Lipase-catalyzed ammonolysis of trimethylsilylmethyl acetate in organic solvent*

Lipase could catalyze the ammonolysis of trimethylsilylmethyl acetate in organic solvents and Novozym 435 was the best biocatalyst for the reaction. The influences of some factors on the reaction were investigated. Cyclohexane, n-hexane and heptane were found to be suitable reaction media and ammonium carbamate was the best ammonium source. The optimal initial water activity, temperature and pH value were 0.55–0.75, 35°C and 6.5 respectively, under which a substrate conversion of 97.6% could be achieved after reaction for 140 h.     

有机相脂肪酶催化合成乙酸肉桂酯

对有机相中酶法催化合成乙酸肉桂酯的转酯化反应进行研究。结果发现:Candida anatarctic脂肪酶(Novozyme435)、根霉脂肪酶(Rhizopus niveus lipase)和荧光假单胞菌脂肪酶(Pseudomonas fluore lipase)均有较好的催化活性。同时考察各反应参数(温度、反应溶剂、体系水活度、酰化剂类型、肉桂醇与酰化剂摩尔比、肉桂醇浓度等)对脂肪酶Novozyme435合成乙酸肉桂酯反应的影响,确定了反应体系最优工艺条件:在10 mL甲基叔丁基醚中,肉桂醇200 mmol/L,n(肉桂醇)∶n(乙酸乙烯酯)=1∶1.5,初始水活度αw=0.84,温度35℃,酶加量0.02 g,反应3 h后肉桂醇转化率可达到99%,产物经质谱(MS)鉴定。固定化酶经过10个批次反应,反应转化率都保持在90%以上。     

Lipase-catalyzed transamidation of non-activated amides in organic solvent

A novel biocatalytic reaction of transamidation of non-activated amides with amines is reported. Among 45 different lipolytic and proteolytic enzymes tested, only the lipase from Candida antarcticawas able to catalyze this reaction. The reaction proceeded with up to ca. 80% conversion in anhydrous methyl tert-butyl ether and worked with both N-substituted and unsubstituted amides. The biocatalytic transamidation is an equilibrium process and, therefore, higher conversions to the desired amide were achieved by using increased concentrations of the amine nucleophile.     

11β-Hydroxylation of norethisterone acetate by Curvularia lunata

Abstract: The biotransformation of norethisterone acetate by Curvularia lunata was studied. The 11β-hydroxy-norethisterone acetate produced was identified by mass spectrometry, and ¹H and ¹³C nuclear magnetic resonance after extractive sample preparation.     

Lipase-catalyzed biosynthesis of cinnamoylated lipids in a selected organic solvent medium

Biosynthesis of cinnamoylated lipids through the lipase-catalyzed transesterification reaction of cinnamic acid with triolein was investigated in organic solvent media. Electrospray ionization-mass spectroscopy (ESI-MS) structural analysis of the reaction mixture revealed the formation of two major end products, monoleyl-1(3)-cinnamate and dioleyl-2-cinnamate. Decreasing the molar ratio of cinnamic acid to triolein from 1:1 to 1:4.5 resulted in an increase in the maximum bioconversion yield of cinnamoylated lipids from 19 to 42%, which remained constant at a lower ratio of 1:6. However, an excess of triolein appeared to have a more beneficial effect on the formation of dioleyl-2-cinnamate than monoleyl-1(3)-cinnamate, leading to different end product compositions at ratios of substrates. With cinnamic acid to triolein ratios of 1:4.5 and 1:6.0, an increase in the bioconversion yield of cinnamoylated lipids to 55% was achieved by adding 2.2 mgmL(-1) silica gel to the reaction mixture. Radical scavenging activity of cinnamoylated lipids, with 50% of radical 2,2-diphenyl-1-picrylhydrazyl (DPPH) scavenging, was found to be higher than that of its corresponding phenolic acid.     

Improving lipase-catalyzed enantioselective ammonolysis of phenylglycine methyl ester in organic solvent by in situ racemization

Lipase-catalyzed enantioselective ammonolysis of phenylglycine methyl ester was processed by in situ racemization with ammonium carbamate as the acyl acceptor. Using 1 mM benzaldehyde or 0.6 mM chloropyridoxal as the racemizing catalyst, 80% substrate conversion with an enantiomeric excess of the product of 95% were achieved at 20 °C after 7 h reaction.     

Lipase-catalyzed acidolysis of fish liver oil with dihydroxyphenylacetic acid in organic solvent media

Lipase-catalyzed acidolysis reaction of fish liver oil with dihydroxyphenylacetic acid (DHPA) was investigated in terms of enzyme specificity as well as the effects of enzyme concentration, molar substrate ratio and organic solvent mixture on the bioconversion yield. The highest bioconversion yield of 83% was obtained when Novozym 435 was used as biocatalyst in a hexane:2-butanone mixture of 75:25 (v/v) at a fish liver oil to DHPA substrate molar ratio of 4:1; however, lower bioconversion yield (15%) was obtained when Lipozyme IM 20 was used. The bioconversion yield of phenolic monoacylglycerols (MAGs) increased from 11 to 70% when the ratio of the hexane/2-butanone reaction medium was changed from 85:15 to 75:25 (v/v), whereas that of phenolic diacylglycerols (DAGs) remained relatively unchanged (13–16%). The results also showed that the acidolysis reaction resulted in an increase of C_20:5 ω-3 and C_22:6 ω-3 proportions from 11.5 and 20.2% in the original fish liver oil to 22.6–27.1 and 22.8–23.1% in the phenolic lipids, respectively. The radical scavenging ability of phenolic lipids was determined to be about half-time lower than that of α-tocopherol.     

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.     

Simple screening method for lipase for transesterification in organic solvent

We investigated lipase-catalyzed hydrolysis in water and dioxane—water with a simple colorimetric method. We screened 24 lipases for the ability to hydrolyze p-nitrophenyl esters as chromogenic substrates. Their hydrolytic activities were varied by adding dioxane. Most of the lipases showed high activity in hydrolysis in water, but some showed activity in 50% dioxane—water several tens times higher than those in water. Moreover, several lipases with hydrolytic abilities in 50% dioxane—water also catalyzed the transesterification of p-nitrophenol using fatty acid vinyl esters. We found it possible that a useful lipase for transesterification can be selected by measuring the hydrolysis activity of p-nitrophenyl ester in 50% dioxane—water.     

Study on the kinetics of enzymatic interesterification of triglycerides for biodiesel production with methyl acetate as the acyl acceptor

A new route for biodiesel production using methyl acetate instead of methanol as the acyl acceptor was proposed in our previous research, and it has been found that this novel route could enhance the stability of the immobilized lipase greatly. In this paper, the kinetics of lipase-catalyzed interesterification of triglycerides for biodiesel production with methyl acetate as the acyl acceptor was further studied. First, a simplified model based on Ping Pong Bi Bi with substrate competitive inhibition mechanism was proposed to describe the reaction kinetics of the interesterification. During our further study, it was observed that three consecutive and reversible reactions occurred in the interesterification of triglycerides and methyl acetate. So, a kinetic model based on mass balance of three second-order reversible reactions was developed and the reaction rate constant, k, was determined by solving the differential rate equations of the reaction system. The results showed that k_DG–MG (0.1124) and k_MG–TA (0.1129) were much higher than k_TG–DG (0.0311), which indicated that the first step reaction was the limit step for the overall interesterification.     

Kinetics and optimization of lipase-catalyzed synthesis of rose fragrance 2-phenylethyl acetate through transesterification

Lipase from Candida rugosa was immobilized on a polyvinylidene fluoride membrane for synthesis of rose flavor ester, 2-phenylethyl acetate. Response surface methodology (RSM) was employed for kinetic modeling of process and prediction the yield. The RSM was used in practice for determining the kinetic models by fitting the initial rate dates based on the equations of ping-pong bi–bi and order bi–bi model. The maximum reaction rate and kinetic constants were matched with the order bi–bi model. The specificity constant of the immobilized lipase was 10-folds higher than the free form indicated the enzyme–substrate affinity, and catalytic ability was enhanced after immobilization. Moreover, the effects of reaction parameters on the yield were evaluated by RSM using a Box–Behnken experimental design. Based on a ridge max analysis, the maximum conversion was 95.33 ± 2.57% at 38.78 h, 35.85 °C, and substrate mole ratio of 3.65:1. Furthermore, the order bi–bi kinetic model was simulated successfully in a batch reaction. A good prediction existed between the RSM results and integrated equation was found.     

Lipase-catalyzed transesterification in several reaction systems: An application of room temperature lonic liquids for bi-phasic production ofn-butyl acetate

Organic solvents are widely used in biotransformation systems. There are many efforts to reduce the consumption of organic solvents because of their toxicity to the environment and human health. In recent years, several groups have started to explore novel organic solvents called room temperature ionic liquids in order to substitute conventional organic solvents. In this work, lipase-catalyzed transesterification in several uni-and bi-phasic systems was studied. Two representative hydrophobic ionic liquids based on 1-butyl-3-methylimidazolum coupled with hexafluorophosphate ([BMIM][PF₆]) and bis[(trifluoromethylsulfonyl) imide] ([BMIM] [Tf₂N]) were employed as reaction media for the transesterification ofn-butanol. The commercial lipase, Novozym 435, was used for the transesterification reaction with vinyl acetate as an acyl donor, The conversion yield was increased around 10% in a water/[BMIM][Tf₂N], bi-phasic system compared with that in a water/hexane system. A higher distribution of substrates into the water phase is believed to enhance the conversion yield in a water/[BMIM][Tf₂N] system. Partion coefficients of the substrates in the water/[BMIM][Tf₂N] bi-phasic system were higher than three times that found in the water/hexane system, while n-butyl acetate showed a similar distribution in both systems. Thus, RTILs appear to be a promising substitute of organic solvents in some biotransformation systems.     

Structure and dynamics of Candida rugosa lipase: the role of organic solvent

The effect of organic solvent on the structure and dynamics of proteins was investigated by multiple molecular dynamics simulations (1 ns each) of Candida rugosa lipase in water and in carbon tetrachloride. The choice of solvent had only a minor structural effect. For both solvents the open and the closed conformation of the lipase were near to their experimental X-ray structures (C rms deviation 1–1.3 Å). However, the solvents had a highly specific effect on the flexibility of solvent-exposed side chains: polar side chains were more flexible in water, but less flexible in organic solvent. In contrast, hydrophobic residues were more flexible in organic solvent, but less flexible in water. As a major effect solvent changed the dynamics of the lid, a mobile element involved in activation of the lipase, which fluctuated as a rigid body about its average position. While in water the deviations were about 1.6 Å, organic solvent reduced flexibility to 0.9 Å. This increase rigidity was caused by two salt bridges (Lys85–Asp284, Lys75–Asp79) and a stable hydrogen bond (Lys75–Asn 292) in organic solvent. Thus, organic solvents stabilize the lid but render the side chains in the hydrophobic substrate-binding site more mobile. Figure Superimposition of open (black, PDB entry 1CRL) and closed (gray, PDB entry 1TRH) conformers of C. rugosa lipase. The mobile lid is indicatedThis revised version was published online in October 2004 with corrections to the Graphical Abstract.     

Lipase-catalyzed methanolysis of palm oil in presence and absence of organic solvent for production of biodiesel

Enzymatic production of methyl esters (biodiesel) by methanolysis of palm oil in presence and absence of organic solvent was investigated using Candida antarctica lipase immobilized on acrylic resin as a biocatalyst. Although, at least molar equivalent of methanol (methanol-palm oil ratio 3:1) is required for the complete conversion of palm oil to methyl esters, lipase catalyzed methanolysis of palm oil in absence of organic solvent was poisoned by adding more than 1/3 molar equivalent of methanol. The use of polar organic solvents prevented the lipase to be poisoned in methanolysis with a molar equivalent of methanol, and tetrahydrofuran (THF) was found to be the most effective. The presence of water in methanolysis of palm oil both in presence and absence of THF inhibited the reaction rate but this inhibition was considerably low in THF containing system. The palm oil-lipase (w/w) ratio significantly influenced the activity of lipase and the optimal ratio in presence and absence of THF was 100 and 50, respectively.     

Synthesis of monoglyceride containing omega-3 fatty acids by microbial lipase in organic solvent

Summary An enzymatic method for synthesis of monoglyceride from 1,2-isopropylidene glycerol and n-3 polyunsaturated fatty acid concentrate was investigated in organic solvent. Optimal reaction conditions for monoglyceride synthesis by lipase were established. Lipase IM-60 fromMucor miehei produced yields of monoglyceride of up to 80% in this system. The resultant monoglyceride contained 76.2% n-3 polyunsaturated fatty acid (eicosapentaenoic acid 43.3%; docosahexaenoic acid, 32.7%). Isooctane and hexane were suitable organic solvents for monoglyceride synthesis and optimal initial water content was 2.5%. Lipase IM-60 was relatively stable in organic solvent and is easily recovered for reuse.     

Removal of water produced from lipase-catalyzed esterification in organic solvent by pervaporation

Esterification of oleic acid with n-butanol in the presence of Lipozyme(R) was carried out at 25 degrees C in isooctane with various initial water activities. Initial reaction rate as well as equilibrium conversion decreased at high initial water activity. Therefore, removal of water present in the reaction mixtures was essential. A pervaporation process was applied to the lipase-catalyzed synthesis of n-butyloleate to remove water. Pervaporation selectively separated water from the reaction mixture using a nonporous polymeric membrane, cellulose acetate. Therefore, pervaporation is potentially applicable to remove the water produced from various enzymatic processes, such as synthesis of various esters, peptides, and glycosides in a solvent system as well as in a solvent-free system. (c) 1995 John Wiley & Sons, Inc.     

Lipase-catalyzed acylation of naringin with palmitic acid in highly concentrated homogeneous solutions

Acylation reactions of naringin with palmitic acid were performed by a lipase after formation of highly concentrated homogeneous solutions. Their initial naringin concentration was 840–950 mM, which is 20–60 times greater than that in organic solvent media. The overall productivity of highly concentrated solutions was more than 15 times greater than those of organic phase media. The addition of DMSO (20–40%, w/w) to substrate mixtures lowered the melting temperature of a naringin–palmitic acid mixture (1:1 molar ratio) to about 40 °C. Reactions at 80 °C apparently followed Michaelis–Menten kinetics despite extremely high substrate concentrations. As the temperature increased from 60 °C to 80 °C, the apparent viscosity of the highly concentrated solution decreased remarkably from 4.31 Pa s to 0.063 Pa s. An activation energy of 7.65 kcal/mol obtained in a range of 60–75 °C suggests a diffusion-control. On the other hand, an activation energy of 17.09 kcal/mol in a range of 75–90 °C indicates a reaction-control. The highest product conversion yield of 33% (mol/mol) was obtained in a 10 h reaction at 80 °C. Addition of activated molecular sieves to the highly concentrated solution increased the product conversion yield by 7% (mol/mol), suggesting that the original equilibrium was disrupted by removing water and then a new equilibrium was reached.     

Lipase-catalyzed transesterification of rapeseed oils for biodiesel production with a novel organic solvent as the reaction medium

tert-Butanol, as a novel reaction medium, has been adopted for lipase-catalyzed transesterification of rapeseed oil for biodiesel production, with which both the negative effects caused by excessive methanol and by-product glycerol could be eliminated. Combined use of Lipozyme TL IM and Novozym 435 was proposed further to catalyze the methanolysis and the highest biodiesel yield of 95% could be achieved under the optimum conditions (tert-butanol/oil volume ratio 1:1; methanol/oil molar ratio 4:1; 3% Lipozyme TL IM and 1% Novozym 435 based on the oil weight; temperature 35 °C; 130 rpm, 12 h). There was no obvious loss in lipase activity even after being repeatedly used for 200 cycles with tert-butanol as the reaction medium. Furthermore, waste oil was also explored for biodiesel production and it has been found that lipase also showed good stability in this novel system.     

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.     

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%.