Use of reverse micellar systems for the extraction and purification of bromelain from pineapple wastes

Reverse micellar systems of CTAB/isooctane/hexanol/butanol and AOT/isooctane are used for the extraction and primary purification of bromelain from crude aqueous extract of pineapple wastes (core, peel, crown and extended stem). The effect of forward as well as back extraction process parameters on the extraction efficiency, activity recovery and purification fold is studied in detail for the pineapple core extract. The optimized conditions for the extraction from core resulted in forward and back extraction efficiencies of 45% and 62%, respectively, using reverse micellar system of cationic surfactant CTAB. A fairly good activity recovery (106%) and purification (5.2-fold) of bromelain is obtained under these conditions. Reverse micellar extraction from peel, extended stem and crown using CTAB system resulted in purification folds of 2.1, 3.5, and 1.7, respectively. Extraction from extended stem using anionic surfactant AOT in isooctane did not yield good results under the operating conditions employed.     

Extraction of bovine serum albumin using nanoparticulate reverse micelles

The extraction of a relatively large molecular weight protein, bovine serum albumin (BSA), using nano-sized reverse micelles of nonionic surfactant polyoxyethylene p-t-octylphenol (Triton-X-100) is attempted for the first time. Suitability of reverse micelles of anionic surfactant sodium bis (2-ethyl hexyl) sulfosuccinate (AOT) and Triton-X-100/AOT mixture in organic solvent toluene for BSA extraction is also investigated. Although, the size of the Triton-X-100 reverse micelle in toluene is large enough to host BSA molecule in the hydraulic core, the overall extraction efficiency is found to be low, which may be due to lack of strong driving force. AOT/toluene system resulted in complete forward extraction at aqueous pH 5.5 and a surfactant concentration of 160 mM. The back extraction with aqueous phase (pH 5.5) resulted in 100% extraction of BSA from the organic phase. The addition of Triton-X-100 to AOT reduced the extraction efficiency of AOT reverse micelles, which may be attributed to reduced hydrophobic interaction. The circular dichroism (CD) spectrum of BSA extracted using AOT/toluene reverse micelles indicated the structural stability of the protein extracted.     

Enzymatic hydrolysis of microcrystalline cellulose in reverse micelles

The activities of cellulases from Trichoderma reesei entrapped in three types of reverse micelles have been investigated using microcrystalline cellulose as the substrate. The reverse micellar systems are formed by nonionic surfactant Triton X-100, anionic surfactant Aerosol OT (AOT), and cationic surfactant cetyltrimethyl ammonium bromide (CTAB) in organic solvent media, respectively. The influences of the molar ratio of water to surfactant omega0, one of characteristic parameters of reverse micelles, and other environmental conditions including pH and temperature, on the enzymatic activity have been studied in these reverse micellar systems. The results obtained indicate that these three reverse micelles are more effective than aqueous systems for microcrystalline cellulose hydrolysis, and cellulases show "superactivity" in these reverse micelles compared with that in aqueous systems under the same pH and temperature conditions. The enzymatic activity decreases with the increase of omega0 in both AOT and Triton X-100 reverse micellar systems, but reaches a maximum at omega0 of 16.7 for CTAB reverse micelles. Temperature and pH also influence the cellulose hydrolysis process. The structural changes of cellulases in AOT reverse micelles have been measured by intrinsic fluorescence method and a possible explanation for the activity changes of cellulases has been proposed.     

Reverse micellar extraction and precipitation of lysozyme using sodium di(2-ethylhexyl) sulfosuccinate

Sodium di(2-ethylhexyl) sulfosuccinate, referred to as Aerosol-OT or AOT, was used to remove lysozyme from an aqueous phase via reverse micellar extraction and precipitation method. For both methods, when the surfactant was in excess, a complete removal of lysozyme from the aqueous phase was obtained at the values of pH below the pI of lysozyme. However, for the reverse micellar method, a solubilization limit of lysozyme in the organic phase was observed, and a white precipitate was formed at the aqueous-organic interface. This observation suggested using AOT directly as a precipitating ligand. The lysozyme precipitated with AOT was fully recovered, with its original enzymatic activity, using acetone as a recovery solvent. A mechanism is suggested to explain the solubilization of lysozyme in an AOT reverse micellar system. It is shown that a direct precipitation method can be used with advantage instead of using the reverse micellar extraction method to recover lysozyme from an aqueous phase.     

Estimation of direct-contact fraction for phenanthrene in surfactant solutions by toxicity measurement

The toxicity of solutions containing nonionic surfactants Tween 80, Brij 35 and/or phenanthrene to Pseudomonas putida ATCC 17484 was investigated. The fraction of direct contact between micellar-phase phenanthrene and bacterial cell surface was estimated by using the toxicity data and a mathematical model. The mathematical model was used to calculate phenanthrene concentration in the micellar phase and aqueous pseudophase separately. The first-order death rate constant increased from 0.088+/-0.016 to 0.25+/-0.067 h(-1) when the phenanthrene concentration was increased from 0 to 5.17 x 10(-6)M (equals water solubility). The intrinsic toxicity of surfactant was higher in Brij 35 than in Tween 80. When phenanthrene concentration was increased to 9.7 x 10(-5)M in surfactant solutions, the death rate constant increased to 1.8 +/- 0.024 and 0.41 +/- 0.088 h(-1) for 8.4 x 10(-4)M Brij 35 and 7.6 x 10(-4)M Tween 80. The direct-contact fraction was 0.083 and 0.044 for Brij 35 and Tween 80, respectively, under these conditions using exponential model. The toxicity increased with increasing phenanthrene concentration at a fixed surfactant concentration. The toxicity decreased with increasing the surfactant concentration at a fixed phenanthrene concentration due to decreased contact of bacteria with phenanthrene present in the interior of surfactant micelles.     

Study of the factors affecting the extraction of soybean protein by reverse micelles

In this work, the forward and back extraction of soybean protein by reverse micelles was studied. The reverse micellar systems were formed by anionic surfactant sodium bis(2-ethyl hexyl) sulfosuccinate (AOT), isooctane and KCl solution. The effects of AOT concentration, aqueous pH, KCl concentration and phase volume ratio on the extraction efficiency of soybean protein were tested. Suitability of reverse micelles of AOT and Triton-X-100/AOT mixture in organic solvent toluene for soybean protein extraction was also investigated. The experimental results lead to complete forward extraction at the AOT concentration 120 mmol l⁻¹, aqueous pH 5.5 and KCl concentration 0.8 mol l⁻¹. The backward extraction with aqueous phase (pH 5.5) resulted in 100% extraction of soybean protein from the organic phase.     

Protein refolding mediated by reverse micelles of Cibacron Blue F-3GA modified nonionic surfactant

An affinity-based reverse micellar system formulated with nonionic surfactant was applied to the refolding of denatured-reduced lysozyme. The nonionic surfactant of sorbitan trioleate (Span 85) was modified with Cibacron Blue F-3GA (CB) as an affinity surfactant (CB-Span 85) to form affinity-based reverse micelles in n-hexane. The water content of 15 was found optimal for lysozyme refolding in the reverse micellar system of 62.7 mmol/L Span 85 with coupled CB of 0.3 and 0.5 mmol/L. In addition, the operating conditions such as pH and the concentrations of urea and redox reagents were optimized. Under the optimized conditions, complete renaturation of lysozyme at 3-3.5 mg/mL was achieved, whereas dilution refolding in the bulk aqueous phase under the same conditions gave much lower activity recovery. Moreover, the secondary structure of the refolded lysozyme was found to be the same as the native lysozyme. Over 95% of the refolded lysozyme was recovered from CB-Span 85 reverse micelles by a stripping solution of 0.5 mol/L MgCl(2). Thus, the present system is advantageous over the conventional reverse micellar system formed with ionic surfactants in the ease of protein recovery.     

Protein precipitation using an anionic surfactant

The precipitation of lysozyme from aqueous solution by direct addition of the anionic surfactant sodium bis-(2-ethylhexyl) sulfosuccinate (AOT) was investigated as a function of the AOT and lysozyme molar ratio between 5 and 35, and a pH ranging from 2 to 12. An optimum stoichiometric molar ratio of 16:1 (AOT:lysozyme) achieved 100% removal efficiency of lysozyme at pH 6.2. The effect of pH on protein removal indicated that electrostatic interactions between oppositely charged protein and surfactant molecules drives the precipitation process. This ionic interaction induces the formation of an uncharged lysozyme–AOT complex which is not soluble and hence precipitates. The change of lysozyme structure in the aqueous phase after precipitation was measured using circular dichroism spectroscopy and liquid chromatography, and considerable insight has been gained into surfactant initiated protein precipitation.     

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.     

Reverse micelles in protein separation: the use of silica for the back-transfer process

In order to use reverse micellar solutions successfully for the separation of proteins, good methods are needed to recover the biomolecules into an aqueous environment after solubilization into organic micellar media. Usually the recovery is accomplished by equilibrating the protein-loaded reverse micellar solution with a water phase containing an appropriate salt (back-transfer). In this article we describe an alternative "back extraction" procedure which is based on the addition of silica to the protein-containing reverse micellar solution. In this way, the water is stripped from the reverse micellar solution. [i.e., bis(2-ethylhexyl) sodium sulfosuccinate (AOT)/isooctane/water] and the proteins adsorb to the silica particles. The adsorption process is shown to be practically quantitative. The subsequent recovery of the proteins form the silica into an aqueous solution turns out to be most efficient at alkaline pH (pH 8); 60-80 of the total protein (alpha-chymotrypsin or trypsin) could be recovered. The specific enzyme activity at the end of the whole cycle can be as high as 80-100%. The procedure is applied also for the back extraction from micellar solutions in which, instead of AOT, a biocompatible surfactant such as a synthetic short-chain lecithin was used. It is shown that the recovery of a alpha-chymotrypsin and trypsin is also achievable under these conditions in quite good yield and under good maintenance of the enzyme's catalytic activity. (c) 1993 John Wiley & Sons, Inc.     

Mixed reverse micelles facilitated downstream processing of lipase involving water‐oil‐water liquid emulsion membrane

Our earlier work for the first time demonstrated that liquid emulsion membrane (LEM) containing reverse micelles could be successfully used for the downstream processing of lipase from Aspergillus niger. In the present work, we have attempted to increase the extraction and purification fold of lipase by using mixed reverse micelles (MRM) consisting of cationic and nonionic surfactants in LEM. It was basically prepared by addition of the internal aqueous phase solution to the organic phase followed by the redispersion of the emulsion in the feed phase containing enzyme, which resulted in globules of water‐oil‐water (WOW) emulsion for the extraction of lipase. The optimum conditions for maximum lipase recovery (100%) and purification fold (17.0‐fold) were CTAB concentration 0.075 M, Tween 80 concentration 0.012 M, at stirring speed of 500 rpm, contact time 15 min, internal aqueous phase pH 7, feed pH 9, KCl concentration 1 M, NaCl concentration 0.1 M, and ratio of membrane emulsion to feed volume 1:1. Incorporation of the nonionic surfactant (e.g., Tween 80) resulted in remarkable improvement in the purification fold (3.1–17.0) of the lipase. LEM containing a mixture of nonionic and cationic surfactants can be successfully used for the enhancement in the activity recovery and purification fold during downstream processing of enzymes/proteins. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1084–1092, 2014     

Single step purification of lactoperoxidase from whey involving reverse micelles‐assisted extraction and its comparison with reverse micellar extraction

The extraction of lactoperoxidase (EC 1.11.1.7) from whey was studied using single step reverse micelles‐assisted extraction and compared with reverse micellar extraction. The reverse micelles‐assisted extraction resulted in extraction of contaminating proteins and recovery of lactoperoxidase in the aqueous phase leading to its purification. Reverse micellar extraction at the optimized condition after forward and backward steps resulted in activity recovery of lactoperoxidase and purification factor of the order of 86.60% and 3.25‐fold, respectively. Whereas reverse micelles‐assisted extraction resulted in higher activity recovery of lactoperoxidase (127.35%) and purification factor (3.39‐fold). The sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS‐PAGE) profiles also evidenced that higher purification was obtained in reverse micelles‐assisted extraction as compared of reverse micellar extracted lactoperoxidase. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Antimicrobial activity of AOT-isooctane reverse micelle as a bioseparation and biocatalysis tool

Abstract

The antimicrobial activity of different reverse micelles on microorganisms is been compared using the disc diffusion method. The bis (2-ethylhexyl) sodium sulfosuccinate (AOT) reverse micelle showed a more significant inhibitory effect than do other reverse. micelles, and it had an antimicrobial activity against a broad range of microorganisms. Results from an antimicrobial activity test of isooctane and a forward extraction containing soybean protein suggest that the surfactant was chiefly responsible for inhibiting microbes in AOT/isooctane reverse micelle, while isooctane hardly inhibited the microbial growth. The properties of S. aureus, cultured in the TSB with AOT reverse micellar solution, were identified by the SEM and SDS-PAGE fingerprinting of cell-wall proteins. It is concluded that the cell-wall of the S. aureus decreased in the TSB with AOT reverse micellar solution, and some cell protein subunits of the S. aureus did not occurr, especially between 14.4 and 42.7 kDa, while one new protein subunit at near 97.4 kDa occurred     

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.     

Deactivation and conformational changes of cutinase in reverse micelles

Deactivation data and fluorescence intensity changes were used to probe functional and structural stability of cutinase in reverse micelles. A fast deactivation of cutinase in anionic (AOT) reverse micelles occurs due to a reversible denaturation process. The deactivation and denaturation of cutinase is slower in small cationic (CTAB/1-hexanol) reverse micelles and does not occur when the size of the cationic reverse micellar water-pool is larger than cutinase. In both systems, activity loss and denaturation are coupled processes showing the same trend with time. Denaturation is probably caused by the interaction between the enzyme and the surfactant interface of the reversed micelle. When the size of the empty reversed micelle water-pool is smaller than cutinase (at W0 5, with W0 being the water:surfactant concentration ratio) a three-state model describes denaturation and deactivation with an intermediate conformational state existing on the path from native to denaturated cutinase. This intermediate was clearly detected by an increase in activity and shows only minor conformational changes relative to the native state. At W0 20, the size of the empty water-pool was larger than cutinase and the data was well described by a two-state model for both anionic and cationic reverse micelles. For AOT reverse micelles at W0 20, the intermediate state became a transient state and the deactivation and denaturation were described by a two-state model in which only native and denaturated cutinase were present. For CTAB/1-hexanol reverse micelles at W0 20, the native cutinase was in equilibrium with an intermediate state, which did not suffer denaturation. 1-Hexanol showed a stabilizing effect on cutinase in reverse micelles, contributing to the higher stabilities observed in the cationic CTAB/1-hexanol reverse micelles. Copyright 1998 John Wiley & Sons, Inc.     

A simple peptide mapping method by partial filling micellar electrokinetic capillary chromatography with a zwitterionic-nonionic mixed micelle

A partial filling micellar electrokinetic capillary chromatography (PF-MEKC) method with a mixed micelle system composed of a zwitterionic surfactant named 3-(N,N-dimethylhexadecylammonium)propanesulfonate (PAPS) and a nonionic surfactant polyethylene glycol dodecyl ether (Brij 35) for peptide mapping is described. The method was demonstrated by the separation of tryptic digestion of bovine serum albumin (BSA). The optimal mixed micelle solution was 50 mM NH(4)OH-HCOOH buffer (pH 2.0) containing 32 mM PAPS and 0.6% (m/v) Brij 35. It was found that the mixed micelle system permitted a highly selective separation of the tryptic digestion. The high separation selectivity was probably due to the ion-pairing interaction between the zwitterionic surfactant molecules and the peptides.     

Fractionation of IgG fragments using reversed micellar extraction

Reversed micellar extraction was applied for the fractionation of IgG fragments. With isooctane solution containing 50 mM AOT, Fab, Fe and IgG were extracted to the micellar phase. Each protein had an optimum pH range in the extraction. Fab and Fc were separated from the mixture at pH 7.0, with Fab being extracted to the micellar phase and Fe remaining in the aqueous phase. Extracted Fab fragments were recovered by bringing them into contact with 6M guanidine/HCl followed by dilution with PBS. Fab and Fc fragments were separated and recovered by reversed micellar extraction from IgG lysate digested with papain. Since the procedure is simple and rapid compared with column chromatography, mass preparation of the fragments can be expected by this method.     

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。     

A simple method for extracting DNA from Cryptosporidium oocysts using the anionic surfactant LSS

Detection of low amounts of Cryptosporidium oocysts in raw water sources is considered an important component in the management, prevention and control of Cryptosporidium in drinking water supplies as Cryptosporidium causes massive waterborne outbreaks worldwide. As Cryptosporidium has a robust oocyst that is extremely resistant to chlorine and other drinking water disinfectants, both the freeze-thaw method and DNA extraction kits have been commonly used for extracting and purifying DNA from the oocyst. However, the DNA extraction procedures are time consuming and costly. Therefore, a simple and low-cost method to extract and purify DNA from the robust oocyst has been required. In this study, we discussed a simple method for detecting Cryptosporidium DNA with the anionic surfactant, n-lauroylsarcosine sodium salt (LSS) using the loop-mediated isothermal amplification (LAMP) to eliminate the need for the freeze-thaw method and the DNA extraction kits. As a result, Bst DNA polymerase was inhibited by 0.1% LSS but not 0.01% LSS and 5% Triton X-100 or Tween 20. Although DNA was extracted from the oocysts by incubating with 0.1% LSS at 90°C for 15 min, Bst DNA polymerase was inhibited by 0.1% LSS. The inhibition by 0.1% LSS was suppressed by adding 5% of the nonionic surfactants, Triton X-100 or Tween 20. The concentration of LSS in a LAMP tube was 0.01% while that in an incubation tube was 0.1%, because LSS in an incubation tube was diluted by a factor of 10 at the DNA amplification process. Therefore, we found that ten oocysts of Cryptosporidium parvum could be detected by incubation with 0.1% LSS, without removing LSS or adding the nonionic surfactants in the LAMP method.     

Effects of surfactant mixtures, including Corexit 9527, on bacterial oxidation of acetate and alkanes in crude oil

Mixtures of nonionic and anionic surfactants, including Corexit 9527, were tested to determine their effects on bacterial oxidation of acetate and alkanes in crude oil by cells pregrown on these substrates. Corexit 9527 inhibited oxidation of the alkanes in crude oil by Acinetobacter calcoaceticus ATCC 31012, while Span 80, a Corexit 9527 constituent, markedly increased the oil oxidation rate. Another Corexit 9527 constituent, the negatively charged dioctyl sulfosuccinate (AOT), strongly reduced the oxidation rate. The combination of Span 80 and AOT increased the rate, but not as much as Span 80 alone increased it, which tentatively explained the negative effect of Corexit 9527. The results of acetate uptake and oxidation experiments indicated that the nonionic surfactants interacted with the acetate uptake system while the anionic surfactant interacted with the oxidation system of the bacteria. The overall effect of Corexit 9527 on alkane oxidation by A. calcoaceticus ATCC 31012 thus seems to be the sum of the independent effects of the individual surfactants in the surfactant mixture. When Rhodococcus sp. strain 094 was used, the alkane oxidation rate decreased to almost zero in the presence of a mixture of Tergitol 15-S-7 and AOT even though the Tergitol 15-S-7 surfactant increased the alkane oxidation rate and AOT did not affect it. This indicated that there was synergism between the two surfactants rather than an additive effect like that observed for A. calcoaceticus ATCC 31012.