从反胶束溶液中反萃牛血清白蛋白的研究

由近红外光谱证实,十六烷基三甲基溴化铵(CTAB)/正己醇-正辛烷反胶束溶液是牛血清白蛋白(BSA)增溶于非极性有机溶剂的较理想中介。研究了反萃液酸度、离子强度和种类等参数对BSA反萃率的影响,过低的溶液酸度导致BSA变性。适宜的反萃液为:1.0～2.0mol/L KBr,pH4.3～4.9。蛋白质的紫外光谱表明,BSA分子在料液,反胶束溶液和反萃液中的构象大致相同。此外,探讨了反胶束溶液循环使用的效率问题。最后,通过采用适当的相比,成功地实现了蛋白质的回收和浓缩。     

微生物转谷氨酰胺酶(MTGase)的AOT反胶束纯化研究

研究微生物转谷氨酰胺酶(MTGase)反胶束纯化的工艺和条件,调节MTGase离心上清液等电点,除去部分杂蛋白,MTGase活力升高7.5倍;用截留分子量为10000的超滤膜除去小分子杂蛋白,MTGase活力升高1.33倍;用0.05mol/L的AOT/异辛烷反胶束进一步纯化MTGase,其最适萃取条件是粗MTGase蛋白质浓度20mg/mL,[Na ]0.12mol/L,水相pH4.80～5.20,相比1:1(v/v);荷载MTGase的AOT反胶束用2.0mol/LKCl进行反萃取,MTGase活力为14.2U/g,纯化8.875倍;冷冻干燥脱盐反萃取液,获得MTGase冻干粉,其活力为110.3U/g,与粗酶液相比较,纯化689.4倍。经过AOT/异辛烷反胶束萃取纯化的MTGase,其SDS-聚丙烯酰胺凝胶电泳为一条带。Ca2 与表面活性剂非极性尾上丁二酰羰基氧、极性头磺酸基硫氧基氧及MTGase分子表面具有孤电子对的基团的配位结合放大了AOT反胶束的另一种萃取作用——配位萃取,致使其对MTGase的萃取率高于K 而接近Na 。     

生姜蛋白酶提取及反胶束纯化工艺初步研究

本文研究了生姜中生姜蛋白酶的分布及贮藏中的活力变化 ,研究了从新鲜生姜中提取生姜粗蛋白酶及用AOT 异辛烷和CTAB庚烷 /辛醇反胶束萃取该酶的工艺和方法。实验结果指出 :在贮藏茎中生姜蛋白酶的活力为 2 .7μg/mL·min-1,在膨大茎中该酶活力为 0 .6 8μg/mL·min-1,而在幼嫩茎中活力最低 ,仅为0 .4 8μg/mL·min-1。新鲜生姜在 0℃下贮藏 2 4h即完全丧失活力 ,在室温下贮藏 3d后其活力损失达38 2 5 %。用 10倍 0 .2mol/L、pH =6 .0的磷酸缓冲液 (4℃ )三次提取生姜蛋白酶 ,其提取率分别为 6 4 .75 %、14 .2 8%和 5 .2 %。用 6 5 %饱和度的 (NH4) 2 SO4沉淀提取液中的生姜蛋白酶 ,再以 pH 6 .2、0 .1mol/L的柠檬酸缓冲液溶解 ,其比活力达到 4 .2 1(μgPro/ μgPro·min-1)。生姜蛋白酶的 pI =5 .4～ 5 .5 ,在pH 5 .4以上 ,用AOT 异辛烷反胶束不能萃取出生姜蛋白酶 ,但却可以萃取出 71.86 %的杂蛋白。用CTAB庚烷 /辛醇反胶束二次萃取AOT 异辛烷萃余液 ,其蛋白质萃取率为 6 0 .2 5 % ,萃取液中生姜蛋白酶理论比活力达到 4 9.77(μgPro/ μgPro·min-1)。     

胰凝乳蛋白酶在反胶束体系中热稳定性的研究

研究了AOT／正辛烷反胶束体系中,表面活性剂AOT,助溶剂甘油和体 压力对胰凝乳蛋白酶热稳定性的影响,结果表明;常压下,40度时,体系中的甘油浓度分别为20％,30％,50％,60％（V／V）时,酶的活力分别为原来的10％,22％,59％,48％,说明在体系中加入甘油作为助溶剂可减少胰凝乳蛋白酶的运动,增强其稳定性,同时,发现体系压力的增加也能增强酶的稳定性,实验测出,AOT正辛烷反胶束体系萃取胰凝乳蛋白酶的最佳条件：R＝10,甘油浓度为50％,体系压力为50MPa,酶的萃取率为97％。     

氯化三辛基甲胺/氯仿/正丁醇反胶束萃取地木耳多糖

采用阳离子表面活性剂氯化三辛基甲胺(TOMAC)/氯仿/正丁醇反胶束体系萃取地木耳中的多糖。分析有机溶剂氯仿与助表面活性剂正丁醇比例、TOMAC浓度、多糖粗提液浓度、促溶剂盐酸胍浓度、盐离子种类和浓度对前萃取率的影响。结果表明:向0.5 mg/m L多糖粗提液中加入10 mmol/L盐酸胍(Gu HCl)和0.06 mol/L Na Cl,与等体积25 mmol/L TOMAC/氯仿-正丁醇(V∶V=3∶1)的反胶束体系混合,地木耳多糖前萃取率为53.21%;反萃时水相中Na Cl浓度为0.14 mol/L,盐酸胍浓度浓度为0.6 mol/L,在此条件下地木耳多糖反萃取率为93.2%。     

AOT/异辛烷反胶束萃取纯化胰蛋白酶及酶变性失活问题的解决

用反胶束技术分离纯化蛋白质,具有高选择性、易于大规模操作等优点,具有良好的工业应用前景。但是离子型表面活性剂形成的反胶束体系萃取蛋白质容易引起蛋白质的变性,这是由于离子型表面活性剂的强电荷作用所导致的。对用AOT/异辛烷反胶束体系从胰酶粗提物中萃取胰蛋白酶进行了研究,通过在反胶束相加入乙醇,解决了反胶束萃取蛋白质时蛋白质变性失活的问题。并且由于乙醇的加入大大减少了分相的时间,简化了实验步骤,优化了实验方法,使此技术在工业上的大规模应用成为可能。通过优化各种实验条件,胰蛋白酶的前萃取率达到90%,反萃取率接近100%。最终得率为88%。纯化后的比活提高了5倍多,从300U/mg左右提高到了1800U/mg。     

用乙醇消除AOT/异辛烷反胶束体系萃取过程中蛋白质的变性失活

用反胶束技术分离纯化蛋白质,具有高选择性、易于大规模操作等优点,具有良好的工业应用前景。但是离子型表面活性剂形成的反胶束体系萃取蛋白质容易引起蛋白质的变性,这是由于离子型表面活性剂的强电荷作用会导致蛋白质发生变性,从而在两相界面上产生沉淀。这也是离子型反胶束体系用于蛋白质萃取所存在的最大的困难。本文对用AOT/异辛烷反胶束体系从胰酶粗提物中萃取胰蛋白酶进行了研究,通过在反胶束相加入乙醇,解决了反胶束萃取蛋白质时使蛋白质变性失活的问题,并且大大减少了分相的时间。前萃取和反萃取之后的分相时间只需要10分钟左右,简化了实验步骤,优化了实验方法,在工业上的大规模应用成为可能。在本研究中,胰蛋白酶的前萃取率达到90%,反萃取率接近100%。最终得率为88%。纯化后的比活提高了5倍多,从300U/mg左右提高到了1800U/mg。     

非离子反胶束中木素过氧化物酶催化性能研究

木素过氧化物酶（LiP）在环己烷/Brij30/水反胶束体系中可体现催化活力,然而在水/醇/TritonX100/环己烷反胶束体系中却没有催化活力。对影响Brij30反胶束中LiP催化活力各主要因素进行了优化并测定了LiP在其中的时间稳定性;结果表明,20℃下,使LiP体现最佳活力的Brij30反胶束介质条件为：ω₀＝8.5,pH＝2.2,［Brij30］＝600mmol/L;在此条件下,LiP的半衰期可达到50h;与水介质相比,酶活力下降了,但稳定性却提高了。直链醇是TritonX100形成反胶束的必要组分,为揭示醇的作用,还考察了戊醇对Brij30 反胶束中LiP催化活力的影响,发现高浓度戊醇对LiP有失活作用。据此推测助表面活性剂醇可能是LiP在环己烷/TritonX100/戊醇/水反胶束中不能体现催化活力的主要原因。     

白地霉脂肪酶的双水相萃取和反胶团提取

对影响双水相萃取和反胶团提取脂肪酶的各种因素进行了探讨,并通过正交实验进一步优化提取条件,PEG浓度15%,(NH4)2SO4浓度22.5%,pH8.0的条件下进行双水相萃取,脂肪酶纯化倍数达到7.5倍;CTAB浓度150mmol/L,相体积比4/2,水相pH8.0,温度40℃的条件下进行反胶团提取,脂肪酶的比活力达到最大,但其比活力稍有下降,约为原来的0.9倍。     

苦参碱的反胶束萃取研究

本文探索AOT-异辛烷反胶束萃取苦参碱的最佳工艺和条件,以AOT-异辛烷反胶束对粗苦参碱中的苦参碱进行萃取,利用毛细管电泳对苦参碱进行定量分析,通过正交试验优化萃取工艺和条件,确定影响萃取率的主要因素为萃取水相的酸度,次要因素为水相的温度,反胶束的W0和离子强度对萃取率的影响较小,得出最优萃取条件为:pH=12,W0=30,T=35℃。     

The phenomenon of super activity in dihydrofolate reductase entrapped inside reverse micelles in apolar solvents

Bovine liver dihydrofolate reductase has been solubilized in reverse micelles of cationic surfactant cetyltrimethylammonium bromide (CTAB) in isooctane-chloroform (1:1,V/V) mixture. Variation of waterpool (WO), pH and surfactant concentration showed that the enzyme activity was regulated by these parameters and was higher than the activity found in aqueous buffer (defined as superactivity); the maximum being at WO 13.3, pH 7.0 and CTAB concentration 75 mM. The Michaelis constants, Km for the substrate FAH2 and NADPH were found to be greater than those determined in water. Since reverse micelles have some features similar to those of biomembranes, display of super activity by dihydrofolate reductase indicates that enzymes in vivo may possess higher activity than actually observed in vitro studies in aqueous solutions.     

Liquid-liquid extraction of commercial glucose oxidase by reversed micelles

Aim of this work was to establish the optimum operating conditions for the extraction and recovery by cationic reversed micelles of commercial glucose oxidase (GOX) from Aspergillus niger, in view of possible application to raw cell homogenates. The influence of pH, temperature, electric conductivity and solvent/co-solvents ratio on the extraction was investigated by a fractional factorial design of 2(3-1) type, conjugated with a mixture experimental design, using the residual enzyme activity to evaluate the results. The best conditions for GOX extraction were ensured using isooctane as solvent and hexanol and butanol as co-solvents at 76/6/18 volume ratio, pH 6.0, 0.2 M cetyl trimethylammonium bromide (CTAB) as cationic surfactant, and electrical conductivity (kappa) of 4.8 mS cm-1. The highest yield of GOX activity recovery (about 90%) was in fair accordance with the value predicted by the model.     

Effect of chaotropes in reverse micellar extraction of kallikrein

Reverse micellar extraction is a promising technique in large-scale bioseparation. However, low recovery and high salt concentration in back extraction limit its application. In CTAB/n-octane/n-hexanol reverse micellar system, the enzyme, pancreatic kallikrein could be effectively enwrapped into reverse micelles in forward extraction, but was difficult to be released during back extraction. In this study, dilute chaotropes (urea and GuHCl) were introduced to enhance the release of enzyme instead of high salts in back extraction. Kallikrein enwrapped in reverse micelles was released effectively in the presence of dilute urea and GuHCl during back extraction. Nearly 100% activity recovery of kallikrein from commercial product was obtained by adding 0.60 M urea, and for kallikrein from crude material, the recovery increased greatly by adding 0.80 M urea and 0.08 M GuHCl in the stripping solution. The mechanism of chaotrope for enhancing the release of enzyme from micelles was explored and dynamic light scatter analysis showed that the chaotrope would influence the sizes of micelles during reverse micellar extraction.     

Downstream processing of soy hull peroxidase employing reverse micellar extraction

Phase transfer studies were conducted to evaluate the solubilization of soy hull peroxidase (SHP) in reverse micelles formed in isooctane/butanol/hexanol using the cationic surfactant cetyltrimethylammonium bromide (CTAB). The effect of various parameters such as pH, ionic strength, surfactant concentration of the initial aqueous phase for forward extraction and buffer pH, type and concentration of salt, concentration of isopropyl alcohol and volume ratio for back extraction was studied to improve the efficiency of reverse micellar extraction. The active SHP was recovered after a complete cycle of forward and back extraction. A forward extraction efficiency of 100%, back extraction efficiency of 36%, overall activity recovery of 90% and purification fold of 4.72 were obtained under optimised conditions. Anionic surfactant sodium bis (2-ethylhexyl) sulfosuccinate (AOT) did not yield good results under the conditions studied. The phase transfer of soy hull peroxidase was found to be controlled by electrostatic and hydrophobic interactions during forward and back extraction respectively.     

反相胶束体系中辣根过氧化物酶的活力和动力学性质

本文系统研究辣根过氧化物酶在ＣＴＡＢ／Ｈ２Ｏ／ＣＨＣ．３－ｉｓｏｏｃｔａｎｅ（１∶１,Ｖ／Ｖ）反相胶束体系中的催化行为。在一定条件下酶反符合Ｍｉｃｈａｅｌｉｓ－Ｍｅｎｔｅｎ动力学。研究水含量、底物浓度、ＰＨ、温度、表面活性剂的浓度等对酶反应的影响,结果表明表面活性剂对酶表现非竞争性抑制作用,高浓度的过氧化氢抑制酶活,最适ＰＨ为７．０。在低水含量（Ｗ０＜５）的胶束体系中保温后,酶的活力发生不可逆的改     

Synthesis of fatty acid esters by a recombinant cutinase in reversed micelles

Fusarium solani pisi recombinant cutinase, solubilized in AOT/isooctane-reversed micelles, was used to catalyze the esterification of fatty acids with aliphatic alcohols. Some relevant parameters for the enzyme activity such as pH, W(o) (water/surfactant molar ratio), temperature, and substrate concentration were optimized. Maximal specific activity was obtained for hexanol. The cutinase showed selectivity for short-chain fatty acids. The stability of the microencapsulated cutinase was investigated at various concentrations of water and different values of pH. Oleic acid had a negative effect on the cutinase stability, while hexanol proved to be a strong stabilizer increasing the half-life of the enzyme about 45 times. (c) 1993 John Wiley & Sons, Inc.     

Optimized extraction by cetyl trimethyl ammonium bromide reversed micelles of xylose reductase and xylitol dehydrogenase from Candida guilliermondii homogenate

The intracellular enzymes xylose reductase (XR, EC 1.1.1.21) and xylitol dehydrogenase (XD, EC 1.1.1.9) from Candida guilliermondii, grown in sugar cane bagasse hydrolysate, were separated by reversed micelles of cetyl trimethyl ammonium bromide (CTAB) cationic surfactant. An experimental design was employed to optimize the extraction conditions of both enzymes. Under these conditions (temperature = 5 degree C, hexanol: isooctane proportion = 5% (v/v), 22 %, surfactant concentration = 0.15M, pH = 7.0 and electrical conductivity = 14 mScm(-1)) recovery values of about 100 and 80% were achieved for the enzymes XR and XD, respectively. The purity of XR and XD increased 5.6- and 1.8-fold, respectively. The extraction process caused some structural modifications in the enzymes molecules, as evidenced by the alteration of K(M) values determined before and after extraction, either in regard to the substrate (up 35% for XR and down 48% for XD) or cofactor (down 29% for XR and up 11% for XD). However, the average variation of V(max) values for both enzymes was not higher than 7%, indicating that the modified affinity of enzymes for their respective substrates and cofactors, as consequence of structural modifications suffered by them during the extraction, are compensated in some extension. This study demonstrated that liquid-liquid extraction by CTAB reversed micelles is an efficient process to separate the enzymes XR and XD present in the cell extract, and simultaneously increase the enzymatic activity and the purity of both enzymes produced by C. guilliermondii.     

Reverse micellar extraction of papain with cationic detergent based system: An optimization approach

In this study, reverse micellar extraction of papain model system was performed using cetyltrimethylammonium bromide (CTAB)/iso-octane/hexanol/butanol system to optimize the forward and back extraction efficiency (BEE). A maximum forward extraction efficiency of 55.0, 61.0, and 54% was achieved with an aqueous phase pH of 11.0, 150?mM CTAB/iso-octane and 0.1?M NaCl, respectively. Taguchi’s orthogonal array was applied to optimize the pH of stripping phase, concentration of isopropyl alcohol (IPA) and potassium chloride (KCl) for maximizing BEE. The optimal levels of stripping phase pH, concentration of IPA and KCl were found to be 6, 20% (v/v), and 0.8?M, respectively. Under these optimal levels, the BEE was found to be 88% after which enzyme activity was recovered with 2.5-fold purification. Further optimization was performed using artificial neural network-linked genetic algorithm, where the BEE was improved to 90.52% with pH 6, IPA (%)?=?19.938, and KCl (M)?=?0.729.     

Effect of hexanol as a cosolvent on partitioning and mass transfer rate of protein extraction using reversed micelles of CB-modified lecithin

Using the affinity-based reversed micelles composed of Cibacron Blue F3G-A (CB) modified soybean lecithin, the effect of hexanol as a cosolvent on the extraction of lysozyme and bovine serum albumin (BSA) was investigated. The water concentration in the reversed micelles increased significantly with increasing hexanol concentration. The partition coefficient of lysozyme could be increased by over 12-fold by introducing hexanol of higher than 0.5 vol%. However, the transfer of BSA was hardly affected because its high molecular weight resulted in a strong steric hindrance effect. The enzymatic activity of lysozyme was nearly 100% retained after undergoing the extraction process with the CB–lecithin micelles containing 3 vol% hexanol. The partitioning isotherms of lysozyme in the CB–lecithin micelles with and without hexanol addition were expressed by the Langmuir equation. The partitioning capacity of lysozyme was nearly increased twofold by introducing 3 vol% hexanol to the CB–lecithin micelles and reached 2.12 g/l. The cosolvent hexanol revealed insignificant effect on the mass transfer rate, and in both the systems with and without hexanol, the mass transfer rate in back extraction was 5–10 times slower than that in the forward extraction. This phenomenon was similar to that in conventionally employed ionic surfactant systems. The result suggests that in the present affinity-based reversed micelles, the interfacial resistance also played a more important role in back extraction than in forward extraction.     

Reverse micelles as a versatile medium for the study of lactate dehydrogenase in vitro

Rabbit muscle lactate dehydrogenase has been solubilized in cationic reverse micelles of cetyltrimethyl ammonium bromide (CTAB) and isooctane-chloroform (1:1, V/V). The activity of the enzyme was notably affected by the change in water pool, pH, and concentration of the surfactant. Lactate dehydrogenase showed its full activity in this reverse micellar system in non-aqueous solvent under specific conditions at a Wo value of 30.55, pH 7.0, and 100 mM CTAB in comparison to the activity measured in aqueous system under optimum conditions. These results indicate that even the large and complex enzymes (M.W. hundred thousand and four subunits) can be solubilized in apolar solvents where they may retain their conformational integrity and oligomericity, i.e., optimum subunit-subunit interaction with maintenance of full activity.