Aqueous Micellar Two-phase Systems Research Articles

Phase equilibrium and protein partitioning in aqueous micellar two-phase system composed of surfactant and polymer

The phase equilibrium and protein partitioning in the aqueous micellar two-phase system composed of nonionic surfactant polyoxyethylene octyl phenyl ether (Triton X-100) and polymer polyethylene glycol (PEG) with different low molecular weights are studied. The phase diagrams under various PEG molecular weight, salt concentration and pH value are determined at 298K. The results show that the biphase areas of the aqueous micellar two-phase system are expanded with an increase in PEG molecular weight or salt concentration, while the biphase areas and binodal curves are nearly unchanged by varying pH values. With raising PEG molecular weight, the tie lines lengths increase, and the tie lines slopes decrease first and then increase. Using lysozyme and bovine serum albumin (BSA) as model proteins, protein partitioning in the aqueous micellar two-phase system is investigated. As the hydrophilic proteins, both lysozyme and BSA partition preferably to the PEG-rich phases. The partition coefficients of proteins increase with increasing tie line length, or with decreasing PEG molecular weight and protein molecular size. These results indicate that the excluded volume interactions play an important role in protein partitioning in the aqueous micellar two-phase system composed of surfactant and polymer.

Extraction of the antimicrobial peptide cerein 8A by aqueous two-phase systems and aqueous two-phase micellar systems

Cerein 8A is an antimicrobial peptide with potential application against food spoilage and pathogenic bacteria. The partitioning of cerein 8A was investigated in two liquid–liquid extraction systems that are considered promising for bioseparation and purification purposes. Aqueous two-phase systems (ATPSs) were prepared with polyethylene glycol (PEG) and inorganic salts, and the addition of NaCl was investigated in this system. The best results concerning partition coefficients (K b) were obtained with PEG + ammonium sulphate, and K b value significantly increases when NaCl was added. Cerein 8A was effectively extracted into the micelle-rich phase in a 4% Triton X-114 medium. Recovery yield was higher for ATPS compared to micellar systems. Cerein 8A can be isolated from a crude suspension containing the bioactive molecule by ATPSs. Successful implementation of peptide partitioning represents an important step towards developing a low-cost effective separation method for cerein 8A.

Nanoparticle Mediated Protein Separation in Aqueous Micellar Two-Phase Systems

Magnetic nanoparticles with cation exchange functionality (MNCX) are combined with an Aqueous Micellar Two-Phase System (AMTPS) based on the nonionic surfactant Eumulgin ES for the purpose of protein separation. As proof of principle the positively charged protein lysozyme is separated from the negatively charged protein ovalbumin with a purity of approximately 100%. In comparison with the application of the MNCX alone, the presence of Eumulgin ES reduced the amount of lysozyme bound; however, the amount of eluted lysozyme stays the same. The advantage of applying the AMPTS is that the MNCX are easily handled as they partition completely into the dispersed phase of the system while the applied proteins partition almost entirely to the continuous phase.

Green fluorescent protein extraction and LPS removal from Escherichiacoli fermentation medium using aqueous two-phase micellar system

The viability of large-scale industrial production of recombinant biomolecules of pharmaceutical interest significantly depends on the separation and purification techniques used. In biotechnology, endotoxin (LPS) removal from recombinant proteins is a critical and challenging step in the preparation of injectable therapeutics, since endotoxin is a natural component of bacterial expression systems widely used to manufacture therapeutic proteins. This work aimed to study the use of aqueous two-phase micellar systems (ATPMS) from preparations containing recombinant proteins of pharmaceutical interest, such as green fluorescent protein (GFPuv), which works as a biological indicator. The GFPuv extraction and LPS removal were evaluated in ATPMS, partition assays were carried out using pure GFPuv and cell lysate from Escherichia coli. The ATPMS technology proved to be effective in GFPuv recovery, preferentially into the micelle-poor phase ( K GFPuv > 1), and LPS removal into the micelle-rich phase (% REM LPS > 98%). GFPuv was partitioned preferentially into the micelle-poor phase due to excluded-volume interactions in the micelle-rich phase. Therefore, this system can be exploited as the first step for purification in biotechnology processes for removal of higher LPS concentrations.

Primary recovery of lipase derived from Burkholderia sp. ST8 with aqueous micellar two-phase system

The partitioning and recovery of lipase derived from Burkholderia sp. ST8 strain was explored using temperature-induced aqueous micellar two-phase system (AMTPS) composed of single nonionic surfactant. Nonionic surfactant Triton X-114 and Pluronic series (triblock copolymer) were evaluated in terms of their clouding phenomenon (cloud-point temperature) and the performance of the lipase partitioning in these AMTPSs. Pluronic L81 showed the most optimum partition efficiency for the recovery of lipase to the micellar phase of the AMTPS. Based on the AMTPS which consisted of 24% (w/w) Pluronic L81 and 0.5% (w/w) potassium chloride (KCl), the selectivity of lipase partitioned to bottom phase has been enhanced to 0.035 and the lipase was purified 7.2 fold. Furthermore, the lipase from the micellar phase was consecutively extracted to a new aqueous solution, with an aim of removing the surfactant from the purified lipase. It was attained by replacing the aqueous top phase from the primary recovery of AMTPS with a new potassium thiocyanate (KSCN) solution. The lipase was then recovered in the newly formed bottom aqueous phase which culminated in the yield of 89% and partition coefficients of 0.34 and 4.50 for lipase and surfactant, respectively. AMTPS offers a convenient and efficient method for the primary recovery of lipase with low cost, large loading capacity and the potential of linear scale up.

Aqueous two-phase micellar systems in an oscillatory flow micro-reactor: study of perspectives and experimental performance

BACKGROUND: Aqueous two-phase micellar systems (ATPMS) are micellar surfactant solutions with physical properties that make them very efficient for the extraction/concentration of biological products. In this work the main proposal that has been discussed is the possible applicability and importance of a novel oscillatory flow micro-reactor (micro-OFR) envisaged for parallel screening and/or development of industrial bioprocesses in ATPMS. Based on the technology of oscillatory flow mixing (OFM), this batch or continuous micro-reactor has been presented as a new small-scale alternative for biological or physical-chemical applications. RESULTS: ATPMS experiments were carried out in different OFM conditions (times, temperatures, oscillation frequencies and amplitudes) for the extraction of glucose-6-phosphate dehydrogenase (G6PD) in Triton X-114/buffer with Cibacron Blue as affinity ligand. CONCLUSION: The results suggest the potential use of OFR, considering this process a promising and new alternative for the purification or pre-concentration of bioproducts. Despite the applied homogenization and extraction conditions have presented no improvements in the partitioning selectivity of the target enzyme, when at rest temperature they have influenced the partitioning behavior in Triton X-114 ATPMS. Copyright © 2011 Society of Chemical Industry

Direct determination of the composition of aqueous micellar two-phase systems (AMTPS) using potentiometric titration—A rapid tool for detergent-based bioseparation

Coexistence curves of two different aqueous micellar two-phase systems (AMTPS) were determined by potentiometric titration. The nonionic surfactants Triton X-114 and Eumulgin ES were quantified by means of the Metrohm NIO Surfactant Electrode with excellent correlations coefficients. The influence of different media on the titration end-point was ascertained. Measurement in the presence of commonly used biotechnological buffers 2-(N-morpholino)ethanesulfonic acid (MES), sodium phosphate, and 2-(Bis(2-hydroxyethyl)amino)acetic acid (bicine) as well as in the supernatant of an E. coli fermentation exhibited deviations below 5%. Coexistence curves of Triton X-114 AMTPS and Eumulgin ES AMTPS were investigated in a temperature range of 25–40 °C by measuring the surfactant concentration of both, the detergent-rich (coacervate) and the detergent-depleted (aqueous) phase after phase separation. The resulting coexistence curves are in good agreement with those published by authors who have employed the cloud point method. Yet, potentiometric titration outranges the cloud point method as it provides direct information about the compositions of the coacervate and the aqueous phase, which form when an AMTPS is shifted up to a temperature at which it splits.

LPS removal from an E. coli fermentation broth using aqueous two‐phase micellar system

In biotechnology, endotoxin (LPS) removal from recombinant proteins is a critical and challenging step in the preparation of injectable therapeutics, as endotoxin is a natural component of bacterial expression systems widely used to manufacture therapeutic proteins. The viability of large-scale industrial production of recombinant biomolecules of pharmaceutical interest significantly depends on the separation and purification techniques used. The aim of this work was to evaluate the use of aqueous two-phase micellar system (ATPMS) for endotoxin removal from preparations containing recombinant proteins of pharmaceutical interest, such as green fluorescent protein (GFPuv). Partition assays were carried out initially using pure LPS, and afterwards in the presence of E. coli cell lysate. The ATPMS technology proved to be effective in GFPuv recovery, preferentially into the micelle-poor phase (K(GFPuv) < 1.00), and LPS removal into the micelle-rich phase (%REM(LPS) > 98.00%). Therefore, this system can be exploited as the first step for purification in biotechnology processes for removal of higher LPS concentrations.

Enhancing the lateral-flow immunoassay for viral detection using an aqueous two-phase micellar system.

Availability of a rapid, accurate, and reliable point-of-care (POC) device for detection of infectious agents and pandemic pathogens, such as swine-origin influenza A (H1N1) virus, is crucial for effective patient management and outbreak prevention. Due to its ease of use, rapid processing, and minimal power and laboratory equipment requirements, the lateral-flow (immuno)assay (LFA) has gained much attention in recent years as a possible solution. However, since the sensitivity of LFA has been shown to be inferior to that of the gold standards of pathogen detection, namely cell culture and real-time PCR, LFA remains an ineffective POC assay for preventing pandemic outbreaks. A practical solution for increasing the sensitivity of LFA is to concentrate the target agent in a solution prior to the detection step. In this study, an aqueous two-phase micellar system comprised of the nonionic surfactant Triton X-114 was investigated for concentrating a model virus, namely bacteriophage M13 (M13), prior to LFA. The volume ratio of the two coexisting micellar phases was manipulated to concentrate M13 in the top, micelle-poor phase. The concentration step effectively improved the M13 detection limit of the assay by tenfold from 5 × 108 plaque forming units (pfu)/mL to 5 × 107 pfu/mL. In the future, the volume ratio can be further manipulated to yield a greater concentration of a target virus and further decrease the detection limits of the LFA. FigureA schematic representation of concentrating viruses with an aqueous two-phase micellar system containing Triton X-114 surfactant prior to the detection of the virus through the lateral-flow immunoassay Electronic supplementary materialThe online version of this article (doi:10.1007/s00216-010-4213-7) contains supplementary material, which is available to authorized users.

Concentration of mammalian genomic DNA using two‐phase aqueous micellar systems

The concentration of biomarkers, such as DNA, prior to a subsequent detection step may facilitate the early detection of cancer, which could significantly increase chances for survival. In this study, the partitioning behavior of mammalian genomic DNA fragments in a two-phase aqueous micellar system was investigated using both experiment and theory. The micellar system was generated using the nonionic surfactant Triton X-114 and phosphate-buffered saline (PBS). Partition coefficients were measured under a variety of conditions and compared with our theoretical predictions. With this comparison, we demonstrated that the partitioning behavior of DNA fragments in this system is primarily driven by repulsive, steric, excluded-volume interactions that operate between the micelles and the DNA fragments, but is limited by the entrainment of micelle-poor, DNA-rich domains in the macroscopic micelle-rich phase. Furthermore, the volume ratio, that is, the volume of the top, micelle-poor phase divided by that of the bottom, micelle-rich phase, was manipulated to concentrate DNA fragments in the top phase. Specifically, by decreasing the volume ratio from 1 to 1/10, we demonstrated proof-of-principle that the concentration of DNA fragments in the top phase could be increased two- to nine-fold in a predictive manner.

Hydrophobin (HFBI): A potential fusion partner for one-step purification of recombinant proteins from insect cells

Hydrophobins play an important role in binding and assembly of fungal surface structures as well as in medium–air interactions. These, hydrophobic properties provide interesting possibilities when purification of macromolecules is concerned. In aqueous micellar two-phase systems, based on surfactants, the water soluble hydrophobins are concentrated inside micellar structures and, thus, distributed to defined aqueous phases. This, one-step purification is attractive particularly when large-scale production of recombinant proteins is concerned. In the present study the hydrophobin HFBI of Trichoderma reesei was expressed as an N-terminal fusion with chicken avidin in baculovirus infected insect cells. The intracellular distribution of the recombinant fusion construct was analyzed by confocal microscopy and the protein subsequently purified from cytoplasmic extracts in an aqueous micellar two-phase system by using a non-ionic surfactant. The results show that hydrophobin and an avidin fusion thereof were efficiently expressed in insect cells and that these hydrophobic proteins could be efficiently purified from these cells in one-step by adopting an aqueous micellar two-phase system.

Can affinity interactions influence the partitioning of glucose-6-phosphate dehydrogenase in two-phase aqueous micellar systems?

In this work, we provide an investigation of the role and strength of affinity interactions on the partitioning of the glucose-6-phosphate dehydrogenase in aqueous two-phase micellar systems. These systems are constituted of micellar surfactant solutions and offer both hydrophobic and hydrophilic environments, providing selectivity to biomolecules. We studied G6PD partitioning in systems composed of the nonionic surfactants, separately, in the presence and absence of affinity ligands. We observed that G6PD partitions to the micelle-poor phase, owing to the strength of excluded-volume interactions in these systems that drive the protein to the micelle-poor phase, where there is more free volume available.

Liquid–liquid extraction of commercial and biosynthesized nisin by aqueous two-phase micellar systems

Nisin is a natural additive for conservation of food, and can also be used as a therapeutic agent. Nisin inhibits the outgrowth of spores, the growth of a variety of Gram-positive and Gram-negative bacteria. In this paper we present a potentially scalable and cost-effective way to purify commercial and biosynthesized in bioreactor nisin, including simultaneously removal of impurities and contaminants, increasing nisin activity. Aqueous two-phase micellar systems (ATPMS) are considered promising for bioseparation and purification purposes. Triton X-114 was chosen as the as phase-forming surfactant because it is relatively mild to proteins and it also forms two coexisting phases within a convenient temperature range. Nisin activity was determined by the agar diffusion assay utilizing Lactobacillus sake as a sensitive indicator microorganism. Results indicated that nisin partitions preferentially to the micelle rich-phase, despite the surfactant concentration tested, and its antimicrobial activity increases. The successful implementation of this peptide partitioning, from a suspension containing other compounds, represents an important step towards developing a separation method for nisin, and more generally, for other biomolecules of interest.

Aqueous micellar two-phase system composed of hyamine-type hydrophobically modified ethylene oxide and application for cytochrome P450 BM-3 separation

The hydrophobically modified ethylene oxide polymer, HM-EO, was modified with an alkyl halide to prepare a hyamine-type HM-EO, named N-Me-HM-EO, which could be used for forming N-Me-HM-EO/buffer aqueous micellar two-phase system. The critical micelle concentration of N-Me-HM-EO solution and the phase diagrams of N-Me-HM-EO/buffer systems were determined. By using this novel aqueous micellar two-phase system, the separation of cytochrome P450 BM-3 from cell extract was explored. The partitioning behavior of P450 BM-3 in N-Me-HM-EO/buffer systems was measured. The influences of some factors such as total proteins concentration, pH, temperature and salt concentration, on the partitioning coefficients of P450 BM-3 were investigated. Since the micellar aggregates in the N-Me-HM-EO enriched phase were positively charged, it was possible to conduct the proteins with different charges to top or bottom phases by adjusting pH and salt concentration in the system. A separation scheme consisting of two consecutive aqueous two-phase extraction steps was proposed: the first extraction with N-Me-HM-EO/buffer system at pH 8.0, and the second extraction in the same system at pH 6.0. The recovery of P450 BM-3 was 73.3% with the purification factor of 2.5. The results indicated that the aqueous micellar two-phase system composed of hyamine modified polysoap has a promising application for selective separation of biomolecules depending on the enhanced electrostatic interactions between micelles and proteins.

Bioseparations in Aqueous Micellar Systems Based on Excluded-Volume Interactions

Protein partitioning based on micellar-induced excluded-volume interactions is studied for different aqueous nonionic micellar systems. In particular, protein partitioning in the traditional aqueous micellar two-phase system is compared with a system where a gel phase is combined with a micellar phase and with a membrane system with micelles at the feed side of the membrane. A two-phase system is created using cylindricallyshaped n -decyl tetra(ethylene oxide) (C 10 E 4 ) micelles that are too large to diffuse into the gel-bead or across the membrane. Results are reported for the partition coefficient of single-component protein systems with myoglobin, ovalbumin, and BSA, and for binary protein mixtures. The individual protein partition coefficients in the mixtures follow the same protein concentration dependence as the partition coefficient obtained for the singlecomponent protein solutions.

Affinity‐tagged green fluorescent protein (GFP) extraction from a clarified E. coli cell lysate using a two‐phase aqueous micellar system

Green fluorescent protein (GFP) has been proposed as an ideal choice for a protein-based biological indicator for use in the validation of decontamination or disinfection treatments. In this article, we present a potentially scalable and cost-effective way to purify recombinant GFP, produced by fermentation in Escherichia coli, by affinity-enhanced extraction in a two-phase aqueous micellar system. Affinity-enhanced partitioning, which improves the specificity and yield of the target protein by specific bioaffinity interactions, has been demonstrated. A novel affinity tag, family 9 carbohydrate-binding module (CBM9) is fused to GFP, and the resulting fusion protein is affinity-extracted in a decyl beta-D-glucopyranoside (C10G1) two-phase aqueous micellar system. In this system, C10G1 acts as phase forming and as affinity surfactant. We will further demonstrate the implementation of this concept to attain partial recovery of affinity-tagged GFP from a clarified E. coli cell lysate, including the simultaneous removal of other contaminating proteins. The cell lysate was partitioned at three levels of dilution (5x, 10x, and 40x). Irrespective of the dilution level, CBM9-GFP was found to partition preferentially to the micelle-rich phase, with the same partition coefficient value as that found in the absence of the cell lysate. The host cell proteins from the cell lysate were found to partition preferentially to the micelle-poor phase, where they experience less excluded-volume interactions. The demonstration of proof-of-principle of the direct affinity-enhanced extraction of CBM9-GFP from the cell lysate represents an important first step towards developing a cost-effective separation method for GFP, and more generally, for other proteins of interest.

Affinity‐enhanced protein partitioning in decyl β‐D‐glucopyranoside two‐phase aqueous micellar systems

Liquid-liquid extraction in two-phase aqueous complex-fluid systems has been proposed as a scalable, versatile, and cost-effective purification method for the downstream processing of biotechnological products. In the case of two-phase aqueous micellar systems, careful choices of the phase-forming surfactants or surfactant mixtures allow these systems to separate biomolecules based on size, hydrophobicity, charge, or specific affinity. In this article, we investigate the affinity-enhanced partitioning of a model affinity-tagged protei--green fluorescent protein fused to a family 9 carbohydrate-binding module (CBM9-GFP)--in a two-phase aqueous micellar system generated from the nonionic surfactant n-decyl beta-D-glucopyranoside (C10G1), which acts simultaneously as the phase-former and the affinity ligand. In this simple system, CBM9-GFP was extracted preferentially into the micelle-rich phase, despite the opposing tendency of the steric, excluded-volume interactions operating between the protein and the micelles. We obtained more than a sixfold increase (from 0.47 to 3.1) in the protein partition coefficient (Kp), as compared to a control case where the affinity interactions were "turned off" by the addition of a competitive inhibitor (glucose). It was demonstrated conclusively that the observed increase in Kp can be attributed to the specific affinity between the CBM9 domain and the affinity surfactant C10G1, suggesting that the method can be generally applied to any CBM9-tagged protein. To rationalize the observed phenomenon of affinity-enhanced partitioning in two-phase aqueous micellar systems, we formulated a theoretical framework to model the protein partition coefficient. The modeling approach accounts for both the excluded-volume interactions and the affinity interactions between the protein and the surfactants, and considers the contributions from the monomeric and the micellar surfactants separately. The model was shown to be consistent with the experimental data, as well as with our current understanding of the CBM9 domain.

Two-phase aqueous micellar systems: an alternative method for protein purification

Two-phase aqueous micellar systems can be exploited in separation science for the extraction/purification of desired biomolecules. This article reviews recent experimental and theoretical work by Blankschtein and co-workers on the use of two-phase aqueous micellar systems for the separation of hydrophilic proteins. The experimental partitioning behavior of the enzyme glucose-6-phosphate dehydrogenase (G6PD) in two-phase aqueous micellar systems is also reviewed and new results are presented. Specifically, we discuss very recent work on the purification of G6PD using: i) a two-phase aqueous micellar system composed of the nonionic surfactant n-decyl tetra(ethylene oxide) (C10E4), and (ii) a two-phase aqueous mixed micellar system composed of C10E4 and the cationic surfactant decyltrimethylammonium bromide (C10TAB). Our results indicate that the two-phase aqueous mixed (C10E4/C10TAB) micellar system can improve significantly the partitioning behavior of G6PD relative to that observed in the two-phase aqueous C10E4 micellar system.

Glucose‐6‐phosphate dehydrogenase partitioning in two‐phase aqueous mixed (nonionic/cationic) micellar systems

The enzyme glucose-6-phosphate dehydrogenase (G6PD) plays an important role in maintaining the level of NADPH and in producing pentose phosphates for nucleotide biosynthesis. It is also of great value as an analytical reagent, being used in various quantitative assays. In searching for new strategies to purify this enzyme, the partitioning of G6PD in two-phase aqueous mixed (nonionic/cationic) micellar systems was investigated both experimentally and theoretically. Our results indicate that the use of a two-phase aqueous mixed micellar system composed of the nonionic surfactant C(10)E(4) (n-decyl tetra(ethylene oxide)) and the cationic surfactant C(n)TAB (alkyltrimethylammonium bromide, n = 8, 10, or 12) can improve significantly the partitioning behavior of G6PD relative to that obtained in the two-phase aqueous C(10)E(4) micellar system. This improvement can be attributed to electrostatic attractions between the positively charged mixed (nonionic/cationic) micelles and the net negatively charged enzyme G6PD, resulting in the preferential partitioning of G6PD to the top, mixed micelle-rich phase of the two-phase aqueous mixed micellar systems. The effect of varying the cationic surfactant tail length (n = 8, 10, and 12) on the denaturation and partitioning behavior of G6PD in the C(10)E(4) /C(n)TAB/buffer system was investigated. It was found that C(8)TAB is the least denaturing to G6PD, followed by C(10)TAB and C(12)TAB. However, the C(10)E(4)/C(12)TAB/buffer system generated stronger electrostatic attractions with the net negatively charged enzyme G6PD than the C(10)E(4)/C(10)TAB/buffer and the C(10)E(4)/C(8)TAB/buffer systems, when using the same amount of cationic surfactant. Overall, the two-phase aqueous mixed (C(10)E(4)/C(10)TAB) micellar system yielded the highest G6PD partition coefficient of 7.7, with a G6PD yield in the top phase of 71%, providing the optimal balance between the denaturing effect and the electrostatic attractions for the three cationic surfactants examined. A recently developed theoretical framework to predict protein partition coefficients in two-phase aqueous mixed (nonionic/ionic) micellar systems was implemented, and the theoretically predicted G6PD partition coefficients were found to be in reasonable quantitative agreement with the experimentally measured ones.

L-asparaginase release from Escherichia coli cells with aqueous two-phase micellar systems.

A method was proposed to release and separate L-asparaginase (EC 3.5.1.1) from Escherichia coli ATCC 11303 cells with aqueous two-phase micellar systems. The systems were composed of K2HPO4 and Triton X-100. The method combines enzyme release with enzyme purification. The influence of Triton X-100 concentration, K2HPO4 concentration, and pH on the release and partition of L-asparaginase was investigated. Experimental results showed that E. coli cells treated with 9.4% (w/v) K2HPO4 and 15% (w/v) Triton X-100 at 25 degrees C for 15-20 h released nearly 80% of the enzyme. Most of the released enzyme was partitioned to the bottom phase (phosphate-rich phase). The effects of Triton X-100 concentration, K2HPO4 concentration, and pH on cloud point were also studied. Electron micrography indicated that the chemical treatment altered the inner structure of E. coli cells significantly.