有机相中固定化脂肪酶促有机硅烷醇的转酯

探讨了有机相中固定化脂肪酶（Lipozyme）催化非天然的有机硅院醇与脂肪酸酯转酯反应的可能性;系统地研究了有机溶剂特性、水活度、有机硅烷醇结构、脂肪酸酯碳链长等因素对转酯反应的影响。     

有机相中酶促有机硅烷醇的转酯

在有机介质中,脂肪酶L-1754可以催化非天然有机硅烷醇与脂肪酸酯的转酯反应.反应介质、反应体系水活度和底物的结构对酶促转酯反应有显著的影响.适宜的反应介质为正辛烷,反应体系最适水活度为0.55.     

非水介质中脂肪酶催化的手性拆分研究进展

脂肪酶催化的外消旋体动力学拆分是不对称催化领域中极具吸引力且发展非常迅速的重要技术。对这一领域的最新研究进展进行了调研,并将注意力集中于脂肪酶在非水溶剂中的应用。引用最近五年中的一些文献案例,说明了脂肪酶作为立体选择性生物催化剂在外消旋体拆分中的多样化功能和应用。     

非水介质中酶催化葡甘聚糖的转酯化反应

葡甘聚糖(KGM)是一种具有优异的生物降解性、生物相容性、独特的生理和药理功能的天然聚多糖。通过环境友好的、高选择性的酶催化转酯化反应引入疏水基团可以制备葡甘聚糖的酯化衍生物,从而拓宽其应用领域。本研究探讨了在非水介质中以脂肪酶Novozym 435、Lipozym RMIM、Lipozym TLIM和Lipase TypeⅦ催化KGM和乙酸乙烯酯的转酯化反应,并且考察了相关因素对转酯化反应的影响。实验结果表明:在非水介质N,N-二甲基乙酰胺、甲苯和异辛烷中,脂肪酶Novozym 435可以较好的催化乙酸乙烯酯和KGM发生转酯化反应。以Novozym 435为催化剂、以异辛烷为反应介质,当底物浓度[S]=30(mg/mL)、酶用量[E]/[S]=0.30(wt/wt)、酰基供体乙酸乙烯酯用量[Acyl]/[OH]=3.0(mol/mol)、50℃、反应72 h的条件下,酯化KGM的取代度(DS)可达到0.49。     

非水相中脂肪酶催化甘油三酯转酯反应动力学

本文研究了脂肪酶在己烷中催化甘油三丁酸酯与硬脂酸之间的转酯反应动力学。转酯反应分为二个连续的反应步骤:由酯生成的酰基酶复合物的水解和由酸生成的酰基酶复合物的醇解,整个反应符合乒乓反应机制,动力学参数为:K_m(酯)=3.2×10~(-2)mol/L,K_m(酸)=6.9×10~(-2)mol/L,V_m=1.7×10~(-4)mol/L·min。     

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。     

有机介质中脂肪酶催化反应在有机合成中的应用

综述了近年来有机介质中脂肪酶催化反应在酯合成,酯交换,内酯合成,多肽合成,高聚物合成及立体异构体拆分等有机合成领域的应用。对脂肪酶催化不对称反应合成光学纯化合物进行了较详细的介绍。     

有机介质中脂肪酶催化外消旋苯甘氨酸甲酯的对映体选择性氨解反应

由水解酶催化的酯的对映体选择性水解和醇解反应 ,已在外消旋物质的拆分中得到广泛应用[1 ] 。近年来的一些研究表明 ,某些水解酶还可催化一些非天然酰基受体的转化 ,如过氧化氢、烷基胺、联胺和氨等。这些非天然酰基受体的转化反应在多肽的合成及手性化合物的拆分中显示出巨大的应用前景。其中 ,以氨为酰基受体的酶促氨解反应 ,是继酶促对映体选择性水解、酯化及转酯反应之后的另一制备光学纯化合物的新反应[2 ] 。目前国际上对这一新反应的研究尚属起步 ,国内未见有对该反应研究的报道。(Ｄ ,Ｌ) 苯甘氨酸是半合成 β 内酰胺类抗生素的重…     

脂肪酶催化有机硅化合物的生物转化

C.cylindracea脂肪酶可催化有机介质中有机硅醇与脂肪酸的酯化反应。微水有机介质比水-水不溶有机介质更有利于酶的反应,有机硅醇是比其碳结构类似物更好的酰基受体。对不同有机硅醇底物,当其空间障碍大时,不利于酶催化酯化反应,对不同脂肪酸底物,有机硅醇未影响该脂肪酶的脂肪酸底物特异性。     

Immobilization of lipase by salts and the transesterification activity in hexane

Lipases from six different sources were immobilized on Celite and five types of salt. The transesterification activities in hexane for lipases immobilized on EDTA-Na₂ increased by 463% for the lipase from Candida rugosa (CRL), 2700% for the lipase from Candida sp. (CSL) and 1215% for the lipase from Pseudomonas sp. (PSL), compared to the salt-free enzyme. With 0.5% sucrose for CRL or 1% sorbitol for PSL as the lyoprotectant during lyophilization process, transesterification activity increased by 100% and 13%, respectively, compared to the immobilized enzyme on EDTA-Na₂ without lyoprotectant.     

Chemical modification of alpha-chymotrypsin for obtaining high transesterification activity in low water organic media

Alpha-chymotrypsin was made more hydrophilic by modifying 11 (out of 16) ε-amino groups with pyromellitic dianhydride. The hydrophilic preparation was precipitated with n-propanol. This preparation gave significantly higher initial rates at the optimum a_w (127.51 nmol mg^?1 min^?1 in n-octane and 21.30 nmol mg^?1 min^?1 in acetonitrile at a_w=0.33) compared with the lyophilized preparation (53.50 nmol mg^?1 min^?1 in n-octane and 0.26 nmol mg^?1 min^?1 in acetonitrile at a_w=0.97). FT-IR showed that the precipitate of modified alpha-chymotrypsin has a higher content of alpha-helices and beta-sheets compared to the lyophilized powder.     

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.     

Improved triglyceride transesterification by circular permuted Candida antarctica lipase B

Lipases represent a versatile class of biocatalysts with numerous potential applications in industry including the production of biodiesel via enzyme‐catalyzed transesterification. In this article, we have investigated the performance of cp283, a variant of Candida antarctica lipase B (CALB) engineered by circular permutation, with a series of esters, as well as pure and complex triglycerides. In comparison with wild‐type CALB, the permutated enzyme showed consistently higher catalytic activity (2.6‐ to 9‐fold) for trans and interesterification of the different substrates with 1‐butanol and ethyl acetate as acyl acceptors. Differences in the observed rates for wild‐type CALB and cp283 are believe to be related to changes in the rate‐determining step of the catalytic cycle as a result of circular permutation. Biotechnol. Bioeng. 2010;105: 44–50. © 2009 Wiley Periodicals, Inc.     

Enzymatic interesterification of triglyceride with surfactant-coated lipase in organic media

Several surfactant-coated enzymes have been prepared by coating lipases of various origins with a nonionic surfactant, glutamic acid dioleylester ribitol (2C(18)Delta(9)GE). Enzymatic interesterification of tripalmitin with oleic acid using the surfactant-coated lipase was carried out in organic media. The surfactant-coated lipases could effectively catalyze the interesterification of glycerides better than did the powder lipases. A suitable organic solvent was an aliphatic hydrocarbon such as isooctane. The enzymatic activity for the interesterification strongly depended on the origin of the lipase. The surfactant-coated lipase prepared by Mucor javanicus showed the highest enzymatic activity for the interesterification of glycerides, although its powder lipase did not show enzymatic activity. Selective interesterification of glycerides could be performed by adjusting the concentration ratio of oleic acid to tripalmitin in isooctane. Di-substituted glyceride could be selectively produced when the concentration ratio of carboxylic acid to glycerides was 7. (c) 1995 John Wiley & Sons, Inc.     

Enhancing reaction rate for transesterification reaction catalyzed by Chromobacterium lipase

Precipitation of Chromobacterium viscosum lipase as an interfacial layer by addition of ammonium sulphate and t-butanol [in a process called three phase partitioning (TPP)] led to an increase in the initial rate of tranesterification in iso-octane by 4.9 times. It is shown that the TPP-treated lipase also showed salt activation and further increase in activity in the presence of sorbitol. Thus, in synergy with these strategies, the TPP treatment resulted in a more efficient design of catalytic transesterification; the overall increase in transesterification as a result of the optimization was about 15 times.     

固定化脂肪酶催化制备L-薄荷醇

用大孔树脂NKA固定高选择性的脂肪酶,催化有机相中转酯化反应,从而拆分八异构体消旋薄荷醇来制备L-薄荷醇。研究pH、载体与酶比例对固定化酶制备的影响及固定化酶的反应稳定性;考察温度、转酯化过程醇酯比例、及底物醇异构组成变化对拆分效果的影响。结果表明:固定化酶的最适pH为8,载体与酶的比例为5∶1时,所得固定化酶的反应稳定性比游离酶的反应稳定性提高了约50%;转酯化反应的最优温度为40℃,醇酯比例为1.5∶1时最佳,改进八异构体消旋薄荷醇组分比例后,非对映体选择率dep达到了95.1%。     

Biodiesel fuel production via transesterification of oils using lipase biocatalyst

Biodiesel has gained widespread importance in recent years as an alternative, renewable liquid transportation fuel. It is derived from natural triglycerides in the presence of an alcohol and an alkali catalyst via a transesterification reaction. To date, transesterification based on the use of chemical catalysts has been predominant for biodiesel production at the industrial scale due to its high conversion efficiency at reasonable cost. Recently, biocatalytic transesterification has received considerable attention due to its favorable conversion rate and relatively simple downstream processing demands for the recovery of by-products and purification of biodiesel. Biocatalysis of the transesterification reaction using commercially purified lipase represents a major cost constraint. However, more cost-effective techniques based on the immobilization of both extracellular and intracellular lipases on support materials facilitate the reusability of the catalyst. Other variables, including the presence of alcohol, glycerol and the activity of water can profoundly affect lipase activity and stability during the reaction. This review evaluates the current status for lipase biocatalyst-mediated production of biodiesel, and identifies the key parameters affecting lipase activity and stability. Pioneer studies on reactor-based lipase conversion of triglycerides are presented.