Design of surfactants suitable for protein extraction by reversed micelles

New surfactants have been synthesized for potential use in reversed micellar protein extraction operations. Preferential solubility of the surfactant in an aliphatic solvent such as hexane, heptane, or isooctane and the formation of reversed micelles accompanied with solubilization of significant quantities of water can be achieved by using strongly hydrophobic, twin alkyl chains as the hydrophobic moiety. Different surfactants having identical water-solubilizing capacities can have significantly different behavior in protein extractions, where extraction efficiency appears to be governed by the nature of the interfacial complex that forms between surfactants and proteins. Bulky surfactant chains provide a steric hindrance to the adsorption of the surfactant to the protein surface, thus inhibiting solvation of the protein/surfactant complex, and hence protein extraction. Under these conditions, a precipitate forms either in the bulk aqueous phase or at the interface. Surfactants that can form a close-packed complex with the protein are excellent protein-solubilizing agents. Dioleyl phosphoric acid (DOLPA) appears to be the best surfactant currently available for protein extraction. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 26-32, 1997.     

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.     

Colloidal gas aphrons: A novel approach to protein recovery

Sebba (1987) defined colloidal gas aphrons (CGA) as microbubbles stabilized by surfactant layers, which are created by stirring surfactant solutions at speeds greater than a critical value. A high shear impeller is used for stirring and critical values for the impeller speed must be exceeded to create these stable gas liquid dispersions (typically >5000 rpm). Although there have been no previous reports of direct protein recovery using CGA, it is likely that, with appropriate choice of surfactant, proteins should adsorb to these surfactant bubbles by means of electrostatic and/or hydrophobic interactions. This is the basis of this study, in which the use of CGA for protein recovery from aqueous solution is considered. A surfactant which has been characterized previously for generation of CGA was chosen (Jauregi et al., 1997), i.e., the anionic surfactant sodium bis-(2-ethyl hexyl) sulfosuccinate (AOT). Lysozyme, a well-characterized protein, was chosen as the protein to be recovered. Lysozyme was recovered successfully from aqueous solution using CGA generated from AOT. At optimum conditions, lysozyme recovery, enrichment ratio, and separation ratio were 95%, 19 and 302 respectively, with enzyme activity maintained. These results indicate the exciting potential of this technique. A wide range of process conditions including initial concentration of protein and surfactant, surfactant/protein molar ratio, pH, and ionic strength were considered. High recoveries and enrichments were generally obtained at protein concentrations 0.11 mg/mL. However, at high ionic strength (0.29M) poor separation and recoveries were obtained at low protein concentrations (counter-ions diminishing electrostatic interactions between protein and aphrons at this condition). In general, (ns/np)a was determined to be between 10 and 16 for experiments in which high levels of recovery/separation parameters were found. For most conditions, protein precipitation was observed; however, this precipitate could be resolubilized without loss of enzyme activity.     

Efficient isolation and elution of cellular proteins using aptamer-mediated protein precipitation assay

Protein precipitation is one of the most widely used methods for antigen detection and purification in biological research. We developed a reproducible aptamer-mediated magnetic protein precipitation method that is able to efficiently capture, purify and isolate the target proteins. We discovered DNA aptamers having individually high affinity and specificity against human epidermal growth factor receptor (EGFR) and human insulin receptor (INSR). Using aptamers and magnetic beads, we showed it is highly efficient technique to enrich endogenous proteins complex and is applicable to identify physiologically relevant protein–protein interactions with minimized nonspecific binding of proteins. The results presented here indicate that aptamers would be applicable as a useful and cost-effective tool to identify the presence of the particular target protein with their specific protein partners.     

Direct immunoprecipitation of antigen with phage displaying immunoglobulin fragment

Phage libraries may display hormones, receptors, antibody fragments, etc., by fusion to phage envelope proteins. This report describes the direct precipitation of phage-Fab-antigen complexes by polyethylene glycol precipitation, resulting in highly selective and efficient recovery of antigen from complex mixtures without nonspecific protein contamination. The method demonstrates efficiency and specific recovery of phage-Fab-antigen complexes from a background of a complex mixture of unrelated proteins as may occur in the analysis of biological specimens. This simple, fast, and effective method allows isolation and characterization of target antigens, with no need to further process Fab or sFv, and may reasonably be extended to isolate any interacting partner molecule for any displayed protein.     

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.     

液质联用多反应监测法定量目标多肽或蛋白质

为建立优化的血浆内源性多肽提取方法,并且构建目标多肽和蛋白质的质谱定量方 法,本研究考察了超滤法、有机溶剂沉淀法和固相萃取法对血浆内源性多肽的提取效果 ,并通过Tricine-SDS-PAGE对提取效果进行比较.通过液相色谱串联质谱多反应监测 （MRM）分析,建立了多肽标准品ESAT-6定量方法,并将ESAT-6定量建立的液相色谱和质谱条件应用于蛋白质的定量,对多肽和蛋白质MRM定量的标准曲线进行了考 察.Tricine-SDS-PAGE结果表明,乙腈沉淀法是最佳的血浆内源性多肽提取方法,低分子量的多肽可以得到很好的富集,且能有效地去除高分子蛋白质的污染.液相色谱串联 质谱MRM法检测血浆内提取的多肽,标准曲线的线性较好,相关系数为0.999.另外,采 用MRM法对胶内分离的蛋白质进行定量,标准曲线的线性相关系数为0.995.综上所述, 本研究构建了一种简单有效的血浆多肽提取方法,通过液质联用MRM法成功地实现了目标多肽和蛋白质定量测定.该定量方法可以推广应用于复杂样品中的多肽和蛋白质的定 量分析.     

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.     

乳腺生物反应器表达的重组人乳清白蛋白的高效分离纯化

利用乳腺生物反应器高效地表达重组人乳清白蛋白,但是目标产物分离纯化的难度较大。通过分子模拟计算比较待分离原料中主要蛋白组分的物化性质,包括表面电势和表面疏水性,在此基础上设计了高分辨率、快速的分离纯化工艺。通过硫酸铵沉淀的正交试验条件优化,有效地去除了干扰层析精制过程的IgG杂质,提高了后续疏水层析的稳定性,从而成功地分离开目标蛋白及与其同源的牛乳清白蛋白杂质,得到纯度>95%的rHLA纯品,工艺回收率48.6%。乳糖合成活性和圆二色谱检测结果表明,纯化rHLA具有调节β-1,4-半乳糖苷转移酶活性和天然的空间结构。     

Protein recovery from surfactant precipitation

The recovery of lysozyme from an aqueous solution containing precipitated lysozyme-AOT complexes formed by the direct addition of sodium bis-(2-ethylhexyl) sulfosuccinate (AOT) to a lysozyme solution was studied using both solvents, and a counterionic surfactant. Ethanol,methanol and solvent mixtures dissolved the surfactant precipitate and recovered lysozyme as a solid. Recovery efficiency and protein stability varied with the type of solvent used. An entirely different method of recovery was also evaluated using a counterionic surfactant: tri-octylmethylammonium chloride (TOMAC) which bound to AOT releasing lysozyme into solution.Complete recovery (100%) of lysozyme was achieved at a molar ratio of 2:1(TOMAC:AOT), and the original protein activity was maintained in the final aqueous phase.The recovered lysozyme retained its secondary structure as observed in circular dichroism(CD) spectra. Specific activity studies show that counterionic surfactant extraction does not alter the biological activity of the enzyme.     

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.     

Protein extraction by reverse micelles: studies on the recovery of horseradish peroxidase

Phase transfer studies were carried out on the solubilization of horseradish peroxidase (HRP) (E.C. 1.11.1.7) in reverse micelles formed in isooctane using the anionic surfactant, aerosol OT, at concentrations between 50 and 110mM. The selectivity of this methodology was tested, because the HRP used comprised a mixture of seven different isoenzymes with a wide range of isoelectric points. Forward and backward transfers were carried out in wellstirred vessels until equilibrium was reached. Significant protein partitioning could only be obtained by using NaCl to adjust ionic strength in pH range between 1.5 and 3.5, with a maximum at pH 3. The back transfer process was best at pH 8 with 80mM phosphate buffer and 1 M KCI. A loss of 1% to 3% of the surfactant through precipitation at the interface at pH<4 was observed, which may be due to instability in this pH region, because, even without protein, a similar precipitate was noticed. Protein partitioning was approximately constant when the ionic strength was increased up to 1 MNaCl at pH 3, but protein recovery in back transfer decreased accordingly. Hydrophobic interactions together with association between the protein and surfactant might be responsible for that behavior. Protein partitioning remained the same when the surfactant concentration was decreased to 50 mM, at the expense of higher variability. HPLC chromatograms showed no apparent damage to the protein after reverse micellar extraction. Protein partitioning is best when the temperature is kept at 25xC. The amount of protein and specific activity recovered strongly depends on the phase ratio used during forward transfer. Overall activity recovery varied from 87% to 136% when the phase ratio was increased from 1:1 to 30:1 in forward transfer. This behavior may be due to a change in the ratio of the three isoenzymes recovered after the backward transfer process, with the most active one being increasingly enriched at higher phase ratios. (c) 1994 John Wiley & Sons, Inc.     

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.     

疏水层析结合冷乙醇沉淀纯化人血清白蛋白

将层析技术与冷乙醇工艺相结合用于人血清白蛋白的纯化 ,对各过程所采用的层析介质及层析条件进行了探索 ,得到了一条从人血浆中制备血清白蛋白的新路线 :将一步冷乙醇沉淀后的血浆上清进行脱盐除乙醇 ,用阳离子交换介质CMSepharoseFF以透过式层析的模式吸附非白蛋白组分 ,最后选用ButylSepharoseFF一步疏水层析后所得样品经SDS-PAGE银染显示一条单带 ,分析其纯度大于 99% ,计算工艺收率为 81.2%。与传统冷乙醇工艺相比较 ,该工艺最终样品纯度更高 ,且层析可以在常温下操作 ,易实现自动化控制.     

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.     

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.     

Backward extraction of reverse micellar encapsulated proteins using a counterionic surfactant

The back-extraction of proteins encapsulated in AOT reverse micelles was performed by adding a counterionic surfactant, either TOMAC or DTAB. This novel backward transfer method gave higher backward extraction yields compared to the conventional method with high salt and high pH of the aqueous stripping solution. The protein activity was maintained in the resulting aqueous phase, which in this case had a near neutral pH and low salt concentration. A sharp decrease of the water content was observed in the organic phase corresponding to protein back-extraction using TOMAC. The backward transfer mechanism was postulated to be caused by electrostatic interaction between oppositely charged surfactant molecules, which lead to the collapse of the reverse micelles. The back-extraction process with TOMAC was found to be very fast; more than 100 times faster than back-extraction with the conventional method, and as much as 3 times faster than forward extraction. The formation of 1:1 complexes of AOT and TOMAC in the solvent phase was observed, and these hydrophobic complexes could be efficiently removed from the solvent using adsorption onto Montmorillonite in order for the organic solvent to be reused. A second cationic surfactant, DTAB, confirmed the general applicability of counterionic surfactants for the backward transfer of proteins.     

Bacteria capture, lysate clearance, and plasmid DNA extraction using pH-sensitive multifunctional magnetic nanoparticles

A multifunctional magnetic nanoparticle (MNP)-assisted bioseparation method was developed to isolate plasmid DNA (pDNA) from Escherichia coli culture. Using the pH-sensitive carboxyl-modified magnetic nanoparticles, both cell capture and the subsequent removal of genomic DNA/protein complex after lysis can be achieved simply by magnetic separation. Furthermore, the yield and purity of pDNA extracted by MNPs are comparable to those obtained using organic solvents or commercial kits. This time- and cost-effective protocol does not require centrifugation or precipitation steps and has the potential for automated DNA extraction, especially within miniaturized lab chip applications.     

Interaction of reduced lysozyme with surfactants: Disulfide effects on reformed structure in micelles

The reformation of secondary structure for unfolded, disulfide reduced hen egg white lysozyme (HEWL) upon interaction with surfactants was studied using CD, fluorescence and IR (infrared) techniques. Equilibrium CD studies showed that reduced HEWL when mixed with negatively charged surfactants, such as SDS (sodium dodecyl sulfate), gradually regains average helical structure to a level equivalent to that obtained for the oxidized form also in SDS, but both forms lose tertiary structure in such environments. This non-native structure recovery process begins with monomer surfactant interaction but at higher concentrations is in part dependent on micelle formation, with the helical fraction reaching its maximum value with each surfactant only above the CMC. Fluorescence changes were more complex, evidencing an intermediate state at lower surfactant concentration. With positively charged surfactants the degree of helicity recovered was less, and the intermediate state in fluorescence was not seen. Stopped flow dynamics studies showed the CD kinetics fit to two exponentials as did the fluorescence. The faster steps in CD and fluorescence detected kinetics appear to be correlated which suggests formation of an intermediate on rapid interaction of the micelle and protein. The second step then reflected attainment of a stable surfactant solvated state which attains maximum helicity and moves the Trps to a more hydrophobic environment, which may occur in independent steps, as the slower kinetics are not well correlated.     

Micro-quantitation of lipids in serum-free cell culture media: a critical aspect is the minimization of interference from medium components and chemical reagents

Lipids (fatty acids) at a concentration range of 10-100 microg/L are essential components included in most serum-free cell culture medium formulations. A gas chromatography/mass spectrometry (GC/MS) method for the micro-quantitation of lipids, determined as fatty acid methyl esters (FAMEs), in complex serum-free cell culture media was developed. The interference of derivatizing reagents, extraction solvents and medium additives in the micro-quantitation of lipids was also examined. The results show that the concentration of fatty acids such as palmitic and stearic acids detected in derivatizing reagents or extraction solvents was in the range of 10-230 microg/L. Tween-80, a surfactant and medium additive, produced nearly 20 FAMEs alone when methylated using a derivatizing agent. Moreover, the surfactant Pluronic F-68, a medium additive, interfered in the FAME recovery. Procedures, which include use of low volumetric ratio of reagent to medium and precipitation of the above surfactants, were developed to minimize background FAMEs to levels which do not significantly affect the quantitation of medium lipids and to diminish the interference caused by Pluronic F-68. Fatty acid concentrations in several complex serum-free culture media were quantitated by this method and were very close to the values indicated in their formulations.