离子液体修饰的SBA-16材料在猪胰脂肪酶固定化中的应用

合成了功能化的甲基咪唑类离子液体,并将功能化离子液体修饰介孔材料SBA-16。以三乙酸甘油酯的水解为探针反应,考察离子液体修饰的SBA-16固定化猪胰脂肪酶(PPL)的酶活、最适反应条件及重复稳定性等酶学性质。结果表明:固定化酶对温度的敏感度降低,酶活力及稳定性均显著提高,比酶活是原粉SBA-16固定化酶的1.75倍,重复使用6次后仍然保持最初活性的57%;与原粉SBA-16固定化酶保留的38%相比,有明显的提高。同时通过N2吸附-脱附、红外光谱和热重等方法分析了离子液体修饰对SBA-16结构的影响,结果发现,离子液体修饰后材料保持了原有的介孔结构,修饰后载体表面性质和结构性质导致了PPL酶学性质的变化。     

超临界二氧化碳流体萃取草珊瑚的工艺研究

本文报道了二氧化碳超临界流体萃取草珊瑚的操作过程,得出了CO_2-SFE及CO_2-SFE乙醇夹带剂两种方法的最佳工艺条件。     

南极假丝酵母脂肪酶B(CALB)基因在乳酸乳球菌MG1363中的整合及表达

根据南极假丝酵母脂肪酶B (CALB)的基因序列将CALB基因进行TA克隆、酶切鉴定及测序后,亚克隆至大肠杆菌-乳酸乳球菌穿梭表达栽体pMG36e-Nisl中,构建重组表达栽体pMG36e-Nisl-CALB.设计特异性引物P3和P4,对重组质粒pMG36e-NisI-CALB进行红霉素抗性基因的敲除,以构建食品级表达载体pMG36N-CALB,后再将两种重组质粒分别电转化入乳酸乳球菌MG1363,以Nisin为选择压力,考察CALB在MG1363中的表达情况.结果显示,成功构建了表达载体pMG36e-NisI-CALB及pMG36N-CALB,两株重组菌在含有20 IU Nisir/mL的培养基中均生长情况良好,遗传性能稳定,且经水解圈鉴定,CALB能够进行活性表达.进一步研究发现,CALB基因整合到乳酸乳球菌MG1363染色体中.     

复合脂肪酶协同催化制备生物柴油的研究

【目的】探讨复合酶协同催化体系在含水量较高的体系中催化油脂制备生物柴油的工艺条件。【方法】通过基因工程手段在毕赤酵母中分别高效分泌表达南极假丝酵母脂肪酶(CALB)和米根霉脂肪酶(ROL),构建CALB和ROL复合酶协同催化体系制备生物柴油,利用单因素实验优化工艺条件,以甲酯化得率作为复合酶协同催化体系效能的评价标准。【结果】优化工艺条件为:CALB?ROL最佳复合酶配比为7?3,每克大豆油中加入16 U的复合脂肪酶,甲醇与大豆油摩尔比为4?1,并按0 h时2?1醇油摩尔比,12 h和24 h时以1?1醇油摩尔比分批加入甲醇,含水量为30%-60%之间,40°C反应29-34 h,甲酯得率达到93%。【结论】该复合酶协同催化体系对环境友好,与常规酶法制备生物柴油工艺相比对酶的使用量和催化时间减少幅度都在50%以上,本复合酶协同催化体系能有效降低生物柴油制备成本,具有较好的工业化应用前景。     

含离子液体体系中固定化细胞转化甘草酸生成单葡萄糖醛酸基甘草次酸

研究疏水性离子液体1-丁基-3-甲基咪唑六氟磷酸盐([BMIM]PF6)与醋酸-醋酸钠缓冲液两相体系中,固定化产紫青霉Penicillium purpurogenum Li-3细胞转化甘草酸(GL)生成单葡萄糖醛酸基甘草次酸(GAMG)的反应,并与缓冲液单相体系作为对照.确定了在[BMIM]PF6/缓冲液两相体系中,最适离子液体加入比例、缓冲液pH、反应温度、底物浓度分别为10%、5.8、35℃和6.0mmol/L,在此条件下反应58h,甘草酸转化率为87.03%,比缓冲液单相体系提高了15.02%.离子液体循环使用8次后,回收利用率维持在85.28%.主产物GAMG和副产物甘草次酸(GA)在两相体系中得到有效分离,为后续产物分离带来便利.     

器壁固定化脂肪酶Pseudomonas cepacia lipase的非水活性与稳定性

许多脂肪酶在有机体系中表现出催化作用,可用于绿色有机合成. 但其催化活性和稳定性明显低于水/油（有机相）界面上的表现. 为了提高脂肪酶在有机反应体系中的活性和稳定性,依据脂肪酶的界面活化机制,以水为酶蛋白构象优化剂、羧甲基纤维素为赋形剂,通过物理吸附的方式,将典型的假单胞菌脂肪酶（Pseudomonas cepacia lipase）固定在锥形瓶的内壁上,形成简易的生物反应器. 为方便检测器壁固定化酶促反应动力学,选择特征吸收为640 nm的生化指示剂2,6-二氯靛酚为反应底物,乙酸乙烯酯为酰化试剂,丙酮为溶剂. 光谱检测表明,催化反应0.5 h后,器壁固定化脂肪酶转化底物的能力是脂肪酶粉的6倍. 在每次催化5 h共10次的循环催化中,器壁固定化脂肪酶的催化活性平均每次仅降低3.2%,而酶粉降低11.8%. 结果表明,该器壁固定化脂肪酶的活性和稳定性相对于酶粉明显提高,这将为通过固定化有效提高脂肪酶的非水催化作用提供重要的参考.     

离子液体的性能及应用

离子液体不仅可用作环境友好的“绿色溶剂”,而且在生物合成和有机反应中能表现出特殊的催化、促进效应。在介绍离子液体种类、性质、合成方法的基础上,重点综述离子液体功能化方法、离子液体／超临界CO2体系和其在生物催化反应中应用的最新研究进展。     

毕赤酵母展示表达南极假丝酵母脂肪酶B

将南极假丝脂肪酶B(CALB)基因N端和C端,分别与酿酒酵母絮凝蛋白(Flo1p)絮凝结构域序列的N端(FS)和C端(FL)融合,构建成脂肪酶毕赤酵母表面展示载体KFS和KFL,并转化毕赤酵母GS115后获得重组子KFS-CALB和KFL-CALB。免疫荧光检测证实脂肪酶已展示于毕赤酵母细胞表面。甲醇诱导120 h后展示酶活性分别达到286 U/g干细胞和182 U/g干细胞。酶的热稳定性较游离酶有较大提高,50℃孵育4 h后KFS-CALB菌株的残留酶活力仍保持初始酶活力70%以上;KFL-CALB在50℃孵育2 h后的酶活力也达到初始酶活力50%,远远高于游离态的CALB,其在50℃孵育0.5 h后仅残留18%的初始酶活力。     

非水相体系酶催化反应研究进展

非水相酶催化反应是酶催化反应中的一个重要方面。非水相溶剂通常可增加底物溶解度,减少水相中的副反应,加快生物催化的速率和效率,在药物及药物中间体和食品等方面具有较大的应用价值。以下探讨了非水相体系对酶活力及酶促反应速率的影响因素,并阐述酶的化学修饰、固定化及定点突变对酶活力的影响,进一步分析无溶剂系统、反胶束、超临界流体及离子液体的不同溶剂体系对酶反应速率及催化效率的影响。此外,还列举一些非水相酶催化反应的应用实例。     

微水——有机溶剂两相体系中消旋萘普生的酶法拆分

研究了微水－有机溶剂两相体系中固定化脂肪酶催化的萘甲酯的立体选择性水解反应,固定化酶活性受载体极性、水含量、有机溶剂的ｌｏｇＰ值,产物抑制的影响,据此构建了一种可以连续拆分产生（Ｓ）－（＋）－萘普生的微水－有机溶剂两相体系。反应在一个具有回路的连续流搅拌反应器中进行,反应器中添加有采用吸附法固定化的脂肪酶,截体为一种弱极性的合成载体,水相连同固定化酶颗粒一起永久保持在反应器中,有机流动相带入底物,     

Buffer-mediated activation of Candida antarctica lipase B dissolved in hydroxyl-functionalized ionic liquids

Ionic-liquid buffer having phosphate anion was synthesized for the development of buffered enzymatic ionic liquid systems. Both the conformation and transesterification activity of Candida antarctica lipase B (CALB) dissolved in the hydroxyl-functionalized ionic liquids were buffer dependent. Intrinsic fluorescence studies indicated that the CALB possessed a more compact conformation in the medium consisted of ionic liquid buffer having phosphate anion and hydroxyl-functionalized ionic liquids like 1-(1-hydroxyethyl)-3-methyl-imidazolium tetrafluoroborate and 1-(1-hydroxyethyl)-3-methyl-imidazolium nitrate. High activity and outstanding stability could be obtained with the CALB enzyme in the buffered ionic liquids for the transesterification.     

Criteria to design green enzymatic processes in ionic liquid/supercritical carbon dioxide systems

Five different ionic liquids (ILs) based on quaternary ammonium cations, with functional side chains ((3-hydroxypropyl)-trimethyl-, (3-cyanopropyl)-trimethyl-, butyl-trimethyl-, (5-cyanopentyl)-trimethyl- and hexyl-trimethyl-) associated with the same anion (bis(trifluoromethane)sulfonyl amide)), were synthesized, and their suitability for Candida antarctica lipase B (CALB)-catalyzed ester synthesis in IL/supercritical carbon dioxide (scCO(2)) biphasic systems was assayed. Catalytic efficiency of the system has been analyzed as a function of both enzyme properties and mass-transfer phenomena criteria. First, the suitability of these ILs as enzymic reaction media was tested for the kinetic resolution of rac-phenylethanol. All ILs were found to be suitable media for enzyme catalysis, the best catalytic parameter (5.3 U/mg specific activity, 94.9% selectivity) being obtained for the (5-cyanopentyl)-trimethylammonium. Second, enzyme stability in all of the ILs was studied at 50 degrees C over a period of 50 days, and data were analyzed by a two-step kinetic deactivation model. All of the ILs were shown to act as stabilizing agents with respect to hexane, producing an increase in the free energy of deactivation (to 25 kJ/mol protein) and an improvement in the half-life time of the enzyme (2000-fold), which agrees with the observed increased hydrophobicity of the cation alkyl side chain (measured by Hansen's solubility parameter, delta). By using two different CALB-IL systems with different hydrophobicity in the cation, continuous processes to synthesize six different short chain alkyl esters (butyl acetate, butyl propionate, butyl butyrate, hexyl propionate, hexyl butyrate, and octyl propionate) in scCO(2) at 10 MPa and 50 degrees C were carried out. Both rate-limiting parameters (synthetic activity and scCO(2)-ILs mass-transfer phenomena) were related with the delta-parameter of the ILs-alkyl chain and reagents.     

Production of biodiesel fuel from soybean oil catalyzed by fungus whole-cell biocatalysts in ionic liquids

The methanolysis of soybean oil to produce a fatty acid methyl ester (ME, i.e., biodiesel fuel) was catalyzed by lipase-producing filamentous fungi immobilized on biomass support particles (BSPs) as a whole-cell biocatalyst in the presence of ionic liquids. We used four types of whole-cell biocatalysts: wild-type Rhizopus oryzae producing triacylglycerol lipase (w-ROL), recombinant Aspergillus oryzae expressing Fusarium heterosporum lipase (r-FHL), Candida antarctica lipase B (r-CALB), and mono- and diacylglycerol lipase from A. oryzae (r-mdlB). w-ROL gave the high yield of fatty acid methyl ester (ME) in ionic liquid [Emim][BF₄] or [Bmim][BF₄] biphasic systems following a 24 h reaction. While lipases are known to be severely deactivated by an excess amount of methanol (e.g. 1.5 Mequiv. of methanol against oil) in a conventional system, methanolysis successfully proceeded even with a methanol/oil ratio of 4 in the ionic liquid biphasic system, where the ionic liquids would work as a reservoir of methanol to suppress the enzyme deactivation. When only w-ROL was used as a biocatalyst for methanolysis, unreacted mono-glyceride remained due to the 1,3-positional specificity of R. oryzae lipase. High ME conversion was attained by the combined use of two types of whole-cell biocatalysts, w-ROL and r-mdlB. In a stability test, the activity of w-ROL was reduced to one-third of its original value after incubation in [Bmim][BF₄] for 72 h. The stability of w-ROL in [Bmim][BF₄] was greatly enhanced by cross-linking the biocatalyst with glutaraldehyde. The present study demonstrated that ionic liquids are promising candidates for use as the second solvent in biodiesel fuel production by whole-cell biocatalysts.     

Chemoenzymatic dynamic kinetic resolution of rac-1-phenylethanol in ionic liquids and ionic liquids/supercritical carbon dioxide systems

Continuous dynamic kinetic resolution processes in different ionic liquid/supercritical carbon dioxide biphasic systems were carried out by simultaneously using both immobilized Candida antarctica lipase B (Novozym 435) and silica modified with benzenosulfonic acid (SCX) catalysts at 40°C and 10 MPa. SCX was seen to act as an efficient heterogeneous chemical catalyst for the racemization of (S)-1-phenylethanol in different ionic liquid media ([emim][NTf₂], [btma][NTf₂] and [bmim][PF₆]). Coating both chemical and enzymatic catalysts with ILs greatly improved the efficiency of the process, providing a good yield (76%) of (R)-1-phenylethyl propionate product with excellent enantioselectivity (ee = 91–98%) in continuous operation.     

Expression of Candida antarctica lipase B in Pichia pastoris and various Escherichia coli systems

Candida antarctica lipase B (CALB) carrying a point mutation, N74S, resulting in a non-glycosylated protein was actively expressed in Pichia pastoris yielding 44 mg/L which was similar to that of the glycosylated CALB wild type expressed in P. pastoris. Hence, the major obstacle in the Escherichia coli expression of CALB is not the lack of glycosylation. To understand and improve the expression of CALB in E. coli, a comprehensive investigation of four different systems were tested: periplasmic expression in Rosetta (DE3), cytosolic expression in Rosetta-gami 2(DE3) and Origami 2(DE3) as well as co-expression with chaperones groES and groEL in Origami B(DE3), all using the pET-22b(+) vector and the T7lac promoter. Furthermore the E. coli expression was carried out at three different temperatures (16, 25 and 37 degrees C) to optimise the expression. Periplasmic expression resulted in highest amount of active CALB of the four systems, yielding a maximum of 5.2mg/L culture at 16 degrees C, which is an improvement to previous reports. The specific activity of CALB towards tributyrin in E. coli was found to be the same for periplasmic and cytosolic expression. Active site titration showed that the CALB mutant N74S had a lower specific activity in comparison to wild type CALB regardless of expression host. The expected protein identity was confirmed by LC-ESI-MS analysis in E. coli, whereas in P. pastoris produced CALB carried four additional amino acids from an incomplete protein processing.     

Simulation of protein diffusion: a sensitive probe of protein–solvent interactions

Aqueous solutions of Candida antarctica lipase B (CALB) were simulated considering three different water models (SPC/E, TIP3P, TIP4P) by a series of molecular dynamics (MD) simulations of three different box sizes (L = 9, 14, and 19 nm) to determine the diffusion coefficient, the water viscosity and the protein density. The protein–water systems were equilibrated for 500 ns, followed by 100 ns production runs which were analysed. The diffusional properties of CALB were characterized by the Stokes radius (R_S), which was derived from the diffusion coefficient and the viscosity. R_S was compared to the geometric radius (R_G) of CALB, which was derived from the protein density. R_S and R_G differed by 0.27 nm for SPC/E and by 0.40 and 0.39 nm for TIP3P and TIP4P, respectively, which characterizes the thickness of the diffusive hydration layer on the protein surface. The simulated hydration layer of CALB resulted in agreement with those experimentally determined for other seven different proteins of comparable size. By avoiding the most common pitfalls, protein diffusion can be reliably simulated: simulating different box sizes to account for the finite size effect, equilibrating the protein–water system sufficiently, and using the complete production run for the determination of the diffusion coefficient.     

Influence of cosolvents on the hydrophobic surface immobilization topography of Candida antarctica lipase B

The presence of cosolvents and co-solutes during the immobilization of lipases on hydrophobic supports may influence the extent of lipase immobilization and the long-term catalytic stability of the biocatalyst. Candida antarctica B lipase immobilization was examined on a hydrophobic surface, i.e., gold modified with a methyl-terminated, self-assembled alkylthiol layer. Lipase adsorption was monitored gravimetrically using a quartz crystal microbalance (QCM). Lipase activity was determined colorimetrically by following p-nitrophenol propionate hydrolysis. Adsorbed lipase topography was examined by atomic force microscopy (AFM). Lipase adsorption from low ionic strength aqueous buffer produced a uniform confluent protein monolayer. Inclusion of 10% (vol) ethanol in the buffer during immobilization resulted in a 33% adsorbed mass increase. Chemically similar cosolvents, all at 10% by volume in buffer, were also individually examined for their influence on CALB adsorption. Glycerol or 1-propanol increased mass adsorption by 10%, while 2-propanol increased mass adsorption by 33%. QCM dissipation values increased threefold with the inclusion of either ethanol or 2-propanol in the medium during lipase adsorption, indicating formation of multilayers of CALB. Partial multilayer formation using 10% ethanol was confirmed by AFM. Inclusion of 10% ethanol in the CALB immobilization buffer decreased the specific activity of the immobilized lipase by 37%. The formation of lipase multilayers in the presence of certain cosolvents thus results in lower specific activity, which might be due to either influences on lipase conformation or substrate active site accessibility.     

Influence of ionic liquids as additives on sol–gel immobilized lipase

The immobilization of lipase from Candida rugosa, using ionic liquids as additives to protect the inactivation of lipase by released alcohol and shrinking of gel during sol–gel process, was investigated. The influence of various factors, such as structure of ionic liquids, content of ionic liquids and types of precursor in the sol–gel process on the activity and stability of immobilized lipase was also studied. The highest hydrolytic activity of immobilized lipase was obtained when the hydrophilic ionic liquid, [C₂mim][BF₄], was used as an additive, while the highest stability of immobilized lipase was obtained by using hydrophobic ionic liquid, [C₁₆mim][Tf₂N]. Therefore, the binary mixtures of these ionic liquids as additives were used to obtain the optimal immobilized lipase, which shows both high activity and stability. The hydrolysis and esterification activities of lipase co-immobilized with the mixture of 1:1 at molar ratio of [C₂mim][BF₄] and [C₁₆mim][Tf₂N] were 10-fold and 14-fold greater than in silica gel without ionic liquids (ILs), respectively. After 5 days incubation of this immobilized lipase in n-hexane at 50 °C, 84% of initial activity was remained, while the residual activity of the lipase immobilized without ILs was 28%.     

Immobilized Candida antarctica lipase B: Hydration, stripping off and application in ring opening polyester synthesis

This work reviews the stripping off, role of water molecules in activity, and flexibility of immobilized Candida antarctica lipase B (CALB). Employment of CALB in ring opening polyester synthesis emphasizing on a polylactide is discussed in detail. Execution of enzymes in place of inorganic catalysts is the most green alternative for sustainable and environment friendly synthesis of products on an industrial scale. Robust immobilization and consequently performance of enzyme is the essential objective of enzyme application in industry. Water bound to the surface of an enzyme (contact class of water molecules) is inevitable for enzyme performance; it controls enzyme dynamics via flexibility changes and has intensive influence on enzyme activity. The value of pH during immobilization of CALB plays a critical role in fixing the active conformation of an enzyme. Comprehensive selection of support and protocol can develop a robust immobilized enzyme thus enhancing its performance. Organic solvents with a log P value higher than four are more suitable for enzymatic catalysis as these solvents tend to strip away very little of the enzyme surface bound water molecules. Alternatively ionic liquid can work as a more promising reaction media. Covalent immobilization is an exclusively reliable technique to circumvent the leaching of enzymes and to enhance stability. Activated polystyrene nanoparticles can prove to be a practical and economical support for chemical immobilization of CALB. In order to reduce the E-factor for the synthesis of biodegradable polymers; enzymatic ring opening polyester synthesis (eROPS) of cyclic monomers is a more sensible route for polyester synthesis. Synergies obtained from ionic liquids and immobilized enzyme can be much effective eROPS.     

Molecular and phase toxicity of compressed and supercritical fluids in biphasic continuous cultures of Clostridium thermocellum

A novel continuous high-pressure biphasic bioreactor was designed to investigate the toxicity of compressed and supercritical fluids on the thermophilic bacterium Clostridium thermocellum. Cultures were conducted at 1.8 and 7.0 MPa hydrostatic pressure and in the presence of compressed N(2) (7.0 MPa), gaseous (1.8 MPa) and supercritical ethane (7.0 MPa), and gaseous (1.8 MPa) and liquid (7.0 MPa) propane at a single dilution rate. No significant changes in metabolism or growth were observed in the presence of compressed N(2) relative to 7.0 MPa hydrostatic pressure, indicating that it acted as an inert fluid. However, dramatic inhibitions of growth and metabolism occurred in the presence of ethane and propane at 7.0 MPa. These inhibitions were reversed by depressurization from the supercritical (ethane) or liquid (propane) to gaseous state. Solvent toxicity by compressed and supercritical fluids was attributed to phase toxicity and was correlated with fluid density rather than conventional measures of toxicity (log P(o/w)). This biphasic reactor system facilitates investigations of solvent toxicity and dissolved gas effects on whole cells under elevated pressures.