Selective separation and purification of two lipases from chromobacterium viscosum using AOT reversed micelles

Selective separation and purification of two lipases form Chromobacterium viscosum were carried out by liquid-liquid extraction using a reversed micellar system. Optimum parameters for extraction were determined using a 250 mM AOT micellar solution in isooctane. Complete separation of the two lipases was achieved at pH 6.0 with a 50mM potassium phosphate buffer solution containing 50 mM KCI. By adding 2.5% by volume of ethanol to the lipase-loaded micellar solution, 85% of the extracted lipase could be recovered in a new aqueous phase, 50 mM K(2)HPO(4) with 50 mM KCl, at pH 9.0. Lipase A was purified 2.6-fold with a recovery of 86%, and lipase B by 1.5-fold with a recovery of 76%.     

Forward and backward extraction rates of amino acid in reversed micellar extraction

The mass transfer characterization in reversed micellar extraction of amino acid phenylalanine (Phe) is presented. The mass transfer rates in forward extraction of Phe from aqueous KCl solutions (pH 1.4 – 2.3) to AOT/isooctane reversed micellar solutions and in backward extraction from the reversed micellar organic phase to KHCO₃/KOH buffer solutions (pH 9.0 – 11.0) were investigated using a stirred cell with a flat liquid–liquid interface. Both the forward and the backward extraction rates are controlled by the interfacial rate processes, i.e., the solubilization and the release processes. The solubilizing rate constants for the forward extraction of Phe increase with decreasing pH and initial Phe concentration and with increasing initial AOT concentration. On the other hand, the releasing rate constants for the backward extraction decrease with increasing initial AOT concentration and with decreasing ionic strength, but are little influenced by pH. The backward extraction rates are fairly slow compared to the forward extraction rates, and are accelerated by the addition of 2-methyl-2-propanol, similar to the extraction of protein lysozyme.     

Liquid-liquid extraction of a recombinant cutinase from fermentation media with AOT reversed micelles

This work reports the extraction and back-extraction of an intracellular recombinant cutinase from complex biological media using AOT reversed micelles in isooctane. Cutinase was recovered from different complex media namely, fermentation broths and supernatants after cell disruption by osmotic shock and sonication. The application of the AOT reversed micellar system to the extraction of cutinase allowed activity yields and purification factors ranging from about 5% to 50% and 1.2 to 10.2, respectively, depending on the biological medium.Maria das Graças Carneiro da Cunha, from ITEP-Instituto Tecnológico do Estado de Pernambuco, acknowledges a Ph.D fellowship from Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq) and Centro de Pesquisa Aggeu Magalhães, Recife — PE — Brasil. E. P. Melo thanks Junta Nacional de Investigação Científica, Lisboa, Portugal, for providing a Ph.D. fellowship. The scientific support given by Prof. Sílvia M. B. Costa for the spectroscopic data and further discussions are particularly acknowledged.This work was partly financed by the BRIDGE and BIOTECHNOLOGY Programmes (Contracts BIOT-CT91-0274(DTEE) and BIOT 2 CT-943016).     

Continuous extraction of a recombinant cutinase from Escherichia coli disrupted cells with reversed micelles using a perforated rotating disc contactor

This work reports on the continuous extraction of a recombinant cutinase with reversed micelles using a perforated rotating disc contactor. Intracellular cutinase was directly extracted at 20°C with 100 mM AOT in isooctane from complex biological media of Escherichia coli disrupted cells. The optimal conditions for the direct extraction of the enzyme from media containing cell debris led to an extraction yield of 54.4%.     

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.     

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.     

Recovery of a recombinant cutinase with reversed micelles in a continuous perforated rotating disc contactor

Summary A continuous perforated rotating disc contactor was used for the extraction of a recombinant cutinase from an aqueous solution to a reversed micellar phase of AOT in isooctane. Cutinase was extracted to the organic phase with protein yield of 78% after 70 minutes of operation.     

Liquid-liquid extraction of lectin from Cratylia mollis seeds using reversed micelles

Extraction of lectin from seeds ofCratylia mollis, camaratu bean, with reversed micelles of 100 mM sodium di(2-ethylhexyl) sulfosuccinate/isooctane was performed firstly with affinity-purified lectin. The best conditions were extraction of the seed extract at pH 5 and back-extraction at pH 10, giving yields of 38% and 100%, respectively.     

Process optimization for reverse micellar extraction of stem bromelain with a focus on back extraction

In the current study, reverse micellar extraction (RME) for the purification of stem bromelain was successfully achieved using the sodium bis(2‐ethylhexyl) sulfosuccinate (AOT)/isooctane system. A maximum forward extraction efficiency of 58.0% was obtained at 100 mM AOT concentration, aqueous phase pH of 8.0 and 0.2 M NaCl. Back extraction studies on altering stripping phase pH and KCl concentration, addition of counter‐ion and iso‐propyl alcohol (IPA) and mechanical agitation with glass beads indicated that IPA addition and agitation with glass beads have significant effects on extraction efficiency. The protein extraction was higher (51.9%) in case of the IPA (10% v/v) added system during back extraction as compared to a cetyltrimethylammonium bromide (100 mM) added system (9.42%). The central composite design technique was used to optimize the back extraction conditions further. Concentration of IPA, amount of glass beads, mixing time, and agitation speed (in rpm) were the variables selected. IPA concentration of 8.5% (v/v), glass bead concentration of 0.6 (w/v), and mixing time of 45 min at 400 rpm resulted in higher back extraction efficiency of 45.6% and activity recovery of 88.8% with purification of 3.04‐fold. The study indicated that mechanical agitation using glass beads could be used for destabilizing the reverse micelles and release of bromelain back into the fresh aqueous phase. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:845–855, 2014     

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.     

Solubilizing water involved in protein extraction using reversed micelles

The extraction of protein using reversed micelles was investigated in relation to the amount of solubilizing water in the reversed micellar organic phase. The minimal concentration of amphiphilic molecule di-2-ethylhexyl sodium sulfosuccinate (C(20)H(37)O(7)Na) (AOT) required for 100% cytochrome c extraction was recognized. This critical AOT concentration increased with protein concentration in the aqueous phase. On this minimal AOT condition, the molar ratio of solubilizing water to extracted protein was found to be a constant of 3500 under C(KCI) = 1.0 x 10(2) mol . m(-3) in this system. This ratio means the hydrophillic surroundings required for extracting one protein molecule into the micellar organic phase under the suitable pH and salt concentration for the forward extraction. In this regard, AOT molecules seemed to take the part of water solubilizing agent in the reversed micellar extraction. This role of AOT is important to extract protein under the suitable pH and salt concentration. The amount of solubilizing water in the protein-containing system was larger than in the protein-free system. This difference shows that the water molecules accompany the extracted protein into the reversed micellar organic phase at constant ratio 2200 under C(KCI) = 1.0 x 10(2) mol . m(-3), i.e., accompanying water molecules per one extracted protein. The minimal AOT concentration increased with ionic strength. On this minimal AOT condition, the molar ratio of solubilizing water to extracted protein also increased with ionic strength, so that in higher ionic strength, more solubilizing water was required. Then more AOT was required to provide the hydrophillic surroundings for protein. The pH affected the minimal AOT concentration required for 100% protein extraction.     

Extraction and purification of a lectin from small black kidney bean (Phaseolus vulgaris) using a reversed micellar system

Lectin from crude extract of small black kidney bean (Phaseolus vulgaris) was successfully extracted using the reversed micellar extraction (RME). The effects of water content of organic phase (W_o), ionic strength, pH, Aerosol-OT (AOT) concentration and extraction time on the forward extraction and the pH and ionic strength in the backward extraction were studied to optimize the extraction efficiency and purification factor. Forward extraction of lectin was found to be maximum after 15 min of contact using 50 mM AOT in organic phase with W_o 27 and 10 mM citrate-phosphate buffer at pH 5.5 containing 100 mM NaCl in the aqueous phase. Lectin was backward extracted into a fresh aqueous phase using sodium-phosphate buffer (10 mM, pH 7.0) containing 500 mM KCl. The overall yield of the process was 53.28% for protein recovery and 8.2-fold for purification factor. The efficiency of the process was confirmed by gel electrophoresis analysis.     

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。     

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.     

Separation and purification of penicillin acylase from Escherichia coli using AOT reverse micelles

Summary The extraction of penicillin acylase by reverse micellar solutions of a surfactant was studied. A 50 mM solution of dioctyl sodium sulphosuccinate in isooctane extracted 46% of the enzyme activity in a crude periplasmic extract of induced cells of E. coli ATCC 9637. The increase in the specific activity of the final enzyme preparation, after stripping of the organic phase at pH 7.5, in the presence of 1 M KCl, was 8 - fold.Abbreviations PA penicillin acylase (penicillin amidohydrolase EC 3.5.1.11) - AOT Aerosol OT (dioctyl sodium sulphosuccinate) - NIPAB 6-nitro-3-(phenylacetamido)-benzoic acid - NABA 6-nitro-3-aminobenzoic acid - BSA bovine serum albumin - SDS sodium dodecylsulphate     

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.     

Reverse micellar extraction for downstream processing of lipase: Effect of various parameters on extraction

Reverse micellar extraction of lipase using cationic surfactant cetyltrimethylammonium bromide (CTAB) was investigated. The effect of various process parameters on both forward and backward extraction of lipase from crude extract was studied to optimize its yield and purity. Forward extraction of lipase was found to be maximum using Tris buffer at pH 9.0 containing 0.10 M NaCl in aqueous phase and 0.20 M CTAB in organic phase consisting of isooctane, butanol and hexanol. In case of backward extraction, lipase was extracted from the organic phase to a fresh aqueous phase in 0.05 M potassium phosphate buffer (pH 7.0) containing 1.0 M KCl. The activity recovery, extraction efficiency and purification factor of lipase were found to be 82.72%, 40.27% and 4.09-fold, respectively. The studies also indicated that the organic phase recovered after back extraction could be reused for the extraction of lipase from crude extract.     

Separation and purification of periplasmic cytochrome c553 using reversed micelles

Surfactant concentration, ionic strength, and pH were optimised for the selective separation and purification of periplasmic cytochrome c553 from recombinant E. coli TG2 cells using response surface methodology. Back-extraction was accomplished using counter-ionic surfactant addition. Optimum forward extraction conditions were: 65 mM bis(2-ethylhexyl)sulfosuccinate sodium salt (AOT), 0.07 M NaCl, and pH 8.4, while the optimum back-extraction conditions were 80 mM trioctylmethylammonium chloride, 0.85 M KCl, and pH 9.62. In comparison to a conventionally purified sample using column chromatography (10 mg cytochrome c553 l–1 with a purity of 0.66), reverse micelles achieved the same concentration and similar purity (0.50) in only two simple steps.     

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。     

Extraction and purification of laccase by employing a novel rhamnolipid reversed micellar system

Biosurfactant-based reversed micellar extraction (RME) is an innovative method for separation and purification of biomolecules. In this study, rhamnolipid (RL), a kind of biosurfactant, was firstly adopted to form a novel reversed micellar system for extracting and purifying laccase from Coriolus versicolor crude extract. Several significant factors affecting both forward and backward extraction processes were studied. The appropriate conditions for forward extraction process were: 3.3 mM RL, 50 mM KCl, pH 5.5 and extracting time 40 min. As regards backward extraction process, 250 mM KCl, pH 7.0 and extracting time 40 min were suggested. The corresponding activity recovery (AR) and purification fold (PF) were 92.7% and 4.79, respectively. Electrophoresis analysis indicated that the laccase was successfully purified. After this reversed micellar system was reused three times, the AR and PF declined to 70.8% and 4.35, respectively, indicating that the reversed micellar system could be reused. Comparisons results of synthetic surfactant-based RME and RL-based RME further verified the superiority of RL.