the microchannel could be reestablished and a separation of phases was achieved at the y-shaped exit of the microreactor. Since product remained in the organic phase, this also enabled its continuous separation from the aqueous phase with the enzyme. A three-dimensional mathematical model was developed, considering the velocity profile developed for steady-state conditions between two immiscible fluids. The model contained convection, diffusion, and enzyme reaction terms, where esterification rate was described with a Ping-Pong Bi-Bi mechanism and inhibition by both substrates. Experimental data, which were in good agreement with model simulations, have demonstrated 35% conversion at residence time 36.5 s at 45 °C and at 0.5 M acetic acid and isoamyl alcohol inlet concentrations, which is much faster as in any literature reported so far. According to model simulations, obtained by non-equidistant finite differences numerical solutions of complex non-linear equations system, further microreactor design and process optimization are feasible.     

Enzymatic synthesis of trieicosapentaenoylglycerol in a solvent-free medium

The enzymatic synthesis of trieicosapentaenoylglycerol from glycerol and eicosapentaenoic ethyl ester in a solvent-free medium is studied here. Novozym SP 435 (immobilized lipase from Candida antarctica) has appeared as a very efficient biocatalyst for this transesterification. A nitrogen bubbling has allowed a good mixing and also the shifting of the reaction toward synthesis by eliminating the ethanol formed. The effect of temperature and of the quantity of lipase has been studied. In the optimal conditions (T=80°C, 5% (w/w) of lipase, 1 mol glycerol for 3 mol ethyl ester), pure triglyceride has been obtained after 10 h.     

Optimized lipase-catalyzed synthesis of adipate ester in a solvent-free system

Immobilized Candida antarctica lipase-catalyzed esterification of adipic acid and oleyl alcohol was investigated in a solvent-free system (SFS). Optimum conditions for adipate ester synthesis in a stirred-tank reactor were determined by the response surface methodology (RSM) approach with respect to important reaction parameters including time, temperature, agitation speed, and amount of enzyme. A high conversion yield was achieved using low enzyme amounts of 2.5% w/w at 60°C, reaction time of 438 min, and agitation speed of 500 rpm. The good correlation between predicted value (96.0%) and actual value (95.5%) implies that the model derived from RSM allows better understanding of the effect of important reaction parameters on the lipase-catalyzed synthesis of adipate ester in an organic solvent-free system. Higher volumetric productivity compared to a solvent-based system was also offered by SFS. The results demonstrate that the solvent-free system is efficient for enzymatic synthesis of adipate ester.     

Enzymatic synthesis of short-chain diacylated alkylglycerols: A kinetic study

Lipase-catalyzed transesterification of 1-O-octadecyl glycerol (batyl alcohol) with ethyl butyrate has been studied. The effect of vacuum on the rate of both transesterification and distillation of ethyl butyrate has also been investigated and at different reaction conditions, more than 85% of 1-O-octadecyl glycerol was consumed in only 5 min giving rise to the monoester. Then the monoester is again acylated to produce the diesterified product. In addition, the transesterification reactions were effected in solvent free reaction medium and it has been scaled-up to produce up to ca. 500 g of 2,3-dibutyroil-1-O-alkylglycerols in three consecutive cycles reutilizing the same batch of lipase. An efficient evaporation of ethanol was necessary to significantly reduce the reaction times of the transesterification reaction. Finally, a kinetics model describing both the rate of transesterification and the rate of inactivation of the immobilized lipase has been developed. The results indicate that the operational stability of the immobilized lipase confined into the mesh baskets (according to the value of k_d attained), was very high and that provides a half-life of the lipase higher than 1500 h.The present procedure is intended to be used for the synthesis of homogeneous alkylglycerols with biological activities and/or precursors of structured alkylglycerols.     

Relationship between lipase production and pseudomycelia formation in a dimorphicCandida sp.

Nitrilotriacetic acid, octanol, hexanol, xylene, naphthalene and camphor increased the lipase production and the formation of mycelia by 10 to 50% and 10 to 27% respectively in a dimorphicCandida sp. Ni²⁺, Ca²⁺, Co²⁺, Cr³⁺ and SeO^2- ₃ ions enhanced lipase production and mycelia formation by 16 to 53% and 13 to 23% respectively.     

Enzymatic synthesis of water-soluble derivatives of salicylic acid in organic media

A novel enzymatic method for preparing water-soluble derivatives of salicylic acid catalyzed by immobilized lipase was described. This study is the first to describe the enzymatic transesterification of methyl salicylate in organic solvents with different hydroxyl donors. The acyl-transfer between methyl salicylate and sorbitol was best supported by solvents of log P values –0.33 to 1.4. With Candida antarctica lipase in tert-amyl alcohol, a sorbitol conversion yield of 98% can be obtained by transesterification with sorbitol and methyl salicylate in one step.     

Lipase-catalysed synthesis of olvanil in organic solvents

The release rate of vanillylamine from its hydrochloride salt was the limiting step in the lipase-catalysed synthesis of olvanil, a capsaicin analogue amide, in organic solvents. When the tertiary amine base concentration (N,N-diisopropylethylamine) was increased from 20 mM to 360 mM, the initial rate of amide synthesis increased proportionally. At a 12 molar excess of N,N-diisopropylethylamine and 30 min of preincubation, both the initial rate and total conversion were the same as those with free vanillylamine (80% conversion in 20 h). This result was independent of the organic solvent used. It is also shown that N,N-diisopropylethylamine does not enhance lipase activity.     

Improvement of the enzymatic synthesis of ethyl valerate by esterification reaction in a solvent system

The present study reports the improved enzymatic synthesis of ethyl valerate (green apple flavor) by esterification reaction of ethanol and valeric acid in heptane medium. Lipase from Thermomyces lanuginosus (TLL) was immobilized by physical adsorption on polyhydroxybutyrate (PHB) particles and used as a potential biocatalyst. The effect of certain parameters that influence the ester synthesis was evaluated by factorial design. The experimental conditions that maximized the synthesis of ethyl valerate were 30.5°C, 18% m/v of biocatalyst (TLL–PHB), absence of molecular sieves, agitation of 234?rpm, and 1,000?mM of each reactant (ethanol and valeric acid). Under these conditions, conversion percentage ≈92% after 105?min of reaction was observed. Soluble TLL was also used as biocatalyst and the highest conversion was of 82% after 120?min of reaction. Esterification reaction performed in a solvent-free system exhibited conversion of 13% after 45?min of reaction catalyzed by immobilized lipase, while the soluble lipase did not exhibit catalytic activity. The synthesis of the ester was confirmed by Fourier transform infrared spectroscopy and gas chromatography–mass spectrometry analyses. After six consecutive cycles of ethyl valerate synthesis, the prepared biocatalyst retained ≈86% of its original activity.     

Enzymatic production of enantiopure ketoprofen in a solvent-free two-phase system

Enzymatic hydrolysis conducted in a medium composed of solely substrate is considered to resolve racemic ketoprofen esters. In a system composed of two components, the pure liquid substrate (organic phase) and water (aqueous phase), hydrolysis products can be efficiently removed from the reaction mixtures. Accordingly, in this study we designed a solvent-free two-phase system for the enantioselective enzymatic hydrolysis of ketoprofen esters. In order to further optimize this system, the influences of various factors, such as the pH of the aqueous phase, temperature, enzyme content, and the alcohol chain length of esters, were examined on conversion and enantiomeric excess. 1N NaHCO₃ was identified as the most efficient aqueous phase for the extraction of ketoprofen. Changes in the amount of enzyme did not significantly affect the maximum conversion or the enantiomeric excess. On the other hand, ketoprofen esters with shorter alcohol chains displayed higher initial reaction rates and conversions in solventless media. In the case of ketoprofen propyl ester, for example, the productivity of the solvent-free two-phase system was about 10–100 times higher than that obtained to date for ketoprofen esterification with alcohols in organic solvents. The enantioselectivities obtained in solvent-free media were similar to those obtained for the enantioselective esterification of ketoprofen in organic solvents.     

Continuous synthesis of alkyl ferulate by immobilized Candida antarctica lipase at high temperature

1-Pentyl, 1-hexyl and 1-heptyl ferulates were continuously synthesized at 60–90°C using a reactor system in which a column packed with ferulic acid powders and another column packed with immobilized Candida antarctica lipase particles were connected in series. Conversions greater than 0.9 were achieved for the synthesis of the 1-hexyl and 1-heptyl ferulates at 90°C. The system could be stably operated for the 1-heptyl ferulate synthesis at 90°C for at least two weeks.     

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.     

Stereochemistry of a diastereoisomeric amphiphile and the species of the lipase influence enzyme activity in the transesterification catalyzed by a lipase-co-lyophilizate with the amphiphile in organic media

Modified Candida rugosa and Pseudomonas cepacia lipase (CRL and PCL) were co-lyophilized with two pairs of synthetic diastereoisomeric amphiphiles, d- and l-2-(2,3,4,5,6-pentahydroxy-hexanoylamino)-propyl]-carbamoyl-propionylamino)-pentanedioic acid didodecyl ester (d- and l-BIG2C₁₂CA); d- and l-2-(2,3,4,5,6-pentahydroxy-hexanoylamino)-pentanedioic acid didodecyl ester (d- and l-2C₁₂GE). Enzyme activities of the modified lipase in the transesterification in organic solvent were evaluated. Both pairs of the diastereoisomeric amphiphiles showed enhanced enzyme activity in the transacetylation between racemic sulcatol and isopropenyl acetate in diisopropyl ether, catalyzed by the PCL-co-lyophilizate, by 19–48 fold when compared to the native lipase lyophilized from buffer alone independent of the stereochemistry of the amphiphiles, while in the case of the CRL-co-lyophilizate only the l-BIG2C₁₂CA showed enhanced enzyme activity in the transbutyrylation between racemic solketal and vinyl butyrate in cyclohexane as high as 68–78 fold.     

Preparation of a whole-cell biocatalyst of mutated <Emphasis Type="Italic">Candida antarctica</Emphasis> lipase B (mCALB) by a yeast molecular display system and its practical properties

To prepare a whole-cell biocatalyst of a stable lipase at a low price, mutated Candida antarctica lipase B (mCALB) constructed on the basis of the primary sequences of CALBs from C. antarctica CBS 6678 strain and from C. antarctica LF 058 strain was displayed on a yeast cell surface by α-agglutinin as the anchor protein for easy handling and stability of the enzyme. When mCALB was displayed on the yeast cell surface, it showed a preference for short chain fatty acids, an advantage for producing flavors; although when Rhizopus oryzae lipase (ROL) was displayed, the substrate specificity was for middle chain lengths. When the thermal stability of mCALB on the cell surface was compared with that of ROL on a cell surface, T _1/2, the temperature required to give a residual activity of 50% for heat treatment of 30 min, was 60°C for mCALB and 44°C for ROL indicating that mCALB displayed on cell surface has a higher thermal stability. Furthermore, the activity of the displayed mCALB against p-nitrophenyl butyrate was 25-fold higher than that of soluble CALB, as reported previously. These findings suggest that mCALB-displaying yeast is more practical for industrial use as the whole-cell biocatalyst.     

The mechanism of solvent effect on the positional selectivity of Candida antarctica lipase B during 1,3-diolein synthesis by esterification

We investigated the influence of solvent on the positional selectivity of Novozym 435 which was the immobilized Candida antarctica lipase B (CALB) during the esterification of oleic acid with glycerol for 1,3-diolein preparation previously. Herein, molecular modeling was used to elucidate the underlying mechanism of the solvent effect on the positional selectivity of the enzyme. The results showed that the binding energy of sn-1 hydroxyl of glycerol molecular with CALB became higher, and the binding energy of sn-2 hydroxyl of glycerol molecular with CALB became lower along with the increase of the solvent log P. It was demonstrated that, increasing log P of the solvent, the enzyme selectivity to sn-1 hydroxyl of glycerol molecular grew weaker, and the selectivity to sn-2 hydroxyl of glycerol molecular grew stronger.     

Molecular modeling of substrate selectivity of Candida antarctica lipase B and Candida rugosa lipase towards c9, t11- and t10, c12-conjugated linoleic acid

Molecular modeling was used to clarify the mechanism of the selectivity of Candida antarctica lipase B and Candida rugosa lipase towards cis9, trans11 (c9, t11-) and trans10, cis12 (t10, c12-) conjugated linoleic acid. Hydrogen bonds network, substrate conformation, binding affinity and water molecules in the binding site were analyzed. Substrate conformation and binding affinity were not correlated with the experimental results of the substrate selectivity. On the contrary, better enzyme preference towards a substrate was correlated with two stronger hydrogen bonds (His-NH-O_a and His-NH-Ser-O_γ) and less water molecules between the substrate the binding pocket. Possible explanation of these was discussed.     

A simple PCR/RFLP analysis can differentiate between Candida albicans, Aspergillus niger, and Aspergillus fumigatus

The clinical management of immunocompromised patients depends on the rapid identification of infectious agents such as fungal pathogens. The procedure described here for accomplishing this uses a sensitive polymerase chain reaction method, previously reported, combined with restriction-enzyme digestion to distinguish between Candida and Aspergillus species and to classify Aspergillus strains.