微波强化纳米金杂化CRL脂肪酶催化甾醇油酸酯的合成北大核心CSCD

为进一步提高植物甾醇的脂溶性、降低熔点,提出了一种在微波辐射条件下、利用纳米金杂化CRL脂肪酶为催化剂的植物甾醇油酸酯的合成方法.以植物甾醇的转化率为指标,通过响应面法确定合成植物甾醇酯的最佳工艺条件,并对最优条件进行了验证.微波强化纳米金杂化CRL脂肪酶催化植物甾醇油酸酯的最优条件为:AuNPs粒径为15 nm、AuNPs-CRL杂化酶的添加量为8%、微波功率为320 W、反应时间为64 min,在此优化条件下测得植物甾醇的转化率为91.24%±0.42%,收率为83.73%,与预测值吻合度良好.     

无溶剂体系中酶法合成2-辛基十二烷醇酯

考察了无溶剂反应体系下脂脂酶催化直接酯化合成２－辛基十二烷醇酯。在ｍｏｌ醇：ｍｏｌ酸＝１．６：１,反应温度６０℃,脂肪酶添加量４％,反应时间１０ｈ的最佳条件下,酯化率可达９４．８％。     

聚甲基丙烯酸羟乙酯载体固定化酵母脂肪酸在有机溶剂中催化酯合成反应的研究

用悬浮聚合法合成了一系列聚甲基丙烯酸羟乙酯载体，考察了它们固定化酵母脂肪酶活力与载体的交联度和致孔剂用量之间的关系。研究了这些固定化酵母脂肪酶在有机溶剂中催化酯合成反应的活性。脂肪酶的固定化使之活力表达更为充分，对亲水性较强的有机溶剂有更强的耐受性，并能为其在有机溶剂中催化酯合成反应提供必需水。考察了ｐＨ值，底物种类对固定化酵母脂肪酶催化酯合成反应的影响。     

脂肪酶催化缩聚法合成可完全降解的聚羟基丙酸酯(英文)

以3-羟基丙酸甲酯为聚合单体,建立了以固定化脂肪酶Novozym 435为催化剂的酶催化缩聚反应体系,合成可完全降解的高分子聚酯聚羟基丙酸酯,考察了反应条件和介质对反应性能的影响,结果表明,纯度大于95%的单体即可在温和条件下合成聚羟基羧酸酯;降低反应压力可有效提升产物产率和分子量.通过选择合适的有机溶剂介质和表面活性剂,可使产物分子量提升至13000(Mw)以上.脂肪酶催化剂重复利用能力优异,经6批次反应后,其相对活性保持在95%以上.     

聚甲基丙烯酸羟乙酯载体固定化酵母脂肪酶在有机溶剂中催化…

用悬浮聚合法合成了一系列聚甲基丙烯酸羟乙酯载体，考察了它们固定化酵母脂肪酶活力与载体的交联度和致孔剂用量之间的关系。研究了这些固定化酵母脂肪酶在有机溶剂中催化酯合成反应的活性，脂肪酶的固定化使之活力表达更为充分，对亲水性较强的有机溶剂有更强的耐受性，并能为其在有机溶剂中催化酯合成反应提供必需水。考察了ＰＨ值，底物种类对固定化酵母脂肪酶催化酯合成反应的影响。     

高浓度盐系统中指肪酶的固定化及其催化活力

选择了四十多个可溶性的盐，实现了脂肪酶在高浓度盐系统中的固定化，并以 固定化脂肪酶的盐为催化剂，研究了正已烷中脂肪酶催化丁醇和乙酸乙烯酯间的转 酯化制备乙酸丁酯的反应和水溶液中橄榄油的水解反应，考察了高浓度盐系统中脂 肪酶的催化活力。     

树脂D732负载磷钨酸催化合成水杨酸酯

在水杨酸和正丁醇反应中,采用强酸性阳离子树脂D732负载磷钨酸为催化剂,合成了水杨酸酯。考察了醇/酸的摩尔比、反应时间、反应温度、催化剂的用量和催化剂的重复使用性等因素对反应酯化率的影响。结果表明,在反应温度为110℃,反应时间3h,酸/醇摩尔比为1:3,催化剂质量占水杨酸总质量的20%的较优条件下,酯化率达93.2%。催化剂不经处理重复使用4次,酯化率均在83%以上。依据该较佳的工艺条件,进一步催化合成其它水杨酸酯,酯化率均超过82%,表明D732负载磷钨酸具有良好催化效果。     

聚丙烯酸甲酯载体对柱状假丝酵母脂肪酶固定化的研究（Ⅰ）

合成了一系列不同结构的聚丙烯酸甲酯，考察了它们的固定化酵母脂肪酶催化酯水解反应的效果，得到了载体孔结构对固定化效果影响的一些规律．研究了最佳吸附条件，比较ｐＨ和离子强度对酵母脂肪酶自由酶和固定化酶催化酯水解反应活力的影响．     

固定化扩展青霉脂肪酶的制备及其在玉米油转酯反应中的应用

采用吸附法对来源于扩展青霉Penicillium expansum的脂肪酶进行了固定化.从20种不同来源的树脂中筛选出固定化效率高且价格低廉的D4020树脂作为载体,系统研究了固定化条件对固定化效率及固定化酶转酯活力的影响.结果表明,最适加酶量、缓冲液pH和吸附时间分别为0.7 g/g、9.4和4 h.冻干时添加0.5%的半乳糖有助于提高固定化酶的转酯活力.在上述优化条件下,固定化酶的转酯活力为404.0 U/g,而所用的游离酶不能催化该转酯反应.利用该固定化酶催化玉米油转酯反应生产生物柴油时,叔戊醇为适宜的反应介质,其最适添加量为0.5 ml/g;适宜的酶量、加水量和反应温度分别为60.6 U/g、油重的1.2%和35℃.按醇/油摩尔比为1的比例分别在反应0、2和6 h时加入甲醇,在优化反应条件下,反应24 h后甲酯产率达85.0%;固定化脂肪酶具有较好的操作稳定性,反应10批次时,相对酶活力为62.8%.     

脂肪酶催化吉法酯的合成研究

吉法酯(Gefarnate)是一种异戊间二烯化合物,化学名为5,9,13-三甲基-4,8,12-十四三烯酸-3',7'-二甲基-2',6'-辛二烯醇酯。本文主要目的是通过对脂肪酶催化法尼基乙酸和香叶醇的酯化反应合成吉法酯的化学反应条件进行优化,初步建立一套条件温和且污染小的酶催化法制备吉法酯的合成工艺。本文在脂肪酶(Lipozyme 435)催化法尼基乙酸和香叶醇发生酯化反应的条件下,系统研究了酶催化剂、溶剂、投料比、温度等合成条件对酯化反应的影响;结果表明,以Lipozyme 435(0.2 eq)作为催化剂,环已烷作为溶剂,在30℃条件下得到了78.4%的GC收率。该方法具有反应条件温和,副反应少,产率高,催化剂可重复利用等优点,这为进一步吉法酯的工业化合成奠定了良好的基础。     

Enzymatic Synthesizing of Phytosterol Oleic Esters

A method of synthesizing the phytosterol esters from oleic acid and sterols was studied, using immobilized lipase Candida sp. 99-125 as catalyst. Molar ratio (oleic acid/phytosterols), temperature, reaction period, organic solvents, catalyst, and silica-gel drier were optimized, and the result showed that 93.4% of the sterols had been esterified under the optimal synthetic condition: the molar ratio of oleic acid/phytosterol is 1:1 in 10 mL iso-octane, immobilized lipase (w, 140% of the sterols), incubated in an orbital shaker (200 rpm) at a temperature of 45 °C for 24 h. The immobilized lipase could be reused for at least 13 times with limited loss of esterification activity. The conversion still maintained up to 86.6%. Hence, this developed process for synthesizing phytosterol esters could be considered as simple and low-energy consumption compared to existing chemical processes.     

Ester synthesis catalyzed by Mucor miehei lipase immobilized on magnetic polysiloxane-polyvinyl alcohol particles

Mucor miehei lipase was immobilized on magnetic polysiloxane-polyvinyl alcohol particles by covalent binding with high activity recovered. The performance of the resulting immobilized biocatalyst was evaluated in the synthesis of flavor esters using heptane as solvent. The impact on reaction rate was determined for enzyme concentration, molar ratio of the reactants, carbon chain length of the reactants, and alcohol structure. Ester synthesis was maximized for substrates containing excess acyl donor and lipase loading of 25 mg/mL. The biocatalyst selectivity for the carbon chain length was found to be different concerning the organic acids and alcohols. High reaction rates were achieved for organic acids with 8 or 10 carbons, whereas increasing the alcohol carbon chain length from 4 to 8 carbons gave much lower esterification yields. Optimal reaction rate was determined for the synthesis of butyl caprylate (12 carbons). Esterification performance was also dependent on the alcohol structure, with maximum activity occurring for primary alcohol. Secondary and tertiary alcohols decreased the reaction rates by more than 40%.     

Solvent-Free Production of Bioflavors by Enzymatic Esterification of Citronella (<Emphasis Type="Italic">Cymbopogon winterianus</Emphasis>) Essential Oil

Enzymatic esterification of citronella essential oil towards the production of geranyl and citronellyl esters may present great scientific and technological interest due to the well-known drawbacks of the chemical-catalyzed route. In this context, this work reports the maximization of geranyl and citronellyl esters production by esterification of oleic and propionic acids in a solvent-free system using a commercial immobilized lipase as catalyst. Results of the reactions showed that the strategy adopted for the experimental design proved to be useful in evaluating the effects of the studied variables on the reaction conversion using Novozym 435 as catalyst. The operating conditions that maximized the production of each ester were determined, leading, in a general way, to conversions of about 90% for all systems. New experimental data on enzymatic esterification of crude citronella essential oil for geranyl and citronellyl esters production in solvent-free system are reported in this work.     

Process development for production of medium chain triglycerides using immobilized lipase in a solvent-free system

The synthesis of tricaprylin, tricaprin, trilaurin, and trimyristin in a solvent-free system was conducted by mixing a commercial immobilized lipase with the organic reagents (glycerol and fatty acid) in a 20-mL batch reactor with constant stirring. The effects of temperature, fatty acid/glycerol molar ratio, and enzyme concentration on the reaction conversion were determined. The reactions were carried out for 26 h and the nonpolar phase was analyzed by gas chromatography. Appreciable levels of medium chain triglycerides were achieved, except for tricaprylin. The higher selectivity values for the production of triglycerides were attained under the following conditions: a fatty acid/glycerol molar ratio of 5; enzyme concentration of 5 or 9% (w/w); and temperatures of 70°C (tricaprin), 80°C (trilaurin), and 90°C (trimyristin). After completion of the esterification reaction under these conditions, the recovery of the triglyceride and fatty acids, and the reusability of the enzyme were studied. The unreacted fatty acid and the produced triglyceride were satisfactorily recovered. The commercial immobilized lipase was used in 10 consecutive batch reactions at 80°C, with 100% selectivity in the trilaurin and trimyristin synthesis. The possibility of enzyme reuse and the recovery of residual fatty acid are relevant results that contribute to increasing the viability of the process.     

Effect of the Presence of Surfactants and Immobilization Conditions on Catalysts’ Properties of <Emphasis Type="Italic">Rhizomucor miehei</Emphasis> Lipase onto Chitosan

Lipase from Rhizomucor miehei (RML) was immobilized onto chitosan support in the presence of some surfactants added at low levels using two different strategies. In the first approach, the enzyme was immobilized in the presence of surfactants on chitosan supports previously functionalized with glutaraldehyde. In the second one, after prior enzyme adsorption on chitosan beads in the presence of surfactants, the complex chitosan beads-enzyme was then cross-linked with glutaraldehyde. The effects of surfactant concentrations on the activities of free and immobilized RML were evaluated. Hexadecyltrimethylammonium bromide (CTAB) promoted an inhibition of enzyme activity while the nonionic surfactant Triton X-100 caused a slight increase in the catalytic activity of the free enzyme and the derivatives produced in both methods of immobilization. The best derivatives were achieved when the lipase was firstly adsorbed on chitosan beads at 4 °C for 1 h, 220 rpm followed by cross-link the complex chitosan beads-enzyme with glutaraldehyde 0.6% v.v^?1 at pH 7. The derivatives obtained under these conditions showed high catalytic activity and excellent thermal stability at 60° and 37 °C. The best derivative was also evaluated in the synthesis of two flavor esters namely methyl and ethyl butyrate. At non-optimized conditions, the maximum conversion yield for methyl butyrate was 89%, and for ethyl butyrate, the esterification yield was 92%. The results for both esterifications were similar to those obtained when the commercial enzyme Lipozyme® and free enzyme were used in the same reaction conditions and higher than the one achieved in the absence of the selected surfactant.     

One-pot sequences of reactions with sol-gel entrapped opposing reagents: an enzyme and metal-complex catalysts

We extend our sol-gel methodology of one-pot sequences of reactions with opposing reagents to an enzyme/metal-complex pair. Sol-gel entrapped lipase and sol-gel entrapped RhCl[P(C(6)H(5))(3)](3) or Rh(2)Co(2)(CO)(12) were used for one-pot esterification and C-C double bond hydrogenation reactions, leading to saturated esters in good yields. When only the enzyme is entrapped, the homogeneous catalysts quench its activity and poison it. Thus, when 10-undecenoic acid and 1-pentanol were subjected in one pot to the entrapped lipase and to homogeneously dissolved RhCl[P(C(6)H(5))(3)](3) under hydrogen pressure, only 7% of the saturated 1-pentyl undecanoate was obtained. The yield jumped 6.5-fold when both the enzyme and the catalyst were immobilized separately in silica sol-gel matrixes. Similar one-pot esterifications and hydrogenations by sol-gel entrapped lipase and heterogenized rhodium complexes were carried out successfully with the saturated nonoic, undecanoic, and lauric acids together with several saturated and unsaturated alcohols. The use of (S)-(-)-2-methylbutanol afforded an optically pure ester. The heterogenized lipase is capable of inducing asymmetry during esterification with a prochiral alcohol. Both the entrapped lipase and the immobilized rhodium catalysts can be recovered simply by filtration and recycled in further runs without loss of catalytic activity.     

Esterification Synthesis of Ethyl Oleate in Solvent-Free System Catalyzed by Lipase Membrane from Fermentation Broth

In this study, the immobilized lipase was prepared by fabric membrane adsorption in fermentation broth. The lipase immobilization method in fermentation broth was optimized on broth activity units and pH adjustments. The viscose fermentation broth can be used with a certain percentage of dilution based on the original broth activity units. The fermentation broth can be processed directly without pH adjustment. In addition, the oleic acid ethyl ester production in solvent-free system catalyzed by the immobilized lipase was optimized. The molar ratio of ethanol to oil acid, the enzyme amount, the molecular amount, and the temperature were 1:1, 12% (w/w), 9% (w/w)(based the total amount of reaction mixture), and 30 °C, respectively. Finally, the optimal condition afforded at least 19 reuse numbers with esterification rate above 80% under stepwise addition of ethanol. Due to simple lipase immobilization preparation, acceptable esterification result during long-time batch reactions and lower cost; the whole process was suitable for industrial ethyl oleate production.     

Production of citronellyl acetate in a fed-batch system using immobilized lipase

Several reports exist in the literature citing the decrease in conversion rates of organic-phase catalytic synthesis reactions when acetic acid is present as a reaction component. This inhibition is thought to result from damage to either the hydration layer-protein interaction or the overall enzyme structure. In this work, the inhibitory effect of acetic acid on lipase enzyme activity was ameliorated by conducting syntheses under acetic acid-limiting conditions in a fed-batch system, resulting in higher product yields. Periodic additions of acetic acid at levels of 40 mM or less gave maximum yields of 65% conversion for the reaction of citronellol and acetic acid to form citronellyl acetate. The enzyme used was a fungal lipase fromMucor miehei, and was immobilized on macroporous synthetic resin (a Novo lipozyme Novo Nordisk, Denmark). These results represent a fourfold improvement over batch runs reported in the literature for direct esterification of terpene alcohol with acetic acid using lipozyme as a catalytic agent.     

Synthesis of Aliphatic Esters of Cinnamic Acid as Potential Lipophilic Antioxidants Catalyzed by Lipase B from Candida antarctica

Immobilized lipase from Candida antarctica (Novozyme 435) was tested for the synthesis of various phenolic acid esters (ethyl and n-butyl cinnamate, ethyl p-coumarate and n-butyl p-methoxycinnamate). The second-order kinetic model was used to mathematically describe the reaction kinetics and to compare present processes quantitatively. It was found that the model agreed well with the experimental data. Further, the effect of alcohol type on the esterification of cinnamic acid was investigated. The immobilized lipase showed more ability to catalyze the synthesis of butyl cinnamate. Therefore, the process was optimized for the synthesis of butyl cinnamate as a function of solvent polarity (logP) and amount of biocatalyst. The highest ester yield of 60.7 % was obtained for the highest enzyme concentration tested (3 % w/w), but the productivity was for 34 % lower than the corresponding value obtained for the enzyme concentration of 1 % (w/w). The synthesized esters were purified, identified, and screened for antioxidant activities. Both DPPH assay and cyclic voltammetry measurement have shown that cinnamic acid esters have better antioxidant properties than cinnamic acid itself.