Thermobarostability of alpha-chymotrypsin in reversed micelles of aerosol OT in octane solvated by water-glycerol mixtures

Thermostability of alpha-chymotrypsin at normal pressure in reversed micelles depends on both an effective surfactant solvation degree and glycerol content in the system. The difference in alpha-chymotrypsin stability in reversed micelles at various glycerol concentrations [up to 60% (v/v)] was more pronounced at high surfactant degrees of solvation, R >/= 16. After a 1-h incubation at 40 degrees C in "aqueous" reversed micelles (in the absence of glycerol), alpha-chymotrypsin retained only 1% of initial catalytic activity and 10, 22, 59, and 48% residual activity in glycerol-solvated micelles with 20, 30, 50, and 60% (v/v) glycerol, respectively. The explanation of the observed effects is given in the frames of micellar matrix structural order increasing in the presence of glycerol as a water-miscible cosolvent that leads to the decreasing mobility of the alpha-chymotrypsin molecule and, thus the increase of its stability. It was found that glycerol or hydrostatic pressure could be used to stabilize alpha-chymotrypsin in reversed micelles; a lower pressure is necessary to reach a given level of enzyme stability in the presence of glycerol.     

Reversed micellar extraction of trypsin: Effect of solvent on the protein transfer and activity recovery

By using trypsin as the model protein and AOT as the model surfactant, the effect of a variety of solvents on protein transfer and activity recovery during the liquid-liquid reversed micellar extraction was investigated. It was found that several solvents, including isooctane, octane, heptane, and kerosene, had a similar effect on the recovery of trypsin activity after a full cycle of forward and backward extraction, and could all be used as the solvents for AOT-reversed micelles in trypsin extraction. Two other solvents (hexane and cyclohexane), however, were not so efficient. (c) 1995 John Wiley & Sons, Inc.     

Protein refolding by reversed micelles utilizing solid-liquid extraction technique

This article reports that a reversed micellar solution is useful for refolding proteins directly from a solid source. The solubilization of denatured RNase A, which had been prepared by reprecipitation from the denaturant protein solution, into reversed micelles formulated with sodium di-2-ethylhexyl sulfosuccinate (AOT) has been investigated by a solid-liquid extraction system. This method is an alternative to the ordinary protein extraction in reversed micelles based on the liquid-liquid extraction. The solid-liquid extraction method was found to facilitate the solubilization of denatured proteins more efficiently in the reversed micellar media than the ordinary phase transfer method of liquid extraction. The refolding of denatured RNase A entrapped in reversed micelles was attained by adding a redox reagent (reduced and oxidized glutathion). Enzymatic activity of RNase A was gradually recovered with time in the reversed micelles. The denatured RNase A was completely refolded within 30 h. In addition, the efficiency of protein refolding was enhanced when reversed micelles were applied to denatured RNase A containing a higher protein concentration that, in the case of aqueous media, would lead to protein aggregation. The solid-liquid extraction technique using reversed micelles affords better scale-up advantages in the direct refolding process of insoluble protein aggregates.     

Important parameters affecting efficiency of protein refolding by reversed micelles

Refolding of denatured RNase A as a model of inclusion bodies was performed by reversed micelles formulated with sodium di-2-ethylhexyl sulfosuccinate (AOT) in isooctane. In the novel refolding process, a solid-liquid extraction was utilized as an alternative to the ordinary protein extraction by reversed micelles based on a liquid-liquid extraction. First, the effects of operational parameters such as concentration of AOT, W(o) (= [H(2)O]/[AOT]), and pH were examined on the solubilization of solid denatured proteins into a reversed micellar solution. The solubilization was facilitated by a high AOT concentration, a high W(o) value, and a high pH in water pools. These conditions are favorable for the dispersion of the solid protein aggregates in an organic solvent. Second, the renaturation of the denatured RNase A solubilized into the reversed micellar solution was conducted by addition of glutathione as a redox reagent. A complete renaturation of RNase A was accomplished by adjusting the composition of the redox reagent even at a high protein concentration in which protein aggregation would usually occur in aqueous media. In addition, the renaturation rates were improved by optimizing water content (W(o)) and the pH of water pools in reversed micelles. Finally, the recovery of renatured RNase A from the reversed micellar solution was performed by adding a polar organic solvent such as acetone into the reversed micellar solution. This precipitation method was effective for recovering proteins from reversed micellar media without any significant reduction in enzymatic activity.     

Affinity extraction of proteins with a reversed micellar system composed of Cibacron Blue-modified lecithin

Crude soybean lecithin was used as a novel surfactant to form reversed micelles in n-hexane. Cibacron Blue F-3GA (CB) was directly immobilized to the reversed micelles by a two-phase reaction. The reversed micellar system without CB showed low solubilizing capacity for low molecular weight proteins, lysozyme, and cytochrome c due to the weak electrostatic interactions. The introduction of CB significantly increased the solubilization of lysozyme because of its affinity binding to CB but showed no effect on the solubilization of cytochrome c since it did not bind to CB. Although bovine serum albumin had an affinity for CB, it was not extracted to the reversed micelles containing CB because its high molecular weight resulted in a significant steric hindrance effect. Thus the reversed micellar system had a high selectivity resulting from both biospecific and steric hindrance effects. The extraction yield of lysozyme decreased significantly with increasing ionic strength. Therefore, the back extraction of lysozyme was carried out using a stripping solution with an ionic strength of 0.865 mol/L. The overall recovery yield of lysozyme after back extraction could be increased to 87% by stripping for 2 h. The recovered lysozyme exhibited an activity equivalent to native lysozyme, and its secondary structure was also unchanged.     

The Effect of a Quaternary Amine (Aliquat 336) on Growth and Photosynthesis of the Green Alga Chlorella emersonii, and the Effect on Photosynthesis in Isolated Spinach Chloroplasts

A quaternary amine, Aliquat 336, inhibits the growth of the green alga Chlorella emersonii, ¹⁴C-fixation of the alga is also inhibited. The effect and the site of action of the compound was studied by using isolated spinach chloroplasts. The carbon dioxide dependent oxygen evolution of the chloroplasts is inhibited directly upon the addition of the amine and the oxygen evolution is replaced by an oxygen uptake. By investigating some electron transport reactions in the chloroplasts we were able to show that Aliquat 336 affects the electron transport on the level of photophosphorylation. The results from the in vivo and the in vitro experiments thus show that the quaternary amine affects the photosynthetic process. Aliquat 336 is a solvent extractant used in several industrial processes for extraction of metals from aqueous solutions. Aliquat 336 could be considered a presumptive water pollutant as the compound could enter a recipient water body and thus affect photosynthesis.     

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.     

Protein refolding in reversed micelles

A novel process has been developed which uses reversed micelles to isolate denatured protein molecules from each other and allows them to refold individually. These reversed micelles are aqueous phase droplets stabilized by the surfactant AOT and suspended in isooctane. By adjusting conditions such that only one protein molecule is present per reversed micelle, it was possible to achieve independent folding without encountering the problem of aggregation due to interactions with neighboring molecules. The feasibility of this process was demonstrated using bovine pancreatic ribonuclease A as a model system. It was shown that denatured and reduced ribonuclease can be transferred from a buffered solution containing guanidine hydrochloride into reversed micelles to a greater extent than native enzyme under the same conditions. The denaturant concentration can then be significantly reduced in the reversed micellar phase, while retaining most of the protein, by means of extractive contacting stages with a denaturant-free aqueous solution. Denatured and reduced ribonuclease will subsequently recover full activity inside reversed micelles within 24 h upon addition of a mixture of reduced and oxidized glutathione to reoxidize disulfide bonds. Extraction of this refolded enzyme from reversed micelles back into aqueous solution can be accomplished by contacting the reversed micelle phase with a high ionic strength (1.0M KCl) aqueous solution containing ethyl acetate.     

反胶束萃取血红蛋白的研究

研究了ＣＴＡＢ－正辛醇－正庚烷交束溶液萃取牛血红蛋白（ｐＨｂ）时、ｐＨ值、表面活性剂浓度、助表面活性剂浓度、离子种类和离子强度、溶剂比以及蛋白质浓度等因素对萃取效果的影响,并以蛋白质分子与表面活性剂分子间的相互作用以及反胶束大空间阻碍作用上进行了解释。研究表明,水相ＰＨ值在１０．５￣１２．５之间,ＫＣ１浓度为０．１ｍｏｌ／ｌ,反胶束溶液中表面活性剂浓度为０．０２ｍｏｌ／ｌ,正辛醇与正庚烷之比为０．     

Activity and stability of catalase in nonionic micellar and reverse micellar systems

Catalase activity and stability in the presence of simple micelles of Brij 35 and entrapped in reverse micelles of Brij 30 have been studied. The enzyme retains full activity in aqueous micellar solution of Brij 35. Catalase exhibits "superactivity" in reverse micelles composed of 0.1 M Brij 30 in dodecane, n-heptane or isooctane, and significantly lowers the activity in decaline. The incorporation of catalase into Brij 30 reverse micelles enhances its stability at 50 degrees C. However, the stability of catalase incubated at 37 degrees C in micellar and reverse micellar solutions is lower than that in homogeneous aqueous solution.     

Characterization of lipase in reversed micelles formulated with cibacron blue F-3GA modified span 85

Sorbitan trioleate (Span 85) modified by Cibacron Blue F-3GA (CB) was prepared and used as an affinity surfactant to formulate a reversed micellar system for Candida rugosa lipase (CRL) solubilization. The system was characterized and evaluated by employing CRL-catalyzed hydrolysis of olive oil as a model reaction. The micellar hydrodynamic radius results reflected, to some extent, the redistribution of surfactant and water after enzyme addition, and the correlation between surfactant formulation, water content (W0), micellar size, and enzyme activity. An adequate modification density of CB was found to be important for the reversed micelles to retain enough hydration capacity and achieve high enzyme activity. Compared with the results in AOT-based reversed micelles, CRL in this micellar system exhibited a different activity behavior versus W0. The optimal pH and temperature of the encapsulated lipase remained unchanged, but the apparent activity was significantly higher than that of the native enzyme in bulk solution. Kinetic studies indicated that the encapsulated lipase in the reversed micelles of CB-formulated Span 85 followed the Michaelis-Menten equation. The Michaelis constant was found to decrease with increasing surfactant concentration, suggesting an increase of the enzyme affinity for the substrate. Stability of the lipase in the reversed micelles was negatively correlated to W0.     

Protein refolding in reversed micelles: Interactions of the protein with micelle components

A novel process has been developed to improve the refolding yield of denatured proteins. It uses reversed micelles to isolate denatured protein molecules from each other and thus, upon refolding, reduces the intermolecular interactions which lead to aggregation. The feasibility of this process was first demonstrated with Ribonuclease A as a model protein. In the present work, we expanded the scope of this study to better understand both the general mechanisms of protein refolding in reversed micelles and the biotechnological applicability of the process. First, we investigated the interactions between the individual components of the reversed micellar system (the protein molecule, the denaturant guanidine hydrochloride (GuHCl), and the surfactant (AOT)) during the refolding process. We then extended our studies to a more hydrophobic protein, gamma-interferon, which aggregates upon refolding in aqueous solution. However, it was also found to aggregate in our reversed micelle process during the extraction step. Since gamma-interferon is a much more hydrophobic protein than RNase, we hypothesize that interactions between hydrophobic amino acids and the surfactant layer may interfere with refolding. This hypothesis was tested by studying the refolding of chemically modified RNase. The substitution of 55% of the surface lysine residues with hydrophobic caproyl groups caused a significant decrease in the refolding yield of RNase in the reversed micellar system without affecting aqueous solution renaturation. In addition, the extraction efficiency of the enzyme from reversed micelles back into aqueous solution was severely reduced and resulted in aggregation. These experiments indicate that unfolded hydrophobic Proteinsinteract with the Surfactant molecules, which limits their ability to refold in reversed micelles.     

Studies on the extraction and back-extraction of a recombinant cutinase in a reversed micellar extraction process

This work deals with the extraction and back-extraction of a recombinant cutinase using AOT reversed micelles in isooctane. The effect of pH, ionic strength, AOT concentration and temperature on the extraction and back-extraction of the cutinase was investigated. High extraction (97%) of the cutinase was achieved at pH 7.0 with a 50 mM Tris-HCl buffer solution containing 100 mM KCl, but a low activity was detected in the reversed micellar phase. At pH 9.0, cutinase was extracted (75%) to the reversed micelles with higher activity. Cutinase was recovered (50%) from a reversed micellar phase (100 mM AOT/isooctane) into a 50 mM Tris-HCl buffered solution at pH 9.0 with 100 mM KCl, and 20°C. Protein and cutinase activity global yields of 38 and 45%, respectively, were obtained for the global process, extraction and back-extraction steps, using low ionic strength, pH 9.0, 100 mM AOT and 20°C.Maria das Graças Carneiro da Cunha acknowledges a Ph.D. fellowship from Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq) and Centro de Pesquisas Aggeu Magalhães, Brasil. This work was partly financed by the BRIDGE Programme (Contract BIOT-CT91-0274(DTEE)).     

Spectroscopic properties of horse liver alcohol dehydrogenase in reversed micellar solutions

Catalytic and spectroscopic properties of alcohol dehydrogenase from horse liver, incorporated in reversed micellar media, have been studied. Two different reversed micellar systems have been used, one containing an anionic [sodium bis(2-ethylhexyl)sulfosuccinate, AOT], the other containing a cationic (cetyltrimethylammonium bromide, CTAB) surfactant. With 1-hexanol as substrate the turnover number of the enzyme in AOT-reversed micelles is strongly dependent on the water content of the system. At low wo ([H2O]/[surfactant]) (wo less than 20) no enzymatic activity can be detected whereas at high wo (wo = 40) the turnover is only slightly lower than in aqueous solution. In CTAB-reversed micelles the dependence of the turnover number on wo is much less. The enzymatic activity is in this case significantly lower than in aqueous solution and increases only slightly with an increasing water content of the reversed micelles. Possible interactions of the protein with the surfactant interfaces in the reversed micellar media were studied via circular dichroism and fluorescence measurements. From the circular dichroism of the protein backbone it is observed that the protein secondary structure is not significantly affected upon incorporation in the reversed micelles since the far-ultraviolet spectrum is not altered. Results from time-resolved fluorescence anisotropy experiments indicate that, especially in AOT-reversed micelles, interactions between the protein and the surfactant interface are largely electrostatic in nature, as evident from the dependence on the pH of the buffer used. In CTAB-reversed micellar solutions such interactions appear to be much less pronounced than in AOT.     

Reversed micelles of polymeric surfactants in nonpolar organic solvents. A new microheterogeneous medium for enzymatic reactions.

A new microheterogeneous non-aqueous medium for enzymatic reactions, based on reversed micelles of a polymeric surfactant, was suggested. The surfactant termed CEPEI, was synthesized by successive alkylation of poly(ethyleneimine) with cetyl bromide and ethyl bromide and was found to be able to solubilize considerable amounts of water in benzene/n-butanol mixtures. The hydrodynamic radius of polymeric-reversed micelles was estimated to be in the range 22-51 nm, depending on the water content of the system, as determined by means of the quasi-elastic laser-light scattering. Polymeric reversed micelles were capable of solubilizing enzymes (alpha-chymotrypsin and laccase) in nonpolar solvents with retention of catalytic activity. Due to the strong buffering properties of CEPEI over a wide pH range, it could maintain any adjusted pH inside hydrated reversed micelles. It was found that catalytic behavior of enzymes entrapped in polymeric reversed micelles was rather insensitive to the pH of the buffer solution introduced into the system as an aqueous component, but determined mostly by acid-base properties of the polymeric surfactant itself. Both catalytic activity and stability of entrapped alpha-chymotrypsin and laccase were found to increase with increasing water content of the system. Under certain conditions, the entrapment of alpha-chymotrypsin into CEPEI reversed micelles resulted in a considerable increase in catalytic activity and stability as compared to aqueous solution. CEPEI reversed micelles were demonstrated to be promising enzyme carriers for use in membrane reactors. Owing to the large dimensions of CEPEI reversed micelles, they are effectively kept back by a semipermeable membrane, thus allowing an easy separation of the reaction product and convenient recovery of the enzyme.     

Purification of lysozyme by affinity-based reversed micellar two-phase extraction

A dye-affinity reversed micellar system was used for lysozyme purification from a crude solution of chicken egg white. The dye-affinity reversed micelles consisted of Cibacron Blue F-3GA (CB; 0.1 mM) modified lecithin (50 g/l) in n-hexane. Starting with a crude egg white solution containing lysozyme of 0.0381 mg/mg protein, lysozyme purity was increased by 16 to 20 times, reached 0.62 to 0.76 mg/mg protein. The affinity micellar system was recycled and used three times. Addition of polyoxyethylene (20) sorbitan trioleate (Tween 85) as a cosurfactant could increase the capacity of the affinity-based reversed micelles. A lysozyme recovery yield of over 70% was obtained at a forward aqueous phase pH of 9.16 using the reversed micelles additionally containing 20 g/l of Tween 85.     

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.     

Mechanism of extraction of chymotrypsin into isooctane at very low concentrations of aerosol OT in the absence of reversed micelles

Chymotrypsin is easily extracted from an aqueous solution into isooctane containing the anionic surfactant aerosol OT (AOT). The concentration of AOT needed to efficiently extract 0.5 mg/mL CMT is as low as 1 mM and as low as 0.2 mM AOT was sufficient to extract the protein into isooctane. The extraction process was unaffected by 10% (v/v) ethyl acetate in the isooctane phase. Moreover, spectroscopic analysis by electron paramagnetic resonance indicated that CMT did not exist inside a discreet water pool of a reversed micelle. Calculations of the number of AOT molecules associated per extracted CMT molecule indicate that only ca. 30 surfactant molecules interact with the protein, a value too low for reversed micellar incorporation of the protein in isooctane. These studies suggested that reversed micelles do not need to be involved in the actual transfer of the protein from the aqueous to the organic phase and protein solubilization in the organic phase is possible in the absence of reversed micelles. Based on these findings, a new mechanism has been proposed herein for protein extraction via the phase transfer method involving ionic surfactants. The central theme of this mechanism is the formation of an electrostatic complex between CMT and AOT at the aqueous/organic interface between AOT and CMT, thereby leading to the formation of a hydrophobic species that partitions into the organic phase. Consistent with this mechanism, the efficiency of extraction is dependent on the interfacial mass transfer, the concentrations of CMT and AOT in the aqueous and organic phases, respectively; the ionic strength of the aqueous phase; and the presence of various cosolvents. (c) 1994 John Wiley & Sons, Inc.     

来源于Pyrococcus furiosus的耐高温α-淀粉酶基因在衣藻叶绿体中的表达

来源于Pyrococcusfuriosus的耐高温α-淀粉酶是一种重要的酒精工业用酶,在植物中表达耐高温α-淀粉酶可以大大降低用植物秸秆生产酒精的成本。选择衣藻叶绿体基因组同源片段clpP-trnL-petB-chlL-rpl23-rpl2和壮观霉素抗性基因,构建了来源于Pyrococcusfuriosus的耐高温α-淀粉酶基因的衣藻叶绿体表达载体p64A。通过基因枪将其导入衣藻叶绿体中,经壮观霉素抗性(100mg/L)筛选,获得了9个抗性衣藻转化子。转化子经过抗性继代筛选后,经PCR、Southernblot检测分析及暗培养,证实耐高温α-淀粉酶基因已整合到衣藻叶绿体基因组中并得到表达。酶活性检测表明,转基因衣藻表达产物具有耐高温α-淀粉酶活性,每克鲜重衣藻最高达77.5u。实验结果证明在植物叶绿体中表达工业酶制剂是可行的。     

The use of pressure to modify enzyme activity in reversed micelles.

Pressurization of enzyme-containing AOT-water-isooctane reversed micelles with low molecular weight gases leads to markedly different responses in activity characteristics. Microbial lipases exhibit a total cutoff in activity with as low a pressure as 2 MPa and a remarkable activity regain with depressurization. The observation also holds for reaction in monophasic organic solvents. The protease, alpha-chymotrypsin, is unaffected by pressurization until a critical pressure wherein micellar instability occurs. The use of pressure as a switch for lipase reaction in nonaqueous media is discussed.