Enzymatic synthesis of sialic acid derivative by immobilized lipase from Candida antarctica

The effects of important reaction parameters on the enhancement of sialic acid derivative lipophilic properties through the lipase-catalyzed esterification of N-acetyl neuraminic acid methyl ester are investigated in this study. It is found that the lipase Novozym 435 from Candida antarctica is particularly useful in the preparation of sialic acid methyl ester monononanoate (SAMEMN). The optimum temperature for the SAMEMN synthesis reaction using Novozym 435 is 60 °C, and nonanoic anhydride is found to be the best substrate among all acyl donors. The Novozym 435-catalyzed esterification of N-acetyl neuraminic acid methyl ester gave a maximum yield of 87.7% after 6 h in acetonitrile at 60 °C. Because the novel method developed is simple, yet effective, it could potentially be used industrially for the production of sialic acid derivatives.     

Regioselective acylation of flavonoids catalyzed by immobilized Candida antarctica lipase under reduced pressure

A single-step acylation of rutin and naringin, catalyzed by immobilized Candida antarctica lipase B in 2-methyl-2-butanol, occurred preferentially on the primary hydroxyl group. Using palmitic methyl ester as acyl donor, the acylation rate of naringin was 10-fold higher than that of rutin. Under optimal conditions, i.e. a molar ratio acyl donor/naringin of 7:1 and 200 mbar, 92% naringin was acylated.     

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.     

Ester synthesis from trimethylammonium alcohols in dry organic media catalyzed by immobilized Candida antarctica lipase B

Twenty-one different organic solvents were assayed as possible reaction media for the synthesis of butyryl esters from trimethylammonium alcohols in dry conditions catalyzed by immobilized Candida antarctica lipase B. The reactions were carried out following a transesterification kinetic approach, using choline and L-carnitine as primary and secondary trimethylammonium alcohols, respectively, and vinyl butyrate as acyl donor. The synthetic activity of the enzyme was strictly dependent on the water content, the position of the hydroxyl group in the trimethylammonium molecule, and the Log P parameter of the assayed solvent. Anhydrous conditions and a high excess of vinyl butyrate over L-carnitine were necessary to synthesize butyryl-L-carnitine. The synthetic reaction rates of butyryl choline were practically 100-fold those of butyryl-L-carnitine with all the assayed solvents. In both cases, the synthetic activity of the enzyme was dependent on the hydrophobicity of the solvent, with the optimal reaction media showing a Log P parameter of between -0.5 and 0.5. In all cases, 2-methyl-2-propanol and 2-methyl-2-butanol were shown to be the best solvents for both their high synthetic activity and negligible loss of enzyme activity after 6 days.     

Optimization of carbohydrate fatty acid ester synthesis in organic media by a lipase from Candida antarctica

The effect of solvents and solvent mixtures on the synthesis of myristic acid esters of different carbohydrates with an immobilized lipase from C. antarctica was investigated. The rate of myristyl glucose synthesized by the enzyme was increased from 3.7 to 20.2 micromol min(-1) g(-1) by changing the solvent from pure tert-butanol to a mixture of tert-butanol:pyridine (55:45 v/v), by increasing the temperature from 45 degrees C to 60 degrees C, and by optimizing the relative amounts of glucose, myristic acid, and the enzyme preparation. Addition of more than 2% DMSO to the tert-butanol:pyridine system resulted in a reduction of enzyme activity. Lowering the water content of the enzyme preparation below 0.85% (w/w) resulted in significant decreases in enzyme activity, while increasing the water content up to 2.17% (w/w) did not significantly affect the enzyme activity. The highest yields of myristyl glucose were obtained when an excess of unsolubilized glucose was present in the reaction system. In this case, all of the initially solubilized and a significant amount of the initially unsolubilized glucose was converted to the ester within 24 h of incubation, resulting in a myristyl glucose concentration of 34 mg/mL(-1). Myristic acid esters of fructose (22.3 micromol min(-1) g(-1)), alpha-D-methyl-glucopyranoside (26.9 micromol min(-1) g(-1)) and maltose (1.9 micromol min(-1) g(-1)) could also be prepared using the tert-butanol:pyridine solvent system. No synthesis activity was observed with maltotriose, cellobiose, sucrose, and lactose as substrate.     

Synthesis of monoacylglycerol containing pinolenic acid via stepwise esterification using a cold active lipase

High purity monoacylglycerol (MAG) containing pinolenic acid was synthesized via stepwise esterification of glycerol and fatty acids from pine nut oil using a cold active lipase from Penicillium camembertii as a biocatalyst. Effects of temperature, molar ratio, water content, enzyme loading, and vacuum on the synthesis of MAG by lipase‐catalyzed esterification of glycerol and fatty acid from pine nut oil were investigated. Diacylglycerol (DAG) as well as MAG increased significantly when temperature was increased from 20 to 40°C. At a molar ratio of 1:1, MAG content decreased because of the significant increase in DAG content. Water has a profound influence on both MAG and DAG content through the entire course of reaction. The reaction rate increased significantly as enzyme loading increased up to 600 units. Vacuum was an effective method to reduce DAG content. The optimum temperature, molar ratio, water content, enzyme loading, vacuum, and reaction time were 20°C, 1:5 (fatty acid to glycerol), 2%, 600 units, 5 torr, and 24 h, respectively. MAG content further increased via lipase‐catalyzed second step esterification at subzero temperature. P. camembertii lipase exhibited esterification activity up to ?30°C. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2012     

Effect of additives on the esterification activity of immobilized Candida antarctica lipase

In this work, the stabilizing effect of bovine serum albumin (BSA), peptone (PEP), and polyethylene glycol (PEG) during immobilization of Candida antarctica lipase on activated carbon was investigated. The influence of enzyme concentration and type of additive, added during the immobilization procedure, was studied using a 2² factorial central composite design. The goal was to maximize the synthetic activity of butyl butyrate, using butyric acid and butanol as substrate in n-heptane. An increase of 31–58% in the esterification activity was obtained when enzyme concentration on the supernatant was enhanced from 86.50 U m L⁻¹ to 226.80 U mL⁻¹. An enhancement in esterification activity of 38–68.95% was observed, depending on the initial enzyme concentration, when PEP was used instead of BSA. No significant increase in the esterification activity was observed when PEP was replaced by PEG. However, thermal stability tests at 50 °C showed that PEG had a higher stabilizing effect.     

毕赤酵母表面展示南极假丝酵母脂肪酶B全细胞催化合成葡萄糖月桂酸酯

利用表面展示南极假丝酵母脂肪酶B(Candida antarctica lipase B,CALB)的毕赤酵母细胞为全细胞催化剂,以葡萄糖为酰基受体,月桂酸为酰基供体,在非水相体系中催化合成糖酯。用硅胶柱层析对产物进行初提,再用制备液相色谱进一步分离纯化,并用高效液相色谱-质谱鉴定纯品性质。对该酶法合成糖脂反应体系进行了优化,其中考察了有机溶剂种类、复合溶剂体系中二甲基亚砜(DMSO)体积百分比、酶量、底物摩尔比、水活度和温度等几个影响酯化反应的因素。结果表明:在5mL反应体系中,以叔戊醇/二甲基亚砜(DMSO30%,V/V)为反应介质,添加初始水活度为0.11的全细胞催化剂0.5g,葡萄糖0.5mmol/L,月桂酸1.0mmol/L,60°C下反应72h后,葡萄糖月桂酸单酯的转化率达到48.7%。     

Kinetic resolution of drug intermediates catalyzed by lipase B from Candida antarctica immobilized on immobead‐350

Novozyme 435, which is a commercial immobilized lipase B from Candida antarctica (CALB), has been proven to be inadequate for the kinetic resolution of rac‐indanyl acetate. As it has been previously described that different immobilization protocols may greatly alter lipase features, in this work, CALB was covalently immobilized on epoxy Immobead‐350 (IB‐350) and on glyoxyl‐agarose to ascertain if better kinetic resolution would result. Afterwards, all CALB biocatalysts were utilized in the hydrolytic resolution of rac‐indanyl acetate and rac‐(chloromethyl)‐2‐(o‐methoxyphenoxy) ethyl acetate. After optimization of the immobilization protocol on IB‐350, its loading capacity was 150 mg protein/g dried support. Furthermore, the CALB‐IB‐350 thermal and solvent stabilities were higher than that of the soluble enzyme (e.g., by a 14‐fold factor at pH 5–70°C and by a 11‐fold factor in dioxane 30%–65°C) and that of the glyoxyl‐agarose‐CALB (e.g., by a 12‐fold factor at pH 10–50°C and by a 21‐fold factor in dioxane 30%–65°C). The CALB‐IB‐350 preparation (with 98% immobilization yield and activity versus p‐nitrophenyl butyrate of 6.26 ± 0.2 U/g) was used in the hydrolysis of rac‐indanyl acetate using a biocatalyst/substrate ratio of 2:1 and a pH value of 7.0 at 30°C for 24 h. The conversion obtained was 48% and the enantiomeric excess of the product (e.e._p) was 97%. These values were much higher than the ones obtained with Novozyme 435, 13% and 26% of conversion and e.e.p, respectively. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:878–889, 2018     

Hydrolysis of rice bran oil using an immobilized lipase from Candida rugosa in isooctane

The kinetics of enzymatic hydrolysis of rice bran oil in isooctane by immobilized Candida rugosa lipase in a batch reactor showed competitive inhibition by isooctane with a dissociation constant, K1, of 0.92 M. Continuous hydrolysis of rice bran oil was performed in recycling, packed bed reactor with 4352 U of immobilized lipase; the optimum recycle ratio was 9 and the operational half-life was 360 h without isooctane but 288 h with 25% (v/v) isooctane in rice bran oil.     

固定化脂肪酶选择性水解废弃鱼油富集DHA和EPA甘油酯

以鱼油下脚料为原料．以固定化Geotrichum sp．脂肪酶为催化剂,选择性水解粗鱼油,使目标脂肪酸EPA和DHA富集于甘油骨架上,显著提高了甘油酯中EPA和DHA的质量分数。通过单因素试验和响应面分析得出最佳水解条件：2g粗鱼油,2．5g水,221．3U脂肪酶,30℃,反应11．7h。最佳条件下的水解度为42．1％。EPA和DHA质量分数分别为7．8％和41．1％。经过二次水解后,水解度提高到45．9％,EPA和DHA质量分数分别提高到8．5％和42％。与初始鱼油相比,分别提高了2倍和2．2倍。     

Enzymatic preparation of fatty acid esters of sugar alcohols by condensation in acetone using a packed-bed reactor with immobilized Candida antarctica lipase

Mono- and dilauroyl arabitols, ribitols, xylitols and sorbitols were synthesized batchwise or continuously at 50°C or 60°C by condensation catalyzed by an immobilized Candida antarctica lipase in acetone. Continuous production was realized using a system where a column packed with sugar alcohol and a packed-bed reactor with the immobilized lipase were connected in series. The concentrations of the mono- and dilauroyl esters of each sugar alcohol became almost constant at mean residence times of 15 min or longer in the packed-bed reactor. The monolauroyl, monomyristoyl and monopalmytoyl arabitols, ribitols, xylitols and sorbitols were continuously produced using the reactor system at 60°C, and the productivity was in the range of 1.3–2.0 kg L^?1-reactor·day except for the fatty acid esters of sorbitol, the productivity of which was 0.6–0.8 kg L^?1-reactor·day.     

Enzymatic preparation of fatty acid esters of sugar alcohols by condensation in acetone using a packed-bed reactor with immobilized Candida antarctica lipase

Mono- and dilauroyl arabitols, ribitols, xylitols and sorbitols were synthesized batchwise or continuously at 50°C or 60°C by condensation catalyzed by an immobilized Candida antarctica lipase in acetone. Continuous production was realized using a system where a column packed with sugar alcohol and a packed-bed reactor with the immobilized lipase were connected in series. The concentrations of the mono- and dilauroyl esters of each sugar alcohol became almost constant at mean residence times of 15 min or longer in the packed-bed reactor. The monolauroyl, monomyristoyl and monopalmytoyl arabitols, ribitols, xylitols and sorbitols were continuously produced using the reactor system at 60°C, and the productivity was in the range of 1.3-2.0 kg L^-1-reactor·day except for the fatty acid esters of sorbitol, the productivity of which was 0.6-0.8 kg L^-1-reactor·day.     

Esterification degree of fructose laurate exerted by Candida antarctica lipase B in organic solvents

Sugar esters of fatty acids have many applications as biocompatible and biodegradable emulsifiers, which are determined by their degrees of esterification (DE). Direct esterification of fructose with lauric acid in organic media used commercial immobilized Candida antarctica lipase B (CALB) was investigated for DE. Significant difference of DE was observed between 2-methyl-2-butanol (2M2B) and methyl ethyl ketone (MEK), as di-ester/mono-ester molar ratio of 1.05:1 in 2M2B and 2.79:1 in MEK. Fourier transform infrared (FTIR) spectra showed that the secondary structure of the enzyme binding mono-ester presented distinct difference in 2M2B and MEK. Contents of β-turn and antiparallel β-sheet of CALB in 2M2B were 26.9% and 16.2%, respectively, but 19.1% and 13.2% in MEK. To understand the relationship between the conformational changes and differences of DE, mono-ester and fatty acid were directly employed for synthesis of di-ester. The maximum initial velocity of di-ester synthesis in MEK was 0.59 mmol g (enzyme)⁻¹ h⁻¹, which was 2.19-fold as greater as that in 2M2B, indicating that CALB conformation in MEK was preferred for the synthesis of di-ester. These results demonstrated that the conformation of CALB binding mono-ester affected by organic solvents essentially determined DE.     

Highly efficient production of monoglycerides by the continuous removal of fatty acids from lipase-catalyzed oil hydrolysis

Highly efficient production of monoglycerides was achieved from lipase-catalyzed oil hydrolysis by the continuous addition of CaCl₂ to remove the fatty acids produced. A fusion protein produced by connecting a cellulose-binding domain of Trichoderma hazianum cellulase to Bacillus stearothermophilus L1 lipase was used as a model 1,3-regiospecific lipase. The reaction was performed at pH 10 and 50°C, and the relationship between continuous removal of fatty acids and the production of monoglyceride was investigated by microscopic and HPLC analysis of oil emulsions and the reaction products. Without the addition of Ca^{2 +} the reaction was inhibited by fatty acids, with the decrease in reaction rate being proportional to the concentration of fatty acids. When CaCl₂ was continuously added in a 1:2 molar ratio with the released fatty acids, the reaction progressed unimpeded due to the formation of Ca-soaps. Both the yield and the fraction of monoglyceride in the reaction product increased due to the continuous removal of fatty acids.     

Rice bran lipase catalyzed esterification of palm oil fatty acid distillate and glycerol in organic solvent

Rice bran lipase (RBL) was delipidated to enhance its stability in organic solvent and its esterification activity at elevated temperature. The esterification activity of delipidated RBL increased as temperature was increased from 45 to 65°C. The esterification activity of delipidated RBL at 65°C was about 14 times greater than that of the non-delipidated RBL. As temperature was further increased to 75°C, the non-delipidated RBL lost all esterification activity, whereas the delipidated RBL retained approximately 48% of its esterilication activity. The delipidated RBL maintained a relative esterification activity greater than 80% after 16 h of incubation in hexane, whereas the non-delipidated RBL maintained a relative esterification activity of only 50%. A method for production of acylglycerol using delipidated RBL to esterify palm oil fatty acid distillate (PFAD) with glycerol in hexane was successfully developed. The effects of reaction temperatures and type of water removal agents (silica gel and molecular sieve) on the degree of esterification were also examined. A 4 h reaction at 65°C, catalyzed by delipidated RBL and using silica gel as the water removal agent resulted in 53.8% esterification. Thin layer chromatography analysis suggested that the esterified product was primarily comprised of mono-and di-acylglycerols.     

Enzymatic synthesis of terpenyl esters by transesterification with fatty acid vinyl esters as acyl donors by Trichosporon fermentans lipase

Enzymatic synthesis of terpenyl esters by esterification or transesterification with fatty acid vinyl esters as acyl donors by celite-adsorbed lipase of Trichosporon fermentans was investigated. In direct esterification of geraniol, the lipase showed high reactivity toward fatty acids with carbon chains longer than C-8, but little reactivity toward fatty acids with shorter chains. With fatty acid vinyl esters as acyl donors, the lipase catalysed the synthesis of geranyl and citronellyl esters with carbon chains shorter than C-6 in with yields of >90% molar conversion. Time course, effects of added water, temperature and substrate concentration were studied for the synthesis of geranyl acetate. Molar conversion yield reached 97.5% after 5 h incubation at 30–40°C with the addition of 3% water. In this reaction, no inhibition by substrates such as geraniol and vinyl acetate was observed.     

Esterification of phenolic acids from green coffee with an immobilized lipase from Candida antarctica in solvent-free medium

Phenolic acid esters were synthesized by direct esterification catalysed by an immobilized lipase obtained from Candida antarctica. Esterification yields ranged from 3 to 98%; yields seem to be linked to the electronic distribution of phenolic acids which affects the reactivity of the carboxylic function. The carbon chain length of the alcohols also plays an important role. It was observed that even for high yields, reaction times were two days or more.