Response surface modeling of 1-stearoyl-3(2)-oleoyl glycerol production in a pilot packed-bed immobilized Rhizomucor miehei lipase reactor

A dual response approach using diacylglycerol (DAG) and triacylglycerol (TAG) as responses for optimization of 1-stearoyl-3(2)-oleoyl glycerol-enriched DAG synthesis using response surface methodology (RSM) was investigated. Four variables from a lipase-catalyzed esterification reaction were optimized using a central composite rotatable design. The following optimized conditions yielded 51 wt.% DAG and 22 wt.% TAG: reaction temperature of 55 °C, enzyme dosage of 9.5 wt.%, fatty acid/glycerol molar ratio of 2.1 and reaction time of 3 h. Results were repeatable at 10 kg production scale in a pilot packed-bed enzyme reactor. No significant losses in enzyme activity or changes in fatty acid selectivity on DAG synthesis were observed during the five pilot productions. Lipozyme RM IM showed selectivity towards the production of stearic acid enriched DAG. The purity of DAG oil after purification was 90 wt.%.     

Magnetic nanoparticles supported ionic liquids for lipase immobilization: Enzyme activity in catalyzing esterification

Candida rugosa lipase was immobilized on magnetic nanoparticles supported ionic liquids having different cation chain length (C₁, C₄ and C₈) and anions (Cl⁻, BF₄⁻ and PF₆⁻). Magnetic nanoparticles supported ionic liquids were obtained by covalent bonding of ionic liquids–silane on magnetic silica nanoparticles. The particles are superparamagnetic with diameter of about 55 nm. Large amount of lipase (63.89 mg/(100 mg carrier)) was loaded on the support through ionic adsorption. Activity of the immobilized lipase was examined by the catalysis of esterification between oleic acid and butanol. The activity of bound lipase was 118.3% compared to that of the native lipase. Immobilized lipase maintained 60% of its initial activity even when the temperature was up to 80 °C. In addition, immobilized lipase retained 60% of its initial activity after 8 repeated batches reaction, while no activity was detected after 6 cycles for the free enzyme.     

A facile enzymatic process for the preparation of ibuprofen ester prodrug in organic media

A novel glucopyranoside derivative of ibuprofen, ibuprofen methyl -d-glucopyranoside ester was synthesized via immobilized lipase-catalyzed esterification between racemic ibuprofen and methyl -d-glucopyranoside in non-aqueous medium. An appropriate product concentration (4.6 mg ml⁻¹) was achieved by optimization of reaction conditions, such as solvent type, reaction temperature, enzyme concentration and initial concentration of substrates. Comparing with the parent drug ibuprofen in physicochemical properties, the glucopyranoside derivative of ibuprofen has better hydrophilicity. The chemical structure of the ibuprofen ester was confirmed to be methyl 6-O-(2′-(4′-isobutylphenyl) propionyl) -d-glucopyranoside.     

Ultrasonic pretreatment for lipase-catalyzed synthesis of 4-methoxy cinnamoyl glycerol

4-Methoxy cinnamoyl glycerol (4MCG) is a very promising UV filters material in personal care products. In order to effectively improve the yield of 4MCG, a systematic study on ultrasonic pretreatment enzymatic esterification for 4MCG products was carried out. An ultrasonic frequency of 35 kHz, ultrasonic power of 150 W and ultrasound irradiation time of 1.5 h was determined to guarantee satisfactory degree of esterification and lipase activity. The optimum production was achieved in organic solvent system at 65 °C with 4MCA to glycerol molar ratio of 1:5, enzyme amount of 15 mg/mL, resulting in a monoester yield of above 66% and 55% after 48 h and 24 h of reaction under ultrasonic pretreatment, respectively. The experimental kinetic data were studied. The reactions were modeled by a system of sequential first-order rate expressions, kinetic parameters were estimated from experimental data fit to the model equations. Results show that the monoester yield in the ultrasonic pretreatment process (24 h) were above 1.5-fold as that in mechanical stirring process without essential damaging to lipase activity. The enzymatic method using ultrasonic pretreatment was obviously superior to the mechanical stirring for enzymatic method and chemical method in terms of conversion rate and the monoester yield. These results are of great significance for applying ultrasonic pretreatment method to prepare 4MCG.     

Esterified milk proteins inhibit DNA replication in vitro

DNA replication was studied in vitro in the presence of native and esterified milk proteins [-lactalbumin (ALA), β-lactoglobulin (BLG) and β-casein (BCN)]. Addition of unmodified proteins to the PCR medium did not change the result of the reaction seen by electrophoresis, even at excessive ratios of basic amino acids in proteins:phosphate groups in DNA as high as 100:1. Addition of esterified proteins greatly reduced the intensity of the bands corresponding to the newly synthesized DNA, at ratios as low as 1:1 and 5:1 in case of methylated-BLG and methylated-ALA, respectively. The inhibitory effect of esterified proteins was directly proportional to their extent of esterification and strongly related to their DNA-binding capacity. Generally, inhibition of PCR with esterified proteins was similar to what can be observed with histones. However, stronger inhibition was observed with highly esterified proteins when using a higher ratio of basic:acid residues (1:1) when compared with 0.5:1 ratio in case of histones. Highly esterified BCN did not exert any inhibitory effect because of its relatively lower pI when compared with that of other esterified milk proteins and due to its lower positive net charge at the pH used for PCR. During a second PCR run, only the addition of new DNA template was able to reinitiate the reaction, giving rise to new synthesized DNA. Addition of Taq DNA polymerase did not enhance DNA synthesis, showing that inhibition was performed only by binding of DNA template and not by the inhibition of the polymerase.     

高含游离脂肪酸的香果树籽油制备生物柴油的方法

目前生物柴油因其环保和可再生利用资源的特性备受关注。多数生物柴油是通过甲醇和碱催化食用油得到的,而大量非食用油也可以制备生物柴油。本文报道用高含游离酸脂肪油快速高效低成本制备成其单酯的二步法工艺。先用1% H2SO4以少于1.5%量对甲醇和云南特产香果树（Lindera communis）籽的粗原料油以10∶1摩尔比组成的混合液酸催化酯化游离脂肪酸;之后再对醇和得到的油脂产品按摩尔比15∶1的混合液碱催化转化为单甲酯和甘油。本方法是一个直接甲脂化制备生物柴油的工艺简洁、降低成本的新技术。文中还讨论了该工艺影响转化效率的主要因素,如摩尔比,催化量,温度,反应时间和酸度。香果树生物柴油不重蒸,而其生物柴油的主要特性,如粘度、热值、比重、闪点、冷滤点等与生物柴油标准的匹配度,也做了报道,研究结果将为香果树生物柴油以非重蒸油料制备生物柴油产品,作为潜在的柴油燃料替代产品提供技术支撑。     

非水介质中脂肪酶催化亚油酸油醇酯合成的研究

利用实验室自制及购买的几种脂肪酶制剂催化的酯化反应来制备亚油酸油醇酯,其中本实验室制备的丝孢酵母脂肪酸酯化效果最好,作为进一步研究的实验用酶。以正己烷为反应溶剂,在微水系统中对影响亚油酸油醉酯合成的各种因素进行了研究,确定酯化反应合成的最适温度为３５℃,０～１００℃反应１０ｈ的酯化率均可达到９０％,最适酯化ｐＨ为８．０,最适底物浓度为０．２５ｍｏｌ／Ｌ,最适水含量为０．０５％,在选用的１１种有机溶剂中,以环己烷的酯化率最高,二甲亚砜最低。     

酶法合成糖及糖醇酯

以脂肪酸为酰基供体,糖和糖醇为酰基受体,利用吸附到涤棉布上的假丝酵母脂肪酶作催化剂,在含叔丁醇的系统中,研究了酯化反应条件。酯化最适温度和pH值分别为40℃～45℃和50～75。在酰基供体中,以亚油酸和油酸最好,C8到C22的饱和脂肪酸的酯化程度相仿。在23种糖和糖醇中,果糖、木糖、海藻糖、山梨糖、木糖醇、甘露醇以及异丙基葡萄糖和甲基葡萄糖比其它酰基受体的酯化率高。糖醇的酯化程度明显高于相应的糖。此外,酰基供体与受体的摩尔比大于2∶1时,有利于酯化。在由30mmol(085g)油酸,02mmol山梨醇(0036g),3mL叔丁醇和30mg固定化酯肪酶(600u)组成的反应系统中,40℃震荡反应48h,以等摩尔的底物计算,酯化程度达到90%以上。反应产物经薄层色谱鉴定为单酯和双酯。     

非水相脂肪酶催化有机硅醇的酯化反应

非水相酶催化是酶工程研究热点之一。本文介绍了来自Ｃ．ｃｙｌｉｎｄｒａｃｅａ的脂肪酶催化有机硅醇和脂肪酸的酯化反应。该酶可催化有机硅醇与脂肪酸的酯化反应,并对不同链长的脂肪酸底物、有机溶剂极性及水含量等进行了初步研究。