Influence of Igepal reverse micellar and micellar systems on activity and stability of heme peroxidases

The activities of horseradish peroxidase (HRP) and lactoperoxidase (LPO) entrapped in reverse micelles of Igepal CO-520 in cyclohexane were studied. When the molar ratio of water to surfactant, w ₀ was ≥13, the activity of HRP encapsulated in the water pool of the reverse micelle was comparable with that measured in buffer. For LPO, however, lower activity was observed after its incorporation into the same system.

The activity of the investigated peroxidases was also measured in an aqueous solution of Igepal CO-720 or after incubation with this surfactant. The enzymes became inactivated in an aqueous micellar solution of Igepal CO-720, although this process was reversible.

The stability of HRP and LPO at 37 or 50°C was lower in the micellar systems than in buffer with the exception for HRP in reverse micelles at 50°C.     

Influence of Igepal reverse micellar and micellar systems on activity and stability of heme peroxidases

The activities of horseradish peroxidase (HRP) and lactoperoxidase (LPO) entrapped in reverse micelles of Igepal CO-520 in cyclohexane were studied. When the molar ratio of water to surfactant, w₀ was ≥13, the activity of HRP encapsulated in the water pool of the reverse micelle was comparable with that measured in buffer. For LPO, however, lower activity was observed after its incorporation into the same system.

The activity of the investigated peroxidases was also measured in an aqueous solution of Igepal CO-720 or after incubation with this surfactant. The enzymes became inactivated in an aqueous micellar solution of Igepal CO-720, although this process was reversible.

The stability of HRP and LPO at 37 or 50°C was lower in the micellar systems than in buffer with the exception for HRP in reverse micelles at 50°C.     

反胶束萃取酶蛋白的研究进展

反胶束萃取是一项新的分离技术,不仅具有高选择性,而且不易使酶蛋白失活,在提取纯化生物活性物质方面具有巨大的工业应用潜力。本文综述了近年来该方面研究的新进展。     

Protein extration from an aqueous phase into a reversed micellar phase: Effect of water content and reversed micellar composition

In the system composed of the cationic surfactant TOMAC (10 mM), the nonionic (co)surfactant Rewopal HV5 (2 mM), and octanol (0.1% v/v) in isooctane, reversed micelles are formed upon contact with an aqueous phase containing 50 mM ethylene diamine. alpha-Amylase can be transferred from the aqueous phase into reversed micelles in the pH range 9.5 to 10.5 and re-extracted into a second aqueous phase of different composition. The size of the reversed micelles (as reflected in the water content of the organic phase) can be varied by changes in percentage of octanol, type of counterion in the aqueous phase, or in the number of ethoxylate head groups of the nonionic surfactant. An increase in size results in transfer at lower pH values. Experiments in which the charge density in the reversed micellar interface was changed by incorporation of charged derivatives of the nonionic surfactant, without influencing the water content, revealed that an increased charge density facilitated transfer, resulting in a broader transfer profile. Replacement of TOMAC by other quaternary ammonium surfactants differing in number and length of tails revealed that, of the 14 surfactants tested, only 2 gave appreciable amounts of transfer. The amount of transfer is related to the dynamics of phase separation of the surfactants: those giving a poor phase separation inactivate the enzyme. This inactivation is caused by electrostatic interactions between the charged surfactant head groups and charged groups on the enzyme. Electrostatic interactions are the first step of transfer, and can result in either incorporation in a reversed micelle, or, if reversed micelle formation is slow, in enzyme inactivation. (c) 1995 John Wiley & Sons, Inc.     

Dipeptide synthesis and separation in a reversed micellar membrane reactor

The synthesis of dipeptide AcPheLeuNH₂ catalyzed by α-chymotrypsin encapsulated in TTAB/octanol/heptane reversed micelles was investigated in a tubular ceramic membrane reactor, operated in a batch mode. The reaction medium conditions (TTAB concentration, buffer molarity, and pH) were optimized using a factorial design in order to achieve maximum synthesis rates. Hydrated reversed micelles permeated through the membrane together with the substrate ester, dipeptide, and by-products. However, as a result of the low solubility of the peptide in the reaction medium, selective precipitation occurred, thus enabling the complete retention of the solid product by the ultrafiltration membrane and therefore an integration of a separation step in the biotransformation process. In spite of the continuous accumulation of solids inside the reactor, constant permeation flow rates could be maintained throughout the operation. The influence of α-chymotrypsin, TTAB, and water concentration on the kinetics and mass transfer of the system was also investigated. The behavior of the system during a continuous experiment was also evaluated.     

Affinity-based reversed micellar protein extraction: I. principles and protein-ligand systems

Affinity cosurfactants, consisting of hydrophilic ligands derivatized with hydrophobic tails, increase the efficiency of selective protein recoveries using reversed micelles by extending the operating range of pH and salt concentration over which an extraction can be performed. Three different affinity cosurfactant-protein pairs have been used to demonstrate the principles of this extractive technique: (i) concanavalin A, a lectin, was extracted with the addition of octyl glucoside; (ii) natural amphiphiles, such as lecithin, were used to extract myelin basic protein, a membrane-associated protein known to recognize and bind the phosphatidylcholine headgroup; and (iii) alkyl boronic acids were used to extract chymotrypsin. The enhancement in protein transfer correlated with the binding strength of the free ligand and protein in aqueous solution. Several control studies confirmed the biospecificity of the interactions of protein and affinity cosurfactant. (c) 1993 John Wiley & Sons, Inc.     

Purification of industrial alphaamylase by reversed micellar extraction

The purification of industrial alpha-amylase by liquid-liquid extraction with Aliquat 336 reversed micellar solution as the extractant was studied. Seven kinds of Aliquat 336 reversed micellar solution, formed by using seven kinds of straight chain alkyl alcohols as cosolvent, have been utilized to extract industrial a-amylase. It was found that these seven kinds of reversed micellar solution can all achieve a high protein transfer efficiency in the forward extraction process. After a full forward and backward extraction cycle, however, only the reversed micelles with n-butanol as the cosolvent was found to be able to maintain the activity of alpha-amylase in the stripping solution. By using the reversed micelles of Aliquat 336/isooctane/1% (v/v) n-butanol to perform a full extraction cycle, it was found that 85% of the total activity of alpha-amylase in the industrial a-amylase could be recovered at the end of an extraction cycle and the specific activity of alpha-amylase could be concentrated about 1.5-fold; meanwhile, most of the neutral protease in the industrial a-amylase could be removed. The separation factor of alpha-amylase to neutral protease at the end of an extraction cycle can reach about 10. (c) 1995 John Wiley & Sons, Inc.     

Affinity-based reversed micellar protein extraction: II. effect of cosurfactant tail length

The selectivity of protein extraction by reversed micellar solutions can be improved by the addition of affinity cosurfactants bearing ligands which bind strongly to the target protein. The interactions between cosurfactant and protein, as well as the interfacial activity of both the free cosurfactant and the protein-cosurfactant complex, were accounted for in a model of the affinity-partitioning process. The aqueous phase dissociation constant was used to describe the protein-ligand interactions. The interfacial partition coefficient for several cosurfactant families varied with tail length according to the well-established hydrophobic effect. Control studies with alkylated chymotrypsin showed that when longer hydrophobic tails are irreversibly attached to the protein, the protein partitions more strongly to the reversed micellar phase. In contrast, for reversible protein-cosurfactant binding, the model predicts a maximum in protein uptake when the cosurfactant tail length is varied; the decrease at longer tail lengths is due to the lowered aqueous phase concentration of affinity cosurfactant, resulting in the formation of fewer protein-cosurfactant complexes. This behavior was confirmed experimentally. (c) 1993 John Wiley & Sons, Inc.     

An ultrafiltration membrane bioreactor for the lipolysis of olive oil in reversed micellar media

The enzymatic hydrolysis of olive oil using Chromobacterium viscosum lipase B encapsulated in reversed micelles of dioctyl sodium sulfosuccinate (AOT) in isooctane was investigated in an ultrafiltration ceramic membrane reactor of tubular type, operating in a batch mode. Water concentration was found to be a critical parameter in the enzyme kinetics and hydrolysis yield of the reaction. The size of micelles, recirculation rate, and substrate concentration were found to be the major factors affecting the separation process. A correlation that enables the prediction of final conversion degrees in this bioreactor from the initial reaction conditions was established. (c) 1993 Wiley & Sons, Inc.     

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。     

Improving protein extraction yield in reversed micellar systems through surface charge engineering

The mechanism of extraction of rat cytochrome b(5) from water into a sodium dioctylsulfosuccinate (AOT) micellar organic phase was studied using protein engineering of surface charged residues. The extraction behavior of native cytochrome b(5) and modified proteins with substitutions of the type glutamic acid --> lysine at positions 44 (E44K), 56 (E56K), and 92 (E92K), was studied as a function of pH. The results indicate that an important mechanism of extraction is an electrostatic interaction of this protein with the negatively charged surfactant. We demonstrate that it is possible to improve extraction by engineering the protein surface charge, increasing the driving force responsible for the protein transfer to the micellar phase. (c) 1994 John Wiley & Sons, Inc.     

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.     

Structural Change and Catalytic Activity of Horseradish Peroxidase in Oxidative Polymerization of Phenol

The effects of solvent and reaction conditions on the catalytic activity of horseradish peroxidase (HRP) were investigated for oxidative polymerization of phenol in water/organic mixtures using hydrogen peroxide as an oxidant. Also, the structural changes of HRP were investigated by CD and absorption spectroscopy in these solvents. The results suggest that the yield of phenol polymer (the conversion of phenol to polymer) is strongly affected by the reaction conditions due to the structural changes of HRP, that is, the changes in higher structure of the apo-protein and dissociation or decomposition of the prosthetic heme. Optimum solvent compositions for phenol polymerization depend on the nature of the organic solvents owing to different effects of the solvents on HRP structure. In addition to initial rapid changes, slower changes of HRP structure occur in water/organic solvents especially at high concentrations of organic solvents. In parallel with these structural changes, catalytic activity of HRP decreases with time in these solvents. At higher reaction temperatures, the yield of the polymer decreases, which is also ascribed to modification of HRP structure. It is known that hydrogen peroxide is an inhibitor of HRP, and the yield of phenol polymer is strongly dependent on the manner of addition of hydrogen peroxide to the reaction solutions. The polymer yield decreases significantly when hydrogen peroxide was added to the reaction solution in a large amount at once. This is probably due to inactivation of HRP by excess hydrogen peroxide. From the CD and absorption spectra, it is suggested that excess hydrogen peroxide causes not only decomposition of the prosthetic heme but also modification of the higher structure of HRP.     

Effect of polymers on enhanced chemiluminescent assays for peroxidase and peroxidase labels

Hydroxypropyl methylcellulose, hydroxyethyl cellulose, and hydroxybutyl methylcellulose stabilized light emission in a boronic acid-enhanced chemiluminescent assay for horseradish peroxidase. The stabilization of light emission was concentration-dependent and more effective with substituted boronic acid enhancers (e.g. 4-iodophenylboronic acid) than with substituted phenol enhancers (e.g. 4-iodophenol). Hydroxybutyl methylcellulose improved the linearity of the dose–response curve in a peroxidase-based antioxidant assay and stabilized light emission post-consumption of the antioxidant (Trolox). This polymer had no effect on the signal from a peroxidase label immobilized on a membrane (dot blot) or on the inside surface of a microwell in an enzyme immunoassay for thyrotropin.     

脂肪酶在反相胶囊中的催化行为的研究

系统研究了脂肪酶在ＡＯＴ／水／异辛烷反应相胶囊中的催化行为。在一定条件下,反相胶囊中的酶反应的仍符合Ｍｉｃｈａｅｌｉｓ－Ｍｅｎｔｅｎ动力学原理,研究了含水量,底物浓度,ｐＨ,温度,溶剂的种类和表面活性剂浓度等对酶反应的影响。结果表明,酶活力与Ｒ值（水与表面活性剂的摩尔比值）有关。获得最大酶活力的条件是Ｒ＝１１,ｐＨ７．０,温度３２．５℃,橄榄油浓度为４０％。     

Effects of microwaves (900 MHz) on peroxidase systems: A comparison between lactoperoxidase and horseradish peroxidase

ABSTRACT

This work shows the effects of exposure to an electromagnetic field at 900?MHz on the catalytic activity of the enzymes lactoperoxidase (LPO) and horseradish peroxidase (HRP). Experimental evidence that irradiation causes conformational changes of the active sites and influences the formation and stability of the intermediate free radicals is documented by measurements of enzyme kinetics, circular dichroism spectroscopy (CD) and cyclic voltammetry.     

Partitioning behavior and enrichment of proteins with reversed micellar extraction: I. forward extraction of proteins from aqueous to reversed micellar phase

Protein extractions using aerosol OT (AOT)-isooctane reverse micelle solutions have been studied to explore the potential for separating and enriching proteins with the reversed micellar extraction. The effects of pH, ionic strength, and different cations of chlorides in a bulk aqueous phase and of AOT concentration in an organic phase on the partitioning of lysozyme and myoglobin and the solubilization of water are presented in detail. The extraction of lysozyme was affected by the concentration of potassium or barium but was almost independent of that of sodium or calcium, whose ionic diameter is smaller than that of potassium and barium. For the extraction of myoglobin, however, the effect of barium concentration was not appreciable. Lysozyme could be enriched into the reversed micellar phase up to 30 times the aqueous feed concentration. (c) 1993 John Wiley & Sons, Inc.     

Enhancement effect of water activity on enzymatic synthesis of cephalexin

The effect of water activity (a(w)) of the reaction medium on the enzymatic synthesis of cephalexin (CEX) from 7-amino-3-deacetoxycephalosporanic acid (7-ADCA) and D-alpha-phenylglycine methyl ester (PGM) was investigated using the alpha-amino acid ester hydrolase enzyme from Xanthomonas citri. It was found that the synthetic activity of the enzyme and the conversion yield were markedly improved when the a(w) of the reaction medium was lowered to about 0.97. The water activity depressing agents evaluated were glycerol, sucrose, and sorbitol, and the conversion yields were improved up to 170% with 15% glycerol, 230% with 30% sucrose, and 270% with 20% sorbitol, respectively. The extent of favorable effect of a(w) on the conversion yield was not the same among the a(w) depressors, probably due to other unknown interactions between the enzyme and depressors. However, optimal a(w) values corresponding to the maximum conversion yield coincided for all a(w) depressors used. The conversion yield of CEX showed an increasing trend with increasing a(w) up to the optimal a(w) value (0.96-0.97) which corresponds to the maximum conversion yield and a decreasing trend beyond the optimal a(w). There appears to be a delicate balance between the hydrolytic reaction of PGM and synthetic reaction of CEX. The increasing a(w)-[E . PGM] complex and the branched reaction pathway fluxes from [E . PGM] to PG (D-alpha-phenyl glycine) and CEX are balanced in such a way that the maximum CEX conversion yield is obtained at a(w) value of 0.96-0.97. The a(w) depressors stabilized the enzyme somewhat, but this positive effect was considered to be only a minor contribution to the substantial yield enhancement. The a(w) depressor effect on viscosity and in turn the mass transfer rate limitation was ruled out since the change in conversion due to the viscosity change was found to be insignificant. (c) 1993 John Wiley & Sons, Inc.