Lipase-catalyzed synthesis of chlorogenate fatty esters in solvent-free medium

Chlorogenic acid (5-caffeoylquinic acid or 5-CQA) is an hydrophilic phenolic compound with antioxidant properties. Because of its high polarity, its antioxidant properties may be altered when formulated in oil based food or cosmetic preparations. Therefore, there is an interest in trying to enhance its hydrophobicity by grafting of an aliphatic chain. Such lipophilization reactions can be generally achieved through enzymatic catalysis. Our study consisted in synthesizing fatty cholorogenate esters in a two steps reaction. Firstly, 5-CQA was chemically esterified by methanol using an Amberlite IR120 H resin to obtain methyl chlorogenate that is more soluble in the fatty alcohols than 5-CQA. Secondly, this chlorogenate intermediate was transesterified with fatty alcohols of various chain lengths (C₄, C₈, C₁₂, or C₁₆) in the presence of Candida antarctica B lipase. Under optimal reaction conditions (a_w = 0.05; 5% (w/w) of biocatalyst), the transesterification rates were until two-fold higher than in the direct lipase-catalyzed esterification of chlorogenic acid by the same alcohols. The two-step reaction overall yield was between 61 and 93% depending on the alcohol chain length, whereas it was 40–60% for the direct esterification with the same alcohols.     

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.     

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.     

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.     

Lipase-catalyzed synthesis of glycerol carbonate from renewable glycerol and dimethyl carbonate through transesterification

Glycerol carbonate is a key multifunctional compound employed as solvent, additive, monomer, and chemical intermediate. Enzymatic synthesis of glycerol carbonate from renewable starting materials (glycerol and dimethyl carbonate) was successfully achieved by immobilized lipase from Candida antarctica (CALB, Novozym 435). Addition of molecular sieves as scavenger for the removal of methanol, which was generated from dimethyl carbonate during the reaction, accelerated a reaction rate. After the optimization, the equimolar use of glycerol and dimethyl carbonate in the Novozym 435-catalyzed reaction yielded a glycerol carbonate with almost quantitative yield. The resulting glycerol carbonate from 60 °C reaction has shown the low enantiomeric excess (13% ee) as configuration of (R)-enantiomer.     

Enzymatic synthesis of the acrylic esters: a comparative study

Various acrylic esters were synthesized by Candida cylindracea lipase (CCL) catalysed transesterification with different alcohols. A comparative study was carried out using 2,3-butanedione mono-oxime acrylate and vinyl acrylate as acylating agents. The rate of conversion was faster when oxime acrylate was used as acylating agent as compared to vinyl acrylate. Effect of solvents on the rate of conversion was studied and diisopropyl ether (DIPE) was proved to be a better solvent as compared to CHCl₃ and THF. The effect of various structural aspects of the substrates on the rate of conversion was studied. Among the linear alcohols studied, ease of conversion was found to be in the order of n-octanol>n-hexanol>n-butanol. Up to 80% conversion was achieved in the case of cyclohexyl methanol.     

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.     

The effect of substrate polarity on the lipase-catalyzed synthesis of aroma esters in solvent-free systems

The aim of this study was to compare activities of commercial lipases in synthesis of various esters in solvent-free system and in isooctane. Moreover, the effect of substrate polarity (expressed as log P) on solvent-free synthesis was investigated. The decrease of yields of esters of butanoic acid in absence of organic solvent was observed, while similarly high yields were noticed in synthesis of esters of octanoic acid in both systems (solvent-free and organic solvent). The kinetic analysis has shown that ester synthesis can be described with Ping-pong bi-bi kinetics. In a case of esterification of butanoic acid in solvent-free system additional term, which represents enzyme inactivation by acid substrate, must be included. It was found out that log P of initial substrate mixture was in linear correlation with kcat of ester synthesis, while final yields depend only on type of acid substrate. Each of the examined lipases showed similar properties, although immobilized lipase from Rhizomucor miehei was slightly more resistant to harmful influence of butanoic acid. Finally, it was also shown that detrimental influence of butanoic acid could be circumvented by two-step addition of acid substrate in reaction catalyzed with immobilized lipase from R. miehei.     

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.     

Enzymatic synthesis of ethyl glucoside lactate in non-aqueous system

Ethyl glucoside lactate, a novel α-hydroxy acid derivative, was synthesized by transesterification in non-aqueous phase using immobilized lipase as biocatalyst. Parameters such as solvent type, substrate concentration, reaction temperature, and enzyme concentration were investigated to optimize the lipase-catalyzed transesterification. In solvent-free system with butyl lactate as both acyl donor and solvent, a 71% conversion was achieved. In order to investigate the effect of initial water content, the reactions were carried out in the mediums treated with molecular sieves. The results showed that conversion and initial rate decreased with the increase of water content. The conversion and initial rate reached to 95% and 67.4 mM/h, respectively, by carrying out the reaction under reduced pressure, which was employed to eliminate butanol and the initial water.     

Comparison between two processes for the enzymatic synthesis of tri-docosahexaenoylglycerol in a solvent-free medium

The enzymatic synthesis of homogeneous tri-docosahexaenoylglycerol from glycerol and ethyl docosahexaenoate in a solvent-free medium was achieved using Novozym SP 435 (immobilized lipase from Candida antarctica). Two processes were tested: a constant stirred tank reactor with N₂ bubbling through and a constant stirred tank reactor under vacuum. The first experimental apparatus was clearly found to be better than the other, giving 100% (w/w) conversion after 10 h.     

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.     

Fatty Acid Specificity in Lipase-Catalyzed Synthesis of Glucoside Esters

The fatty acid specificity of the B-lipase derived from Candida antarctica was investigated in the synthesis of esters of ethyl D-glucopyranoside. The specificity was almost identical with respect to straight-chain fatty acids with 10 to 18 carbon atoms. However, lower fatty acids such as hexanoic and octanoic acid and the unsaturated 9-cis-octadecenoic acid were found to be poor substrates of the enzyme. As a consequence of this selectivity, these fatty acids were accumulated in the unconverted fraction when ethyl D-glucopyranoside was esterified with an excess of a mixture of fatty acids. This accumulation can reduce the overall effectiveness of the process as the activity of the lipase was found to be reduced when exposed to high concentrations of short-chain fatty acids. Finally, using a simplified experimental set-up, the specificity of the C. antarctica B-lipase was compared to the specificity of lipases derived from C. rugosa, Mucor miehei, Humicola, and Pseudomonas. Apart from the C. rugosa lipase, which exhibited a very poor performance, all the enzymes showed a very similar specificity with respect to fatty acids longer than octanoic acid while only the C. antarctica B-lipase showed activity towards sort-chain fatty acids.     

Fatty Acid Specificity in Lipase-Catalyzed Synthesis of Glucoside Esters

The fatty acid specificity of the B-lipase derived from Candida antarctica was investigated in the synthesis of esters of ethyl D-glucopyranoside. The specificity was almost identical with respect to straight-chain fatty acids with 10 to 18 carbon atoms. However, lower fatty acids such as hexanoic and octanoic acid and the unsaturated 9-cis-octadecenoic acid were found to be poor substrates of the enzyme. As a consequence of this selectivity, these fatty acids were accumulated in the unconverted fraction when ethyl D-glucopyranoside was esterified with an excess of a mixture of fatty acids. This accumulation can reduce the overall effectiveness of the process as the activity of the lipase was found to be reduced when exposed to high concentrations of short-chain fatty acids. Finally, using a simplified experimental set-up, the specificity of the C. antarctica B-lipase was compared to the specificity of lipases derived from C. rugosa, Mucor miehei, Humicola, and Pseudomonas. Apart from the C. rugosa lipase, which exhibited a very poor performance, all the enzymes showed a very similar specificity with respect to fatty acids longer than octanoic acid while only the C. antarctica B-lipase showed activity towards sort-chain fatty acids.     

Enzymatic synthesis of cetyl oleate in a solvent-free medium using microwave irradiation and physicochemical evaluation

Abstract

A cosmetic ester, cetyl oleate was synthesized using microwave irradiated system. The esterification reaction was carried using Candida antarctica lipase B in a solvent-free media. The influence of various reaction parameters was studied, and the efficiency of Fermase CALB^TM10000 was compared with other enzymes. Equilibrium conversion of 97.5% was obtained within 20?min at 60?°C temperature, 1:2 oleic acid to cetyl alcohol molar ratio and 4% w/w dose of lipase. A comparative study showed that microwave irradiation is a much more efficient method than ultrasound irradiation and conventional heating. Fermase CALB^TM10000 was reusable over 6 enzymatic cycles as its stability improved under microwave system. Physicochemical parameters of cetyl oleate were tested in order to analyze its suitability for further cosmetic use.     

A novel,two consecutive enzyme synthesis of feruloylated monoacyl- and diacyl-glycerols in a solvent-free system

Feruloylated mono- and di-acylglycerols were synthesized in a two step reaction: ethyl ferulate was first transesterified with glycerol and then this was esterified with oleic acid. The yield of the combined feruloylated mono- and di-acylglycerols in the second reaction reached 96% when esterification of 0.3 g transesterification products with 2.22 g oleic acid was catalyzed with 0.25 g Candida antarctica lipase at 60°C under a vaccum of 10 mmHg for 1.33 h.     

Enzymatic synthesis of alkyl-α-glucoside catalysed by a thermostable α-transglucosidase in solvent-free organic medium

α-Transglucosidase from Talaromycesduponti was used to synthesize different alkyl-α-d-glucosides from α(1-4) linked carbohydrate donors. The enzymatic preparation, purified by a single step, consisting of hydrophobic interaction chromatography, was sufficiently pure for very stereospecific synthesis to be achieved. Biphasic and homogeneous organic media could be compared for such purposes. Yields appeared to be two- to threefold higher in low-water biphasic media. High concentrations of the glucosyl donor were present in the aqueous phase, while water-immiscible alcohols were used as glucosyl acceptors. The high efficiency of the method was attributed to the shift of the thermodynamic equilibrium thanks to the extraction of the product from the aqueous phase, where the reaction occurs, into the organic phase. Operated in a continuous biphasic reactor, T. dupontiα-transglucosidase showed a good thermostability with a half-life of 23 days at 30 °C. Received: 26 January 1998 / Received revision: 15 April 1998 / Accepted: 19 April 1998     

Parameters affecting incorporation and by-product formation during the production of structured phospholipids by lipase-catalyzed acidolysis in solvent-free system

By-product formation is a serious problem in the lipase-catalyzed acyl exchange of phospholipids (PL). By-products are formed due to parallel hydrolysis reactions and acyl migration in the reaction system. A clear elucidation of these side reactions is important for practical operation in order to minimize by-products during reaction. In the present study we examined the lipozyme RM IM-catalyzed acidolysis for the production of structured phospholipids between phosphatidylcholine (PC) and caprylic acid in the solvent-free system. A five-factor response surface design was used to evaluate the influence of major factors and their relationships on a number of responses reflecting the turnover of main reactions as well as side reactions. The five factors, including enzyme dosage, reaction time, reaction temperature, substrate ratio (mol/mol caprylic acid/PC) and water addition, were varied at three levels with two star points. All parameters besides water addition had an effect on the incorporation of caprylic acid into PC and lysophosphatidylcholine (LPC). Reaction time and enzyme dosage showed increased effect on incorporation into PC, while substrate ratio and reaction temperature showed opposite effect. The PC content decreased with increase of all parameters except for substrate ratio. Optimal conditions are recommended as enzyme dosage 40%, reaction temperature 55 °C, water addition 1%, reaction time 70 h, and substrate ratio 6 mol/mol caprylic acid/PC. Under these conditions an incorporation of 46% with PC accounting for 53% of the PL fraction can be obtained. Regiospecific analysis of the product revealed that the caprylic acid was mainly incorporated into the sn-1 position accounting for 80% of the fatty acids incorporated.     

Lipase-catalyzed synthesis of geranyl acetate in n-hexane with membrane-mediated water removal.

The esterification of geraniol with acetic acid in n-hexane was investigated. A commercial lipase preparation from Candida antarctica was used as catalyst. The equilibrium conversion (no water removal) was found to be 94% for the reaction of 0.1 M alcohol and 0.1 M acid in n-hexane at 30 degrees C. This was shown by both hydrolysis and esterification reactions. The activation energy of reaction over the temperature range 10 degrees to 50 degrees C was found to be 16 kJ/mol. The standard heat of reaction was -28 kJ/mol. Membrane pervaporation using a cellulose acetate/ceramic composite membrane was then employed for selective removal of water from the reaction mixture. The membrane was highly effective at removing water while retaining all reaction components. Negligible transport of the solvent n-hexane was observed. Water removal by pervaporation increased the reaction rate by approximately 150% and increased steady-state conversion to 100%.     

Enzymatic synthesis of new aromatic and aliphatic esters of flavonoids using Candida antarctica lipase as biocatalyst

Enzymatic acylation of rutin and esculin with aromatic, aliphatic and aryl-aliphatic acids using Candida antarctica lipase in tert amyl alcohol as solvent was investigated under low water content. Whatever the acyl donor used, the conversion yields and initial rates for esculin were higher than for rutin. For a given flavonoid, the performance of these reactions depended on the acyl donor structures. For aliphatic acids, conversion yields and initial rates of both flavonoids were respectively in the ranges of 68-90% and of 9.5×10^-2-72×10^-2 mmol l^-1 h^-1. For aromatic acids, the reaction occurred only with the aryl subgroup (cinnamic, hydrocinnamic, 3,4-dihydroxyhydrocinnamic and 4-hydroxyphenyl acetic acids) and was drastically influenced by the presence of side chain and substitution patterns of the aromatic ring. Except for hydrocinnamic acid (75%, 23.4×10^-2 mmol l^-1 h^-1), with these acids the conversion yields and initial rates were lower and in the range of 10-45% and of 0.7×10^-2 to 12.1×10^-2 mmol l^-1 h^-1. Unsaturation of the side chain of the hydrocinnamic acid decreased the esculin conversion rate from 75 to 13% and initial rate from 23.4 to 1.76×10^-2 mmol l^-1 h^-1. The presence of hydroxyl or nitro-groups on the aromatic ring of the aryl aliphatic acid also reduced conversion yields and initial rates. Even without a spacer, the non-phenolic ring acid (quinic acid) was reactive and lead to conversion yields of about 20 and 23% respectively for rutin and esculin.