硫酸铵-丙酮协同沉淀法纯化南极假丝酵母产脂肪酶

采用硫酸铵-丙酮协同沉淀法,对南极假丝酵母产脂肪酶(CALB)进行了分离纯化研究.经正交实验确定纯化工艺为:向酶液中加入硫酸铵至饱和度45%的同时加入0.3倍酶液体积的丙酮;离心后再向上清液中加入硫酸铵至饱和度75%,分相后,相界面处沉淀即为脂肪酶粗品.经分离纯化后,酶活回收率为54%、纯化倍数为2.72.     

双水相萃取技术在分离、纯化中的应用

双水相技术是一种新型的液-液萃取技术,由于其条件温和、易操作等特点,目前已广泛应用于物质的分离、纯化。本文综述了双水相形成原理、工艺流程和特点、体系类别、影响双水相分配的因素及其在分离纯化中的应用,并针对其未来发展趋势进行了展望。     

双水相萃取技术分离纯化蛋白质的研究

阐述了双水相萃取原理,详细分析了影响双水相萃取分离纯化蛋白质的各种因素,探讨了双水相萃取技术在蛋白质分离纯化中的应用并对其前景进行了展望.     

双水相萃取法分离纯化黄酮类化合物的研究进展

综述双水相体系的组成、特点和双水相萃取法分离纯化黄酮类化合物的研究进展。双水相萃取是一项利用不复杂的设备,并在温和条件下进行简单的操作就可获得较高收率和有效成分的新型分离技术,该技术在黄酮类化合物的分离分析中取得了较好的效果,有望成为一种新型的黄酮类化合物的分离纯化方法。     

南极假丝酵母脂肪酶发酵条件优化及酶学性质

分别用摇瓶和15L发酵罐,对南极假丝酵母产胞外脂肪酶的培养基成分和操作条件进行了实验研究。得到最优的培养基组成为:豆粉40g／L,淀粉15g／L,豆油5mL／L,K2HPO4g／L,MgsO4·7H2O1g／L,Tween-800.1％,酵母膏5g／L;操作条件为:温度24℃,初始pH值为6.0,通气量为10.0L／min。在此培养条件下,发酵周期缩短至54h。由15L发酵罐生产的酶液酶活达到19.2U／mL。酶液在pH值为4.0～6.0和7.5～9.0范围内较稳定,其最适宜pH值范围为6～8.5;70℃时酶的催化活性最大.在40～70℃的温度范围内保持1h后残留酶活为60％。     

用蛋白质工程技术提取和修饰南极假丝酵母脂肪酶B

从南极假丝酵母中提取的脂肪酶B,具有较高的对应异构体选择性,广泛应用在培养基中,作为不对称有机化学的生物催化剂。近年来,一系列组合蛋白质工程研究和扩展了南极假丝酵母脂肪酶的催化和物理特性。这些工程不但生产出了指定的催化剂,还有助于阐明酶的结构一作用关系,并且有助于说明这些酶的对应异构体选择性。进一步的研究将在工程与酶的关系方面展开讨论。     

固定化假丝酵母脂肪酶催化合成辛酸甘油酯

以自制固定化假丝酵母脂肪酶作为催化剂,研究了无溶剂体系中辛酸和甘油直接酯化合成辛酸甘油酯的反应条件。考察了酶的种类、底物的物质的量之比、温度、酶量、甘油的初始含水量和反应时间等因素对辛酸转化率和产物组成的影响。结果证明,以纺织物作为载体制备的固定化假丝酵母脂肪酶适宜催化辛酸甘油酯的合成。最优反应条件为：辛酸与甘油的物质的量之比为2∶1,固定化假丝酵母脂肪酶加量为0.5g/0.69g甘油,温度为40 ℃,振荡培养箱转速为190 r/min。最优反应条件下辛酸转化率可以达到94%以上,经过简单处理的固定化酶可以重复使用4批。     

乙醛对假丝酵母脂肪酶催化活性的影响

采用紫外可见分光光度法和荧光发射光谱法研究了乙醛溶液对假丝酵母脂肪酶水解三油酸甘油酯的催化活性和构象的影响。结果表明,低浓度乙醛能提高酶的催化水解活力,当乙醛浓度为0.221 5 mmol/L时,酶活力提高了18.84%;高浓度乙醛对酶活力有抑制作用,当乙醛浓度为3.322 5 mmol/L时,酶活力降低了25.85%。低浓度乙醛使酶催化反应的最适p H向碱性方向偏移,紫外吸收光谱和荧光发射光谱均有显著增强和光谱峰偏移现象。动力学分析表明,加入乙醛后,酶的V_(max)增大,K_m减小。     

双水相萃取技术研究进展

双水相萃取技术作为一项新的分离技术日益受到重视,它与传统的萃取方法相比有独特的优点.本文综述了双水相萃取技术基本原理、特点、应用及热力学模型,并对双水相萃取技术存在的问题和发展趋势作了论述.     

双水相萃取技术研究进展

双水相萃取技术作为一项新的分离技术日益受到重视,它与传统的萃取方法相比有独特的优点,作者综述了又水相萃取技术基本原理、特点、应用及热力学模型,并对双水相萃取技术存在的问题和发展趋势作了论述.     

N-乙基-N-丁基吗啉离子液体双水相体系萃取分离蛋白质

研究了新型离子液体N-乙基-N-丁基吗啉四氟硼酸盐([Nebm]BF4)和KH2PO4形成的双水相体系对牛血清白蛋白(BSA)的萃取行为,考察了盐的加入量、离子液体浓度、溶液pH值、蛋白质浓度等因素对萃取率的影响。结果表明:当KH2PO4的加入量为85 g/L、离子液体浓度在200~250 g/L、BSA的浓度60~120 mg/L、溶液酸度在pH4.5~7.0时,其萃取率达98.0%以上。该双水相体系对α-淀粉酶的萃取率也达98.5%。     

Separation of catalase from Amsonia orientalis with single step by aqueous two-phase partitioning system (ATPS)

Catalase from Amsonia orientalis was purified by ATPS, and its efficiency was compared against hydrophobic interaction chromatography. Activity recovery and purification fold of purified catalase by ATPS were examined under varying experimental conditions. The effects of various factors such as type of phase-forming salts, (PEG) mass, with their different concentrations, pH and temperature effects on partitioning were investigated. The highest activity recovery (156%) and purification fold (8.67) of catalase were obtained in the ATPS system containing 10% (g/g) PEG4000, 15% (g/g) Na₂SO₄ at pH 6.0 and room temperature. In hydrophobic interaction chromatography, the enzyme has been purified 12.54-fold with 57.5% recovery. The molecular weight of catalase was determined as 75 kDa by SDS-PAGE.     

Improved activity and thermostability of Candida antarctica lipase B by DNA family shuffling

DNA family shuffling was used to create chimeric lipase B proteins with improved activity toward the hydrolysis of diethyl 3-(3',4'-dichlorophenyl)glutarate (DDG). Three homologous lipases from Candida antarctica ATCC 32657, Hyphozyma sp. CBS 648.91 and Crytococcus tsukubaensis ATCC 24555 were cloned and shuffled to generate a diverse gene library. A high-throughput screening assay was developed and used successfully to identify chimeric lipase B proteins having a 20-fold higher activity toward DDG than lipase B from C.antarctica ATCC 32657 and a 13-fold higher activity than the most active parent derived from C.tsukubaensis ATCC 24555. In addition, the stability characteristics of several highly active chimeric proteins were also improved as a result of family shuffling. For example, the half-life at 45 degrees C and melting point (T(m)) of one chimera exceeded those of lipase B from C.antarctica ATCC 32657 by 11-fold and 6.4 degrees C, respectively, which closely approached the stability characteristics of the most thermostable parent derived from Hyphozyma sp. CBS 648.91.     

Conversion of vegetable oil to biodiesel using immobilized Candida antarctica lipase

Biodiesel derived from vegetable oils has drawn considerable attention with increasing environmental consciousness. We attempted continuous methanolysis of vegetable oil by an enzymatic process. Immobilized Candida antarctica lipase was found to be the most effective for the methanolysis among lipases tested. The enzyme was inactivated by shaking in a mixture containing more than 1.5 molar equivalents of methanol against the oil. To fully convert the oil to its corresponding methyl esters, at least 3 molar equivalents of methanol are needed. Thus, the reaction was conducted by adding methanol stepwise to avoid lipase inactivation. The first step of the reaction was conducted at 30°C for 10 h in a mixture of oil/methanol (1:1, mol/mol) and 4% immobilized lipase with shaking at 130 oscillations/min. After more than 95% methanol was consumed in ester formation, a second molar equivalent of methanol was added and the reaction continued for 14 h. The third molar equivalent of methanol was finally added and the reaction continued for 24 h (total reaction time, 48 h). This three-step process converted 98.4% of the oil to its corresponding methyl esters. To investigate the stability of the lipase, the three-step methanolysis process was repeated by transferring the immobilized lipase to a fresh substrate mixture. As a result, more than 95% of the ester conversion was maintained even after 50 cycles of the reaction (100 d).     

Enzymatic resolution of racemic secondary alcohols by lipase B from Candida antarctica

Chiral intermediates S-(+)-2-pentanol and S-(+)-2-heptanol were prepared by a lipase-catalyzed enzymatic resolution proces. Among various lipases evaluated for the stereoselective acylation of racemic alcohols, lipase B from Candida antarctica catalyzed the acylation of the undesired enantiomer of racemic alcohols leaving the desired S-(+)-alcohols unreacted. A reaction yield of 43–45% and an enantiomeric excess (e.e.) of >99% were obtained for S-(+)-2-pentanol or S-(+)-2-heptanol when the reaction was carried out using vinyl acetate or succnic anhydride as acylating agent. In an alternative process, an enantioselective hydrolysis of 2-pentyl acetate was demonstrated using lipase B giving S-(+)-2-pentyl acetate and R-(−)-2-pentanol. A reaction yield of 45% and an e.e. of 98.6% were obtained for S-(+)-2-pentyl acetate. This work was presented at the Biocatalysis Symposium in April 2000, held at the 91st Annual Meeting and Expo of the American Oil Chemists' Society, San Diego, CA.     

Prediction of the Candida antarctica lipase A protein structure by comparative modeling and site-directed mutagenesis

A number of model structures of the CalA suggested by comparative modeling were tested by site-directed mutagenesis. Enzyme variants were created where amino acids predicted to play key roles for the lipase activity in the different models were replaced by an inert amino acid (alanine). The results from activity measurements of the overproduced and purified mutant enzymes indicate a structure where the active site consists of amino acid residues Ser184, His366, and Asp334 and in which there is no lid. This model can be used for future targeted modifications of the enzyme to obtain new substrate acceptance, better thermostability, and higher enantioselectivity.     

Glucoside ester synthesis in microemulsions catalyzed by Candida antarctica component B lipase

The surfactant, ethyl 6-O-decanoyl glucoside, was synthesized in microemulsion systems by lipase catalysis. The microemulsions were based on the two substrates for the reaction, ethyl glucoside and fatty acid, and either the sodium salt of the fatty acid or the glucoside ester was used as surfactant. The lipase used was component B from Candida antarctica. Reduced pressure was employed to eliminate the water of condensation. The reaction yield was good, with conversion of fatty acid and ethyl glucoside reaching 77 and 96%, respectively.     

Single step recovery of lipase from Penicillium cyclopium by aqueous two-phase extraction

Recovery of lipase from Penicillium cyclopium by aqueous two-phase extraction was studied with maximal possible crude enzyme loads. In polyethylene glycol/dextran and polyethylene glycol/salt systems the influences of molecular weight and concentration of polyethylene glycol, phase-forming salt and phase volume ratio were evaluated. Lipase partition coefficient 9 followed by the top phase yield 95.7% and purification factor 3.4 were achieved in 15% (w w^?1) polyethylene glycol 4000/15% (w w^?1) KH₂PO₄/70% (w w^?1) crude enzyme. Efficient single-step recovery of lipase followed by partial enzyme purification indicated possible integration of production and primary bioseparation step by aqueous two-phase extraction. By varying phase volume ratio, the concentration of phosphate was reduced without decrease in lipase recovery.     

Influence of delta-functional groups on the enantiorecognition of secondary alcohols by Candida antarctica lipase B

The selectivity of acetylation of delta-functionalized secondary alcohols catalyzed by Candida antarctica lipase B has been examined by molecular dynamics. The results from the simulation show that a delta-alcohol functionality forms a hydrogen bond with the carbonyl group of Thr 40. This interaction stabilizes the tetrahedral intermediate and thus leads to selective acetylation of the R enantiomer. A stabilizing interaction of the delta-(R)-acetoxy group with the peptide NH of alanine 282 was also observed. No stabilizing interaction could be found for the delta-keto functionality, and it is proposed that this is the reason for the experimentally observed decrease in enantioselectivity. From these results, it was hypothesized that the enantioselectivity could be restored by mutating the alanine in position 281 for serine. The mutation was made experimentally, and the results show that the E value increased from 9 to 120.     

Continuous production of biodiesel fuel from vegetable oil using immobilized Candida antarctica lipase

Candida antarctica lipase is inactivated in a mixture of vegetable oil and more than 1∶2 molar equivalent of methanol against the total fatty acids. We have revealed that the inactivation was eliminated by three successive additions of 1∶3 molar equivalent of methanol and have developed a three-step methanolysis by which over 95% of the oil triacylglycerols (TAG) were converted to their corresponding methyl esters (ME). In this study, the lipase was not inactivated even though 2∶3 molar equivalent of methanol was present in a mixture of acylglycerols (AG) and 33% ME (AG/ME33). This finding led to a two-step methanolysis of the oil TAG: The first-step was conducted at 30°C for 12 h with shaking in a mixture of the oil, 1∶3 molar equivalent of methanol, and 4% immobilized lipase; the second-step reaction was done for 24 h after adding 2∶3 molar equivalent of methanol (36 h in total). The two-step methanolysis achieved more than 95% of conversion. When two-step reaction was repeated by transferring the immobilized lipase to a fresh substrate mixture, the enzyme could be used 70 cycles (105 d) without any decrease in the conversion. From the viewpoint of the industrial production of biodiesel fuel production, the two-step reaction was conducted using a reactor with impeller. However, the enzyme carrier was easily destroyed, and the lipase could be used only several times. Thus, we attempted flow reaction using a column packed with immobilized Candida lipase. Because the lipase packed in the column was drastically inactivated by feeding a mixture of AG/ME33 and 2∶3 molar equivalent of methanol, three-step flow reaction was performed using three columns packed with 3.0 g immobilized lipase. A mixture of vegetable oil and 1∶3 molar equivalent of methanol was fed into the first column at a constant flow rate of 6.0 mL/h. The eluate and 1∶3 molar equivalent of methanol were mixed and then fed into the second column at the same flow rate. The final step reaction was done by feeding a mixture of eluate from the second column and 1∶3 molar equivalent of methanol at the same flow rate. The ME content in the final-step eluate reached 93%, and the lipase could be used for 100 d without any decrease in the conversion.