Lipase-catalyzed esterification of glycerol and polyunsaturated fatty acids from fish and microalgae oils

This paper reports on the synthesis of triglycerides by enzymatic esterification of polyunsaturated fatty acids (PUFA) with glycerol. The lipase Novozym 435 (Novo Nordisk, A/S) from Candida antarctica was used to catalyze this reaction. The main factors influencing the degree of esterification and triglyceride yield were the amount of enzyme, water content, temperature and glycerol/fatty acid ratio. The optimum reaction conditions were established as: 100 mg of lipase; 9 ml hexane; 50°C; glycerol/PUFA concentrate molar ratio 1.2:3; 0% initial water; 1 g molecular sieves added at the start of reaction; and an agitation rate of 200 rpm. Under these conditions, a triglyceride yield of 93.5% was obtained from cod liver oil PUFA concentrate; the product contained 25.7% eicosapentaenoic acid and 44.7% docosahexaenoic acid. These optimized conditions were used to study esterification from a PUFA concentrate of the microalgae Phaeodactylum tricornutum and Porphyridium cruentum. With the first, a triglyceride yield of 96.5%, without monoglycerides and very few diglycerides, was obtained after 72 h of reaction; the resulting triglycerides had 42.5% eicosapentaenoic acid. A triglyceride yield of 89.3% was obtained from a P. cruentum PUFA concentrate at 96 h of reaction, which contained 43.4% arachidonic acid and 45.6% EPA. These high triglyceride yields were also achieved when the esterification reaction was scaled up 5-fold.     

硬脂酸和月桂酸在Novozym 435催化下对芦丁酯化及分子筛对酯化率的影响

为了增加芦丁的脂溶性从而使其具有更优秀的抗氧化活性,以硬脂酸和月桂酸为酰基供体,在脂肪酶Novozym 435催化下对芦丁选择性酯化.经色谱柱提纯,得到两种带不同长度烃基的芦丁脂肪酸酯.用红外光谱和核磁共振波谱对芦丁硬脂酸进行了结构鉴定,表明该类酯化物的酯化反应位为鼠李糖的C4′″位羟基.以高效液相色谱监测酯化反应进程,分子筛添加时间对酯化率的研究结果显示,分子筛对酯化率和反应速率有提高的作用.分子筛添加时间对酯化率有影响.对于硬脂酸为酰基供体的情况,反应24h后添加分子筛的酯化反应可以得到最大的酯化转化率46%.以月桂酸为酰基供体的酯化反应,反应11 h后添加分子筛可以得到最大的酯化转化率64.5%.     

Lipase mediated simultaneous esterification and epoxidation of oleic acid for the production of alkylepoxystearates

Epoxy alkylstearates were synthesized by lipase catalysed esterification and perhydrolysis followed by epoxidation of oleic acid in a one-pot process. Immobilized Candida antarctica lipase (Novozym^®435) was used as the catalyst. The esterification reaction occurred relatively quickly and was followed by epoxidation of the alkyl ester and the remaining fatty acid. Higher degree of esterification was achieved with n-octanol, n-hexanol and n-butanol as compared to that with ethanol and iso-propanol. The rate and yield of epoxidation was enhanced with iso-propanol but was lowered with the other alcohols. The lipase suffered significant loss in activity during the reaction primarily due to hydrogen peroxide. The presence of alcohols, in particular ethanol, further contributed to the enzyme inactivation. The epoxidation reaction could be improved by step-wise addition of the lipase.     

Wax ester synthesis by lipase-catalyzed esterification with fungal cells immobilized on cellulose biomass support particles

Esterification reactions between long-chain alcohol and oleic acid were performed for producing wax esters. The reaction can be catalyzed efficiently by cell-bound lipase of Rhizopus niveous fungal cells immobilized within cellulose biomass support particles. Carrying out the reaction in a solvent-free system is feasible by adding a molecular sieve for dehydration purposes. To optimize the yield, addition of a molecular sieve should be performed gradually during the whole course starting from the beginning of the reaction. The influence of reaction conditions such as temperature and substrate concentrations on reaction rates and yields were investigated; however, this reaction system is under the influence of both internal and external mass transfer resistance. Conducting the reaction in an organic solvent system with hexane or heptane as the solvent can eliminate diffusional effects. Reaction kinetics were subjected to detailed study in this system. The kinetics of the reaction can be represented satisfactorily by a Ping-Pong Bi Bi mechanism with deadend inhibition by alcohol.     

非水相酶促合成癸酸偏甘油酯的研究

对无溶剂非水相中癸酸与甘油的酶促酯化反应进行了研究,发现Pseudomonas fluoresces脂肪酶（PFL）、Mucor miehei脂肪酶（MML）和Candida antarictica脂肪酶（CAL）均有较好的催化活性。CAL酶促转化癸酸的最适反应条件为：60℃,加酶量为20～100u/g,初始加水量为甘油质量的12%。CAL的1,3位置专一性在最终产物中未表达。CAL酶催化剂的失活主要与机械磨损有关,反应5批次后酶活残留量为96.4%。敞开物系、真空脱水或分子筛脱水均为有效脱水方式。敞开物系中反应物量比不影响平衡转化率而会影响单甘酯平衡产率。用碳酸氢钠水溶液萃取可有效脱除产品中的残余癸酸,终产品酸价为0.68mg KOH/g。提高甘油比例并使用非脱水原料,无外加水结合部分流加癸酸的工艺,可以减少减压脱水或敞开反应的时间,5h后癸酸最高转化率可达96.9%。      

Production of glycerides from glycerol and fatty acid by immobilized lipases in non-aqueous media

Immobilized Mucor miehei lipase catalyzes synthesis reactions between glycerol and oleic acid. No organic solvent is necessary to solubilize the substrates, which allows for the use of a reaction medium solely composed of the necessary substrates. Water produced in the reaction evaporates due to the high temperature used for the process. A conversion of 86% of oleic acid into triolein is obtained when using the substrates in stoichiometric amounts. Varying the ratio of glycerol over oleic acid allows for the preferential synthesis of one of the glycerides. Some batch reactors have been set up using different means of removing the water: spontaneous evaporation, molecular sieves, vacuum, and dry air bubbling.     

Prediction of the equilibrium conversion for the synthesis of acyl hexose through lipase-catalyzed condensation in water-miscible solvent in the presence of molecular sieve

A method is proposed for predicting the equilibrium conversion for the synthesis of monoacyl hexose through the lipase-catalyzed condensation of a fatty acid and a hexose in a water-miscible solvent in the presence of a molecular sieve, based on the apparent reaction equilibrium constant, the adsorption isotherm of water on the molecular sieve, the solubility of hexose in the solvent, and the mass balance with respect of water. Validity of the model was examined for the syntheses of lauroyl mannose, lauroyl glucose, and myristoyl mannose in acetonitrile, 2-methyl-2-propanol, or 2-methyl-2-butanol with molecular sieves 3A 1/16 and 4A 1/16. The predicted conversions agreed well with the experimental values except for the case where a significant amount of diester was formed as the result of the addition of an excess amount of the molecular sieve to the solvent or the high molar ratio of the fatty acid to the hexose.     

Green enzymatic production of glyceryl monoundecylenate using immobilized Candida antarctica lipase B

Enzymatic synthesis of glyceryl monoundecylenate (GMU) was performed using indigenously immobilized Candida anatarctica lipase B preparation (named as PyCal) using glycerol and undecylenic acid as substrates. The effect of molar ratio, enzyme load, reaction time, and organic solvent on the reaction conversion was determined. Both batch and continuous processes for GMU synthesis with shortened reaction time were developed. Under optimized batch reaction conditions such as 1:5 molar ratio of undecylenic acid and glycerol, 2?h of reaction time at 30% substrate concentration in tert-butyl alcohol, conversion of 82% in the absence of molecular sieve, and conversion of 93% in the presence of molecular sieve were achieved. Packed bed reactor studies resulted in high conversion of 86% in 10-min residence time. Characterization of formed GMU was performed by FTIR, MS/MS. Enzymatic process resulted in GMU as a predominant product in high yield and shorter reaction time periods with GMU content of 92% and DAG content of 8%. Optimized GMU synthesis in the present study can be used as a useful reference for industrial synthesis of fatty acid esters of glycerol by the enzymatic route.     

Enzymatic Synthesis of Ethyl-glucoside Monooleate with Lipase in Solvent-free Medium

Ethylglucoside monooleate was synthesized by esterification between ethylglucoside and oleic acid with immobilized lipase from Candida antarctica in a solvent-free system. It was shown that a stirred tank reactor was suitable for the enzymatic reaction process involving substrates with low miscibility, in which the biocatalyst was recycled five times without significant activity loss. Removal of the co-product, water, from the reaction medium by carrying out the reaction under reduced pressure benefited the esterification reaction and increased the monooleate yield up to 97% within 8 hours.     

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.     

Production of monoacylglycerol of conjugated linoleic acid by esterification followed by dehydration at low temperature using Penicillium camembertii lipase

Conjugated linoleic acid (CLA) has various physiological activities, and a commercial product is a mixture of free fatty acids (named FFA-CLA) which contains almost equal amounts of 9-cis, 11-trans (9c,11t) and 10t,12c isomers. We attempted to efficiently produce monoacylglycerol (MAG) of CLA by lipase-catalyzed esterification. Study on effect of reaction temperature clarified that synthesis of diacylglycerols (DAGs) from MAGs was repressed at low temperature. When FFA-CLA was esterified at 5 °C with 5 molar equivalents of glycerol using 200 U/g mixture of Penicillium camembertii lipase in the presence of 2% water, the degree of esterification reached 89.6% after 45 h and the contents of MAGs and DAGs were 87.0 and 4.5 wt.%, respectively. Triacylglycerols were not synthesized in this Penicillium lipase-catalyzed esterification. After the esterification was conducted for 20 h (the degree of esterification, 80.8%), dehydration was started by evaporation at 5 mmHg using a vacuum pump. The degree of esterification increased concomitantly with dehydration and reached 94.5% after 16 h (36 h in total). The contents of MAGs (main components, 1(3)-isomers) and DAGs were 92.7 and 2.9 wt.%, respectively. Fatty acid compositions in MAGs synthesized with and without dehydration were the same as that in FFA-CLA. These results showed that the esterification system with dehydration is effective for producing MAGs in a high yield.     

pH-optima in lipase-catalysed esterification

Though lipases are frequently applied in ester synthesis, fundamental information on optimal pH or substrate concentration, can almost only be found for the reverse reaction - hydrolysis. This study demonstrates that the pH-optima of lipase-catalysed esterifications differ significantly from the optima of the hydrolysis reaction. In the esterification of n-butanol and propionic acid with lipases of Candida rugosa (CRL) and Thermomyces lanuginosa (TLL) pH-optima of 3.5 and 4.25, respectively, were found. This is about 3-4 units (CRL) and 7 units (TLL) in pH lower than optimum for hydrolysis. Enzyme activity increased with increasing concentrations of protonated acid indicating that the protonated acid rather than the deprotonated form is substrate for esterification. The rate of esterification can be drastically increased by ensuring acid concentrations up to 1000 mmol L^-1 for CRL and 600 mmol L^-1 for TLL in the reaction system.     

Synthesis of triglycerides of phenylalkanoic acids by lipase-catalyzed esterification in a solvent-free system

Immobilized Candida antarctica lipase B catalyzed the synthesis of triglycerides from glycerol and phenylalkanoic acids in a solvent-free system. 4-Phenylbutyric acid was the best acyl donor and displayed the highest synthetic rate of triphenylbutyrin (glyceryl triphenylbutyrate) at 65 degrees C among various phenylalkanoic acids with straight alkyl chains. The external mass transfer between the immobilized lipase and the bulk reaction mixture was limited. Different methods of removing water during the lipase-catalyzed esterification including spontaneous evaporation, the use of saturated salts solutions, and the use of molecular sieves were studied. The highest yield of triphenylbutyrin at 65 degrees C was 98%, by the elimination of water using molecular sieves in a solvent-free system. The glycerol was almost completely esterified to triphenylbutyrin in excess phenylbutyric acid with various substrate molar ratios.     

Evaluation of regioselectivity of lipases based on synthesis reaction conducted with propyl alcohol, isopropyl alcohol and propylene glycol

Preliminary investigations on the regioselectiviy of various lipases were performed. Ten commercial lipases from different origins, including three immobilized lipases, were tested by esterification reaction between caprylic acid and propyl or isopropyl alcohol in n-hexane. Reaction products were analyzed with a gas chromatograph. Best yields were obtained with immobilized lipase IM60 from Rhizomucor miehei. Therefore, this enzyme was chosen as biocatalyst for a second step of regioselectiviy study with propylene glycol which bears primary and secondary alcohol groups. It was shown, by using several solvents, that polarity could influence the product profile in situations in which multiple products of various polarities can be formed. Furthermore, the major role of silica gel in reaction mixture was established.     

Production of Ethyl Butyrate by Candida rugosa Lipase Immobilized in Polyurethane

The enzymatic production of ethyl butyrate was studied: the lipase of Candida rugosa (E.C. 3.1.1.3.) was immobilized in a polyurethane matrix and subsequently introduced in an organic medium containing the substrates in appropriate concentrations. The large majority of experiments was carried out in n-hexane. Two further solvents were tested, namely n-heptane and n-dodecane. The partition coefficients matrix/solvent were estimated for the various solvent systems. The initial esterification rate, the molar yield ester/acid and the degree of conversion were found to be solvent independent when the reaction media were designed so that similar concentrations were created in the microenvironment. Initial rate experiments indicated that in n-hexane the threshold of inhibitory substrate concentrations lies (i) between 0.40 M and 0.50 M for butyric acid, according to the purity of the enzyme preparation and (ii) at 0.30 M for ethanol. Batch operational stability tests indicate that no enzyme deactivation occurs after 20 consecutive batches.     

Analysis of solvent-free ethyl oleate enzymatic synthesis at equilibrium conditions

This work reports experimental equilibrium data for the esterification of pure oleic acid and a fatty acid mixture with ethanol, using an immobilized Candida antarctica B lipase as catalyst. Reactions are performed in a solvent-free system, containing a mixture of substrates and different amounts of distilled water. According to the initial amount of water and the extent of the reaction, one or two liquid phases are present. Therefore, when the equilibrium is achieved, the liquid–liquid and chemical reaction equilibria have to be simultaneously satisfied.

Several reports dealing with enzymatic reactions performed in two-phase systems have found that the value of the reaction equilibrium constant calculated from overall experimental concentrations varies not only with temperature but also with substrate ratio and water content. Although this approach is a valuable way to explore equilibrium shifts in biphasic systems, it is limited to ideal systems with constant partition coefficients. The aim of this work is to consider the biphasic nature of the reactive mixture through a computational procedure that simultaneously takes into account liquid–liquid and reaction equilibria. This approach enables the determination of a classical temperature-dependent thermodynamic equilibrium constant, which accurately fits experimental equilibrium conversions over a wide range of operating conditions.     

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.     

Thermodynamics of the lipase-catalyzed esterification of glycerol and n-octanoic acid in organic solvents and in the neat reaction mixture

The thermodynamics of the lipase-catalyzed esterification of glycerol with n-octanoic acid have been investigated with acetonitrile, benzene, and toluene as solvents and in the neat reaction mixture (no organic solvent added). This esterification reaction leads to five products: 1-monooctanoyl glycerol, 2-monooctanoyl glycerol, 1,2-dioctanoyl glycerol, 1,3-dioctanoyl glycerol and 1,2,3-trioctanoyl glycerol. This, in turn leads to a total of 12 reactions. Values of the equilibrium constants for these reactions have been measured (HPLC, GC, and LC/MS) at 37°C in the above mentioned media. The equilibrium constants range from 0.9 to 20.7, 0.20 to 8.0, 0.23 to 10.0, and 0.57 to 2.2 in acetonitrile, benzene, toluene, and neat media, respectively. Relative standard molar Gibbs free energies of formation Δ_fG_m⁰ of 1-monooctanoyl glycerol, 2-monooctanoyl glycerol, 1,2-dioctanoyl glycerol, 1,3-dioctanoyl glycerol and 1,2,3-trioctanoyl glycerol in the organic solvents and in the neat reaction mixture have been calculated and used to compactly summarize the thermodynamics of these reactions. The results show an approximate correlation with the permittivities of the solvents.     

Enzymatic esterification between n-alcohol homologs and n-caprylic acid in non-aqueous medium under microwave irradiation

The enzymatic esterification between n-alcohol homologs and n-caprylic acid catalyzed by lipozyme RM IM (LRI) in microwave field was investigated. Some interesting findings were obtained. The optimum reaction temperature slightly shifted from that in enzymatic esterification by conventional heating. n-Alcohol homologs used in this experiment showed substrate specificity in terms of the odd and even carbon numbers. THF expressed abnormal solvent effect. Whereas in the contrastive enzymatic esterification by conventional heating, the above mentioned substrate specificity and solvent effect were not observed. All the above phenomena could be explained by both thermal and non-thermal effect of microwave on enzyme and substrates. Further investigation revealed that microwave irradiation reduced the apparent activation energy of the enzymatic reaction according to Arrhenius equation, which is considered as one of the causes increasing initial reaction rate.     

Erratum to: Solvent-free geranyl oleate production by enzymatic esterification

This study reports the maximization of geranyl oleate production by esterification of geraniol and oleic acid in a solvent-free system using a commercial lipase as catalyst. The operating conditions that maximized geranyl oleate production were determined to be 40?°C, geraniol to oleic acid molar ratio of 5:1, 150?rpm and 10?wt% of enzyme, with a resulting reaction conversion of about 93%. After determining the best reaction parameters, a kinetic study was performed and the results obtained in this step allow to conclude that an excess of alcohol (alcohol to acid molar ratio of 5:1), relatively low enzyme concentration (5?wt%) and temperature of 50?°C afforded nearly complete reaction conversion after 1?h of reaction. New experimental data on enzymatic esterification of geraniol and oleic acid for geranyl oleate production are reported in this work, showing a promising perspective of the technique to overcome the inconvenience of the chemical-catalyzed route.