固定化假丝酵母1619脂肪酶催化油酸油醇酯的合成

比较了14种不同来源的脂肪酶催化油酸油醇酯的合成。其中,假丝酵母(Candidasp．)1619脂肪酶酯化能力最强,以硅藻土为载体,分别按0．1％添加椰子油、吐温80．按l％添加MgSO43种共固定物,醇化反应初速度提高了1．5倍。此固定化酶催化油酸油醇酯合成的最适温度为30℃,0～60℃下反应24h的酯化率均在90％以上,100℃下还有10．25％的酯化率。最适酯化pH6．0。反应中去水,可使终酯化率提高到99％。在添加的23种有机溶剂中,以异辛烷促进酯化的效果最好．正壬烷和正己烷次之。此固定化酶在28℃下批式重复反应的半衰期为990h,柱式固定床反应器中28℃连续运转1000h后酯化率为78％。     

生物法合成维生素C棕榈酸酯

研究了不同的脂肪酶在有机溶剂体系中催化合成L-维生素C棕榈酸酯的反应。针对维生素C在有机溶剂中溶解度较低这一问题,对催化合成维生素C棕榈酸酯反应的脂肪酶和反应介质进行比较,同时对影响合成维生素C棕榈酸酯反应的因素（温度、底物浓度、底物摩尔比、反应时间和酶量等）进行探讨,优化了反应条件：在10mL的丙酮中,1.094g棕榈酸与0.107g维生素C在酶量为20％（W/W, 固定化酶/维生素C）的固定化脂肪酶催化下,初始含0.4nm分子筛20%,温度为60℃,转速为200r/min,反应48h转化率可以达到80%,产物维生素C棕榈酸酯的浓度可达20g/L。     

非水相脂肪酶催化合成L-抗坏血酸棕榈酸酯的研究Ⅰ

对催化合成L-抗坏血酸棕榈酸酯反应的脂肪酶(NOVO435、MML、LIPOLASE、PPL)和反应介质进行比较,得出最佳酶种为NOVO435,最佳介质为叔戊醇;同时对影响合成L抗坏血酸棕榈酸酯反应的初速度的因素(转速、温度、水分含量、酶浓度和底物浓度)进行了探讨,确定了最适反应条件：转速为200r/min,温度为55℃,水分含量为0,酶浓度为12.5%。     

固定化脂肪酶合成维生素A棕榈酸酯

研究了有机溶剂中脂肪酶催化维生素A棕榈酸酯的合成工艺。采用维生素A醋酸酯和棕榈酸乙酯作为反应底物, 对催化合成维生素A棕榈酸酯反应介质进行了比较, 同时对影响合成维生素A棕榈酸酯反应的因素(温度、初始水含量、底物摩尔比、反应时间和酶量等)进行了探讨, 优化了反应条件: 在10 mL的石油醚中, 体系初始含水量0.2%(体积比V/V), 0.100 g 维生素A醋酸酯和0.433 g 棕榈酸乙酯在酶量为1.1 g的固定化酶催化下, 在30°C、190 r/min下反应12 h, 转化率可以达到83%, 固定化酶可连续使用5次以上。     

固定化脂肪酶合成维生素A棕榈酸酯

研究了有机溶剂中脂肪酶催化维生素A棕榈酸酯的合成工艺。采用维生素A醋酸酯和棕榈酸乙酯作为反应底物, 对催化合成维生素A棕榈酸酯反应介质进行了比较, 同时对影响合成维生素A棕榈酸酯反应的因素(温度、初始水含量、底物摩尔比、反应时间和酶量等)进行了探讨, 优化了反应条件: 在10 mL的石油醚中, 体系初始含水量0.2%(体积比V/V), 0.100 g 维生素A醋酸酯和0.433 g 棕榈酸乙酯在酶量为1.1 g的固定化酶催化下, 在30°C、190 r/min下反应12 h, 转化率可以达到83%, 固定化酶可连续使用5次以上。     

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。     

响应面分析应用于抗病毒药物香菇多糖酯化工艺的优化

目的:应用响应面分析法(RSM)优化香菇多糖酯化的工艺,确定最佳酯化条件.方法:利用Design Expert软件的中心组合设计法对香菇多糖酯化条件进行了优化,并利用响应面分析法对主要影响因素进行了回归分析,主要考察脂肪酶添加量,反应时间和反应温度对酯化效果的影响.结果:得到了各因素的最佳水平值,即酶加量为0.069g,反应时间为11.92h,反应温度为40.4℃,在模拟优化的条件下,酯化后滴定所消耗NaOH量为36.60ml.结论:将在此条件下酯化的香菇多糖测定红外光谱,证实有酯键生成.     

在无溶剂系统中固定化脂肪酶合成聚乙二醇400月桂酸酯

在无溶荆反应系统中,研究了固定化假丝酵母(Candida sp)-1619脂肪酶催化合成聚乙二醇400(PEG400)月桂酸酯的酯化条件。在反应过程中不断脱水和使月桂酸的量高于化学计量值的方法,使酯化率明显提高。分批补加PEG₄₀₀使产量进一步增加。在5．0mmol月桂酸．2．5mmolPEG400,20mg同定化脂肪酶(200u),O．2ml水组成的反应体系中,40℃,锥形瓶敞口振荡反应48h。醑化率达91％;在负压条件下反应．酯化率达98．9％;反应体系中月桂酸的董增加到6．0mmol时,PEG₄₀₀完全被酯化。用己烷提取产物的收率为95％．通过薄层色谱鉴定酯化产物为双酯。     

离子液体中固定化脂肪酶催化拆分（±）-薄荷醇

以自制的平均粒径为4．5um磁性高分子微球为载体,采用离子交换法固定化Candida rugosa脂肪酶,催化（±）-薄荷醇的酯化反应,以考察反应时间、pH、反应温度、水活度等因素对酶的固定化以及酯化反应的影响。在固定化反应150min、pH5．0、酯化反应温度30℃、固定化酶的水活度为0．78的条件下,所制备的固定化脂肪酶在离子液体[bmim]PF6中催化拆分（±）-薄荷醇的效果最佳,与游离酶相比固定化脂肪酶的立体选择性有很大的提高,对映体过量率可达93％,对映体选择值为35。     

Candidasp．99-125脂肪酶催化猪油酸解合成1，3-二油酸-2-棕榈酸甘油三酯

人乳脂是一种在甘油骨架Sn-2位上富含棕榈酸（C16：0）的结构酯。经分析可知,猪油中棕榈酸主要分布在甘油酯的Sn-2位,可作为制备1,3-二油酸-2-棕榈酸甘油三酯（OPO）的原料。以Candidasp．99—125脂肪酶作催化剂,以猪油和油酸为原料,通过正交试验对无溶剂体系中酸解合成OPO的工艺条件进行研究,得到最适反应条件：猪油与油酸的质量比为1：2．0,酶用量为总底物质量的10％,反应温度40℃,反应时间4h。在该反应条件下,经酸解合成的产物三甘酯中,Sn-2C16：0的含量大于70％,占总脂肪酸中棕榈酸含量的93％以上,并合有43％以上的OPO。     

Optimisation and Characterisation of Lipase-Catalysed Synthesis of a Kojic Monooleate Ester in a Solvent-Free System by Response Surface Methodology

Kojic acid is widely used to inhibit the browning effect of tyrosinase in cosmetic and food industries. In this work, synthesis of kojic monooleate ester (KMO) was carried out using lipase-catalysed esterification of kojic acid and oleic acid in a solvent-free system. Response Surface Methodology (RSM) based on central composite rotatable design (CCRD) was used to optimise the main important reaction variables, such as enzyme amount, reaction temperature, substrate molar ratio, and reaction time along with immobilised lipase from Candida Antarctica (Novozym 435) as a biocatalyst. The RSM data indicated that the reaction temperature was less significant in comparison to other factors for the production of a KMO ester. By using this statistical analysis, a quadratic model was developed in order to correlate the preparation variable to the response (reaction yield). The optimum conditions for the enzymatic synthesis of KMO were as follows: an enzyme amount of 2.0 wt%, reaction temperature of 83.69°C, substrate molar ratio of 1:2.37 (mmole kojic acid:oleic acid) and a reaction time of 300.0 min. Under these conditions, the actual yield percentage obtained was 42.09%, which is comparably well with the maximum predicted value of 44.46%. Under the optimal conditions, Novozym 435 could be reused for 5 cycles for KMO production percentage yield of at least 40%. The results demonstrated that statistical analysis using RSM can be used efficiently to optimise the production of a KMO ester. Moreover, the optimum conditions obtained can be applied to scale-up the process and minimise the cost.     

Synthesis of N-Octyl Oleate with Lipase from Mucor miehei Immobilized onto Polyethylene Based Graft Copolymers

Lpase from Mucor miehei was immobilized onto partially hydrolyzed poly(ethylene)-g.co-hydroxyethyl methacrylate (PE/HEMA) via spacer arms of 1,6-diaminohexane and glutaraldehyde-. The PE/HEMA-lipase system was used for the enzymatic esterification of n-octanol with oleic acid in the absence of organic solvents. The influence of lipase' concentration, in the attachment solution, on the ester production profile and initial reaction rate was studied. It was found that very small amounts of lipase gave preparations which reached good degrees of conversion. The effect of the initial oleic acid concentration on that pseudo-first order reaction, as well as the presence of water in the reactional medium and the influence of temperature were evaluated. It was found that initial oleic acid concentrations lesser than 1.2 M did not inhibit the immobilized lipase activity; the presence of small amount of water (10–30μ) solubilized in the reaction mixture (6.5 cm³) increased the lipase activity and a maximum of activity of the immobilized lipase preparation was found at 55d`C. The operational stability of the preparation was determined at 37d`C in a BSTR type reactor and a half-life time of three days for the immobilized lipase was obtained.     

基于响应面设计脂肪酶Novo435催化合成甘油二酯的工艺优化

以甘油、油酸为原料,优化在无溶剂体系中以固定化脂肪酶Novo435催化合成甘油二酯（diglyceride,DAG）的工艺。系统考察底物摩尔比（油酸／甘油）、反应温度、时间和加酶量等因素对油酸转化率和甘油二酯含量影响的基础上,利用响应面试验设计优化各主效因子,并经回归分析获得最优的工艺条件。所得最优条件：油酸与甘油底物摩尔比2．27、反应温度48．14℃、反应时间6．3h、加酶量1．68％。在此条件下,实验测得油酸转化率为45．42％,甘油二酯质量分数为70．01％,与响应面模型预测值吻合。     

Synthesis of acetone glycerol acyl esters by immobilized lipase ofMucor miehei

Summary The applications of immobilized lipase ofMucor miehei for the synthesis of acetone glycerol acyl ester from acetone glycerol and fatty acid, which is the first step for monoglyceride production was investigated. With a high oleic acid to acetone glycerol ratio (O/A, mol/mol), a high catalytic activity was observed under low water content in the reaction mixture. By the combination of high O/A ratio (>3) and removal of water which was produced during the reaction, the conversion degree was increased to almost 100%. With the O/A ratio of 3, the approximate half-life of the immobilized lipase and productivity of ester was estimated to be 20 days and 869 g product/g immobilized enzyme per 2 half-lives, respectively.     

Kinetic study of the lipase-catalyzed synthesis of triolein

The kinetics of the synthesis of triolein catalyzed by immobilized Mucor miehei lipase were studied. Equilibrium constants for the synthesis of mono-, di-, and triolein were calculated from the equilibrium compositions for different initial ratios of glycerol and oleic acid by means of multiresponse regression. The 1,3-specific lipase can catalyze the synthesis of triolein because the ester enzymatically formed with the primary alcohol isomerizes, through acyl migration, to an ester on the secondary hydroxyl. The freed primary hydroxyl may then undergo further enzymatic conversion. The rates of isomerization depend on the concentration of oleic acid. (c) 1993 Wiley & Sons, Inc.     

Chemo-enzymatic epoxidation of oleic acid and methyl oleate in solvent-free medium

Chemo-enzymatic epoxidation of oleic acid (OA) and its methyl ester has been performed using hydrogen peroxide and immobilized lipase from Candida antarctica (Novozym® 435). The purpose of the study was to characterize the reaction under solvent-free conditions. The reaction temperature had a significant impact on epoxidation of OA. At lower temperatures, the substrate conversion was hindered by the formation of solid epoxystearic acid product. Nearly 90% conversion of OA to the epoxide product was obtained after 6 h at 50°C. Longer reaction times at 40°C and above resulted in by-product formation and eventually lowered the product yield. In contrast, the reaction with methyl oleate (MO) was less influenced by temperature. Almost complete epoxidation was achieved at 40-60°C; the higher the temperature the shorter was the reaction time. The main epoxidation product obtained was epoxystearic acid methyl ester (EME), and the remaining was epoxystearic acid (EA) formed by the hydrolytic action of the lipase. Recycling of the lipase for epoxidation of MO at 50°C indicated that the immobilized enzyme was prone to activity loss.     

Chemo-enzymatic epoxidation of oleic acid and methyl oleate in solvent-free medium

Chemo-enzymatic epoxidation of oleic acid (OA) and its methyl ester has been performed using hydrogen peroxide and immobilized lipase from Candida antarctica (Novozym® 435). The purpose of the study was to characterize the reaction under solvent-free conditions. The reaction temperature had a significant impact on epoxidation of OA. At lower temperatures, the substrate conversion was hindered by the formation of solid epoxystearic acid product. Nearly 90% conversion of OA to the epoxide product was obtained after 6?h at 50°C. Longer reaction times at 40°C and above resulted in by-product formation and eventually lowered the product yield. In contrast, the reaction with methyl oleate (MO) was less influenced by temperature. Almost complete epoxidation was achieved at 40–60°C; the higher the temperature the shorter was the reaction time. The main epoxidation product obtained was epoxystearic acid methyl ester (EME), and the remaining was epoxystearic acid (EA) formed by the hydrolytic action of the lipase. Recycling of the lipase for epoxidation of MO at 50°C indicated that the immobilized enzyme was prone to activity loss.     

Optimized enzymatic synthesis of ascorbyl esters from lard using Novozym 435 in co-solvent mixtures

A mild and efficient method for the conversion of fatty acid methyl esters from lard into ascorbyl esters via lipase-catalyzed transesterification in co-solvent mixture is described. A solvent engineering strategy was firstly applied to improve fatty acid ascorbyl esters production. The co-solvent mixture of 30% t-pentanol:70% isooctane (v/v) was optimal. Response surface methodology (RSM) and central composite design (CCD) were employed to estimate the effects of reaction parameters, such as reaction time (12–36 h), temperature (45–65 °C), enzyme amount (10–20%, w/w, of fat acid methyl esters), and substrate molar ratio of fatty acid methyl esters to ascorbic acid (8:1–12:1) for the synthesis of fatty acid ascorbyl esters in co-solvent mixture. Based on the RSM analysis, the optimal reaction conditions were determined as follows: reaction time 34.32 h, temperature 54.6 °C, enzyme amount 12.5%, substrate molar ratio 10.22:1 and the maximum conversion of fatty acid ascorbyl esters was 69.18%. The method proved to be applicable for the synthesis of ascorbyl esters using Novozym 435 in solvent.     

Optimization of operational conditions for adipate ester synthesis in a stirred tank reactor

Esterification of adipic acid and oleyl alcohol in a solvent-free system featuring a stirred tank reactor containing commercially immobilized Candida antarctica lipase B was performed. The process was carried out using an artificial neural network (ANN) trained by the Levenberg-Marquardt (LM) algorithm. The effects of four operative variables, temperature, time, amount of enzyme, and impeller speed, on the reaction yield were studied. By examining different ANN configurations, the best network was found to consist of seven hidden nodes using a hyperbolic tangent sigmoid transfer function. The values of the coefficient of determination (R²) and root mean squared error (RMSE) between the actual and predicted responses were determined to be 1 and 0.0058178 for training and 0.99467 and 0.622540 for the testing datasets, respectively. These results imply that the developed model was capable of predicting the esterification yield. The operative variables affected the yield, and their order of contribution was as follows: time > amount of enzyme > temperature > impeller speed. A high percentage of yield (95.7%) was obtained using a low level of enzyme (2.5% w/w), and the temperature, time, and impeller speed were 66.5°C, 354 min (about 6 h), and 500 rpm, respectively. A simple protocol for efficient substrate conversion in a solvent-free system evidenced by high enzyme stability is indicative of successful ester synthesis.     

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。