Continuous foaming for protein recovery: part I. Recovery of beta-casein

Foam separation is known to have potential for separation of biological molecules with a range of surface activities. A statistical study (factorial design) was carried out to establish the optimum operating conditions for the continuous foam separation of beta-casein. Maximum values of enrichment of beta-casein into the foam phase were found for low levels of initial feed protein concentration, gas flow rate, feed-flow rate, and high foam heights. Maximum values of protein recovery, were generally found at high levels of initial feed protein concentration, gas-flow rate, feed-flow rate, and low foam heights. The highest values obtained for enrichment and separation ratio were 54.7 and 181.3, respectively, with a simultaneous protein recovery of 62%; thus, illustrating the potential effectiveness of this technique. The effect of foaming on protein conformation is also important, and in this study protein structure was analyzed before and after foam separation experiments. Techniques used were: native polyacrylamide gel electrophoresis (PAGE), UV absorbance spectroscopy, circular dichroism, and fluorescence. Native PAGE showed no detectable changes in protein structure. However, absorbance scanning, fluorimetry, and circular dichroism revealed some conformational changes over a range of concentration effects.     

Partition of protein from binary mixtures by a batch foaming process

An experimental study to assess the partition of 3 binary protein mixtures when foam separated is presented (proteins considered were bovine serum albumin (BSA), conalbumin and lysozyme). Results show that selective partition of protein can be achieved and under certain conditions it is possible to strip the initial solution of BSA. However, purity of the foam phase is limited due to the non-selective carry-up of other proteins in the interstitial liquid.     

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.     

Foam fractionation of globular proteins

Foam fractionation of bovine serum albumin (BSA) was studied as a model system for potato wastewater. The effects of feed concentration, superficial gas velocity, feed flow rate, bubble size, pH, and ionic strength on the enrichment and recovery of BSA were investigated in a single-stage continuous foam fractionation column. Enrichments ranged from 1.5 to 6.0 and recoveries from 5 to 85%. The feed concentrations were varied from 0.01 to 0.2 wt %, and enrichments were found to increase with lower feed concentrations. Enrichments also increased with lower superficial gas velocities and larger bubble sizes. At sufficiently low feed flow rates, enrichment was found to increase with an increase in the flow rate, eventually becoming insensitive to the feed flow rate at higher values. The pH was varied from 3.5 to 7.0 and ionic strength from 0.001M to 0.2M. The effects of pH and ionic strength were found to be coupled with bubble size. A minimum bubble size was found at pH 4.8, the isoelectric point of BSA, resulting in a minimum in the enrichment. Bubble size, and thus enrichment, was found to increase as the ionic strength decreased from 0.2M to 0.01M. Previous models(1,2) for the hydrodynamics of foam column were extended for a singlestage continuous foam fractionation column for the prediction of enrichment and recovery. The model assumed adsorption equilibrium, infinite surface viscosity, and bubbles of the same size. Though coalescence was formally accounted for in the model by considering bubble size as a function of foam height, calculations for the experimental runs were performed only for the case of no coalescence. Quantitative predictions of enrichment and recovery could not be made with a single representative bubble size because of the broad inlet bubble size distribution as well as broadening of the distribution as a result of coalescence. The experimental enrichments were higher and recoveries were lower than the model predictions, the discrepancy being more pronounced at lower feed concentrations because of increased coalescence. The higher enrichments are due to the predominant effect of internal reflux as a result of coalescence whereas the lower recoveries are a result of detrimental effects of broadening bubble size distributions.     

The application of foaming for the recovery of Surfactin from B. subtilis ATCC 21332 cultures

Foaming, a proficient method for the recovery of surface active solutes from dilute solutions, was successfully applied for the concentration of the lipopeptide biosurfactant Surfactin from B. subtilis ATCC 21332 cell culture broths. Foaming was only partially successful in concentrating Surfactin when applied as a separate semi-batch unit downstream of the cell culture stage. Surfactin partitioned strongly into the foam during the latter stages of the semi-batch process, where enrichments of over 50 could be obtained. However, simultaneous high enrichments and recoveries of Surfactin could not be obtained as the majority of Surfactin (around 70% of the total recovered) was produced at a low concentration during the early stages of foaming. Foam fractionation was considered for both cell free and cell containing broths; the presence of cells increased the foamability of the solution and therefore yielded more dilute Surfactin preparations. More favourable recovery and enrichment of Surfactin occurred when foaming was integrated with the cell culture stage. The use of low stirrer speeds was essential in producing foam at a controlled rate. By collecting fractions of the foam produced between 10 and 30 hours, from systems stirred at 166 and 146 rpm, a highly concentrated Surfactin extract could be obtained. The Surfactin concentration in the foam was 1.22 and 1.67 g l(-1) respectively, which represented enrichments and percent recoveries of over 60. This study points to the utility of foaming as a method for the recovery of surface-active fermentation products, particularly when used in an integrated production/recovery system.     

高速逆流双水相色谱法纯化卵白蛋白

生物大分子的液_固色谱纯化过程中固相载体会产生产物吸附、变性等不良影响。高速逆流色谱无需固相载体 ,且具有高分便率和高回收率的优点 ,其中有机相 水相体系在分离天然产物中应用广泛 ,而应用双水相体系分离生物大分子尚处于研究阶段。双水相高速逆流色谱体系的建立与仪器设备及操作工艺条件密切相关 ,因此利用多分离柱高速逆流色谱仪 ,研究了PEG1000-无机盐双水相体系对标准蛋白质混合物以及卵白蛋白的分离。pH值和PEG浓度对不同种类蛋白质的分配系数影响不同 ,实验发现在pH9.2的150% (W/W)PEG1000 170% (W/W)磷酸钾盐体系中 ,细胞色素C、溶菌酶和肌红蛋白的分配系数差异较大 ,且分布合理 ,因而采用该体系在 0 8mL min流速 ,85 0r min转速的条件下 ,成功分离了细胞色素C、溶菌酶和肌红蛋白的混合物。实验也发现在pH9 2的 16 0 % (W/W)PEG10 0 0 17 0 % (W/W)磷酸钾盐体系中 ,鸡蛋清样品中的主要蛋白质成分:卵转铁蛋白、卵白蛋白和溶菌酶的分配系数差异最大 ,因而采用该体系在 1 8mL min流速、85 0r mi转速的条件下,200min内从鸡蛋清样品中成功分离卵白蛋白,其电泳纯度为100%,收率为95%.     

Aqueous polymer two-phase systems formed by new thermoseparating polymers

A set of new polymers that can be used as phase forming components in aqueous two-phase systems is presented. All polymers studied have thermoseparating properties i.e. form one separate polymer enriched phase and one aqueous solution when heated above the critical temperature. This property makes the polymers attractive alternatives to the polymers used in traditional aqueous two-phase systems such as poly(ethylene glycol) (PEG) and dextran. The thermal phase separation simplifies recycling of the polymers, thus making the aqueous two-phase systems more cost efficient and suitable for use in large scale. Thermoseparating polymers studied have been copolymers of ethylene oxide and propylene oxide (EO-PO), poly (N-isopropylacrylamide) (poly-NIPAM), poly vinyl caprolactam (poly-VCL) and copolymers of N-isopropylacrylamide and vinyl caprolactam with vinyl imidazole (poly(NIPAM-VI) and poly(VCL-VI), respectively). In addition, the copolymer poly(NIPAM-VI) has the property to be uncharged at pH above 7.0 and positively charged at lower pH. This allows the partitioning of protein to be directed by changing the pH in the system instead of the traditional addition of salt to direct the partitioning. Hydrophobically modified EO-PO copolymer (HM-(EO-PO)) with alkyl groups (C₁₄) at both ends forms two-phase system with for example poly(NIPAM-VI). The phase diagram for poly(NIPAM-VI)/HM-(EO-PO) was determined and the model proteins lysozyme and BSA were partitioned in this system. For BSA in poly(NIPAM-VI)/HM-(EO-PO) system a change in pH from 8.0 to 5.4 results in a change of partition coefficient from K=0.8 to K=5.1, i.e. BSA could be transferred from the HM-(EO-PO) phase to the poly(NIPAM-VI) phase. BSA partitioning in poly(NIPAM-VI)/HM-(EO-PO) system allows quantitative BSA recovery, and recoveries of poly(NIPAM-VI) and HM-(EO-PO) were 53% and 92%, respectively, after the thermoseparation step.     

Foam fractionation of protein: correlation of protein adsorption onto bubbles with a pH-induced conformational transition

A foam fractionation apparatus was prepared to aid protein separation at the gas–liquid interface. Using lysozyme as a model protein, we investigated the alteration of enzymatic and optical activities through foaming. The lysozyme transferred to the gaseous nitrogen phase after 5 min of bubbling with no exogenous detergent. The bacteriolytic and optical activities of lysozyme from the foamate were nearly equivalent to those of the original lysozyme. This result indicated that lysozyme did not irreversibly denature during foam fractionation. We then performed protein separation using binary mixtures of lysozyme and α-amylase. When the two proteins were dissolved in bulk solution of pH 10.5, which is close to the isoelectric point (pI) of lysozyme (10.7), selective fractionation of lysozyme from the foam was observed. Indeed, this fractionation was identical to that from a single component solution of lysozyme. Similarly, selective fractionation of α-amylase was achieved in pH 3.0 buffer. Furthermore, circular dichroism (CD) and subsequent model fitting revealed that the protein had a reduced or nearly complete absence of α-helical content, whereas the amount of β-sheet structure and random coil was elevated in the buffer conditions that promoted protein adsorption. These results indicate that a pH-induced conformational transition might correlate with protein foaming.     

Mechanisms of phase behaviour and protein partitioning in detergent/polymer aqueous two-phase systems for purification of integral membrane proteins

Detergent/polymer aqueous two-phase systems are studied as a fast, mild and efficient general separation method for isolation of labile integral membrane proteins. Mechanisms for phase behaviour and protein partitioning of both membrane-bound and hydrophilic proteins have been examined in a large number of detergent/polymer aqueous two-phase systems. Non-ionic detergents such as the Triton series (polyoxyethylene alkyl phenols), alkyl polyoxyethylene ethers (C(m)EO(n)), Tween series (polyoxyethylene sorbitol esters) and alkylglucosides form aqueous two-phase systems in mixtures with hydrophilic polymers, such as PEG or dextran, at low and moderate temperatures. Phase diagrams for these mixtures are shown and phase behaviour is discussed from a thermodynamic model. Membrane proteins, such as bacteriorhodopsin and cholesterol oxidase, were partitioned strongly to the micelle phase, while hydrophilic proteins, BSA and lysozyme, were partitioned to the polymer phase. The partitioning of membrane protein is mainly determined by non-specific hydrophobic interactions between detergent and membrane protein. An increased partitioning of membrane proteins to the micelle phase was found with an increased detergent concentration difference between the phases, lower polymer molecular weight and increased micelle size. Partitioning of hydrophilic proteins is mainly related to excluded volume effects, i.e. increased phase component size made the hydrophilic proteins partition more to the opposite phase. Addition of ionic detergent to the system changed the partitioning of membrane proteins slightly, but had a strong effect on hydrophilic proteins, and can be used for enhanced separation between hydrophilic proteins and membrane protein.     

Polyethyleneglycol molecular mass and polydispersivity effect on protein partitioning in aqueous two-phase systems

The partitioning of model proteins (bovine serum albumin, ovalbumin, trypsin and lysozyme) was assayed in aqueous two-phase systems formed by a salt (potassium phosphate, sodium sulfate and ammonium sulfate) and a mixture of two polyethyleneglycols of different molecular mass. The ratio between the PEG masses in the mixtures was changed in order to obtain different polymer average molecular mass. The effect of polymer molecular mass and polydispersivity on the protein partition coefficient was studied. The relationship between the logarithm of the protein partition coefficient and the average molecular mass of the phase-forming polymer was found to depend on the polyethyleneglycol molecular mass, the salt type in the bottom phase and the molecular weight of the partitioned protein. The polymer polydispersivity proved to be a very useful tool to increase the separation between two proteins having similar isoelectrical point.     

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.     

Cerium ion-chelated magnetic silica microspheres for enrichment and direct determination of phosphopeptides by matrix-assisted laser desorption ionization mass spectrometry

In this study, we employed, for the first time, the Ce4+-chelated magnetic silica microspheres to selectively concentrate phosphopeptides from protein digest products. Cerium ions were chelated onto magnetic silica microspheres using the strategy we established before. After enrichment, the phosphopeptide-conjugated magnetic microspheres were separated from the sample solution just by using a magnet. With the optimized enrichment conditions, the performance of the Ce4+-chelated magnetic microspheres was compared with the Fe3+-chelated microspheres using tryptic digested peptides originating from ovalbumin, a five protein mixture containing phosphoproteins and nonphosphoproteins, as well as a mixture of beta-casein and BSA with a molar ratio of 1:50. Compared to Fe3+, Ce4+-chelated magnetic microspheres exhibited more selective isolation ability for concentrating phosphopeptides from complex mixtures. Even when the amount of the tryptic digest product of BSA is 50 times higher than that of beta-casein in the sample solution, the trace phosphopeptides derived from beta-casein can still be concentrated effectively by the Ce4+-chelated magnetic microspheres in only 30 s. Furthermore, we initially utilized the Ce4+-chelated magnetic microspheres to directly enrich phosphopeptides from human serum without extra purification steps or tedious treatment, which opens up a possibility for their further application in phosphoproteomics.     

Polymer recycling in aqueous two-phase extractions using thermoseparating ethylene oxide–propylene oxide copolymers

This is a study on the recovery and recycling of copolymer in aqueous two-phase systems containing random copolymers of ethylene oxide (EO) and propylene oxide (PO). The random copolymers separate from water solution when heated above the lower critical solution temperature (LCST). The primary phase systems were composed of EOPO copolymer and hydroxypropyl or hydroxyethyl starch. After phase separation the upper EOPO phase was removed and subjected to temperature induced phase separation. Copolymers with different EO/PO compositions have been investigated, EO50PO50 [50% EO and 50% PO (w/w)], EO30PO70 and EO20PO80. The temperature required for thermoseparation decreases when the PO content of the copolymer is increased. The effect on the recovery of copolymer after addition of salts, a second polymer or protein was investigated. The added components increased the recovery of copolymer after thermoseparation, e.g., increased the amount copolymer separated from the water phase after thermoseparation. Recycling of copolymer and measurements of polymer concentrations in the primary top and bottom phases after repeated recycling steps was performed. The fluctuation in polymer concentration of the phases was very small after recycling up to four times. Partitioning of the proteins BSA and lysozyme was studied in primary phase systems after recycling of copolymer. The partition coefficients of total protein and lysozyme was not significantly changed during recycling of copolymer. More than 90% of the copolymer could be recovered in the thermoseparation step by optimising the temperature and time for thermoseparation. In repeated phase partitionings in EOPO–starch systems the EO50PO50 copolymer could be recovered to 77% including losses in primary system and thermoseparation, which is equivalent to a total copolymer reuse of 4.3 times.     

Correlation of diafiltration sieving behavior of lysozyme-BSA mixtures with osmotic second virial cross-coefficients

The role of protein-protein interactions in membrane separations of protein mixtures remains incompletely understood, largely due to the difficulty of characterizing protein self- and, especially, cross-association. Recently, a novel technique, cross-interaction chromatography, has been developed to measure weak protein cross-association in terms of the osmotic second virial cross-coefficient. In this work the relationship between protein cross-association and the sieving behavior of lysozyme in the presence of BSA has been investigated. Sieving coefficients were measured using a stirred diafiltration cell over a range of pH and ionic strength, and a striking correlation between the lysozyme sieving and second virial cross-coefficients for BSA/lysozyme mixtures has been found: when the protein cross-interactions are most attractive (negative second virial cross-coefficient), the lysozyme sieving coefficients are lowest, and vice versa. The correlation between the sieving and second virial cross-coefficients may be due to the physically similar environments in the chromatography and filtration experiments since one protein is passed through a concentrated region of the second protein either immobilized on the column or accumulated at the membrane surface, and the migration rate of the mobile protein in both cases is influenced by protein cross-association. This study represents the first time that molecular interactions in binary mixtures have been related directly to filtration behavior, and may provide a useful approach to optimize the separation of other binary protein mixtures.     

Novel Fe3O4@TiO2 core-shell microspheres for selective enrichment of phosphopeptides in phosphoproteome analysis

Due to the dynamic nature and low stoichiometry of protein phosphorylation, enrichment of phosphorylated peptides from proteolytic mixtures is often necessary prior to their characterization by mass spectrometry. Immobilized metal affinity chromatography (IMAC) is a popular way to enrich phosphopeptides; however, conventional IMAC lacks enough specificity for efficient phosphoproteome analysis. In this study, novel Fe 3O 4@TiO 2 microspheres with well-defined core-shell structure were prepared and developed for highly specific purification of phosphopeptides from complex peptide mixtures. The enrichment conditions were optimized using tryptic digests of beta-casein, and the high specificity of the Fe 3O 4@TiO 2 core-shell microspheres was demonstrated by effectively enriching phosphopeptides from the digest mixture of alpha-casein and beta-casein, as well as a five-protein mixture containing nonphosphoproteins (bovine serum albumin (BSA), myoglobin, cytochrome c) and phosphoproteins (ovalbumin and beta-casein). The Fe 3O 4@TiO 2 core-shell microspheres were further successfully applied for the nano-LC-MS/MS analysis of rat liver phosphoproteome, which resulted in identification of 56 phosphopeptides (65 phosphorylation sites) in mouse liver lysate in a single run, indicating the excellent performance of the Fe 3O 4@TiO 2 core-shell microspheres.     

Aqueous two-phase protein partitioning using textile dyes as affinity ligands.

A simple and inexpensive aqueous two-phase system for the affinity partitioning of proteins is introduced. An aqueous solution consisting of maltodextrin (M100; molecular mass, 1800) and polyvinylpyrrolidone (PVP360; molecular mass, 360,000) formed two phases at 4 degrees C when the concentration of the polymers was 22.5% (w/w) and 4.0% (w/w), respectively. When the amino derivatives of chlorotriazine textile dyes or other azo textile dyes were added to the two-phase system they partitioned asymmetrically, favoring the upper, less dense, PVP360-rich phase. The association of the textile dyes with PVP360 did not prevent them from acting as affinity ligands for proteins. Three of the dyes screened increased the partition coefficient of purified lysozyme nearly 50-fold over a control containing no dye. Parameters such as pH, ionic strength, and dye concentration modulated the affinity-partitioning effect of the system. The partition coefficient of lysozyme in an egg white protein mixture increased severalfold as the total protein content of the system approached 4% (w/w), indicating that protein concentration is also important in determining the partitioning characteristics of this two-phase system. Proteins were efficiently freed of PVP360 and textile dye by recovery in a high-salt solution when another two-phase system was formed upon the addition of a solution of concentrated potassium phosphate to the isolated upper phase of a PVP360/M100/textile dye two-phase system. The affinity-partitioning system presented here allows one to screen large numbers of potentially useful protein ligands to optimize protein separation, followed by direct scaleup to a system size determined by the user.     

Protein adsorption at solid-liquid interfaces: Part II--Adsorption from binary protein mixture

Extent of adsorption of proteins at alumina-water interface from solutions containing binary mixture of beta-lactoglobulin and bovine serum albumin (BSA), beta-lactoglobulin and gelatin, and gelatin and bovine serum albumin has been estimated as functions of protein concentrations at varying pH, ionic strength, temperature and weight fraction ratios of protein mixture. The extent of adsorption (gamma lacw) of lactoglobulin in the presence of BSA increases with increase of protein concentration (Clac) until it reaches a maximum but a fixed value gamma lacw(m). Extent of adsorption gamma serw also initially increases with increase of protein concentrations until it reaches maximum value gamma serw(m). Beyond these protein concentrations, adsorbed BSA is gradually desorbed due to the preferential adsorption of lactoglobulin from the protein mixture. In many systems, gamma serw at high protein concentrations even becomes negative due to the strong competition of BSA and water for binding to the surface sites in the presence of lactoglobulin. For lactoglobulin-gelatin mixtures, adsorption of both proteins is enhanced as protein concentration is increased until limiting values for adsorption are reached. Beyond the limiting value, lactoglobulin is further accumulated at the interface without limit when protein concentration is high. For gelatin-albumin mixtures, extent of gelatin adsorption increases with increase in the adsorption of BSA. The limit for saturation of adsorption for gelatin is not reached for many systems. At acid pH, adsorbed BSA appears to be desorbed from the surface in the presence of gelatin. From the results thus obtained the role of electrostatic and hydrophobic effects in controlling the adsorption process has been analysed.     

Aqueous two-phase extraction for protein recovery from corn extracts

Corn has been used as an expression host for several recombinant proteins with potential for large-scale production. Cost-effective downstream initial recovery, separation and concentration remain a challenge. Aqueous two-phase (ATP) partitioning has been used to recover and concentrate proteins from fermentation broths and offers advantages for integration of those steps with biomass removal. To examine the applicability of ATP partitioning to recombinant protein purification from corn endosperm and germ, ATP system parameters including poly(ethylene glycol) (PEG) molecular weight (MW), phase-forming salt, tie line length (TLL), and pH were manipulated to control partitioning of extracted native proteins from each fraction. Moderate PEG MW, reduction of phase ratio, and added NaCl effected complete recovery of the hydrophobic model protein lysozyme in the top phase with ca. 5x enrichment and illustrates a favorable match of recombinant protein characteristics, expression host, and separation method. Furthermore, integration of protein extraction with the partitioning reduced the load of contaminating host proteins relative to the more traditional separate steps of extraction followed by partitioning. Performance of the integrated partitioning was hindered by endosperm solids loading, whereas for germ, which has ca. 35x higher aqueous soluble protein, the limit was protein solubility. For more hydrophilic model proteins (the model being cytochrome c), effective separation required further reduction of PEG MW to effect more partitioning of host proteins to the top phase and enrichment of the model protein in the lower phase. The combination of PEG MW of 1450 with 8.5 wt.% NaCl addition (Na(2)SO(4) as the phase-forming salt) provided for complete recovery of cytochrome c in the lower phase with enrichment of 9x (germ) and 5x (endosperm). As a result of lower-phase recovery, the advantage of simultaneous removal of solids is lost. The lower solubility of native endosperm proteins results in higher purity for the same enrichment.     

Analysis of multi-component fluorescence emission by phase-sensitive detection using one modulation frequency

We describe the use of phase-sensitive detection of fluorescence to resolve the lifetimes and fractional intensities from multi-component fluorescence samples, using data obtained at a single modulation frequency. Phase-sensitive spectra of the mixture are recorded at arbitrarily chosen detector phase angles. The steady-state spectrum of each component must be known. The phase-sensitive spectra are fitted, using a nonlinear least-squares algorithm, to obtain the lifetimes and fractional intensities of each fluorophore in the mixture. Simulations for two- and three-component mixtures are presented to illustrate how the resolution is affected by spectral overlap and lifetime separation. Experimentally, we resolved two- and three-component mixtures of protein-like fluorophores (N-acetyl-L-tyrosinamide, N-acetyl- L-tryptophanamide, indole and 2,3-dimethylindole) using data collected at 30 MHz. These fluorophores have closely spaced lifetimes of 1.5, 2.9, 4.5 and 4.3 ns, respectively, and display extensive spectral overlap. These results demonstrate that phase-sensitive spectra, recorded at only one modulation frequency with a standard phase fluorometer, can be used to resolve multi-component emissions.     

Model Phase Separations of Proteins Using Aqueous/Ethanol Components

Of several saturated or partially saturated inorganic salt solutions forming stable biphasic systems when mixed with ethanol, K₂HPO₄/ethanol was used to partition several model proteins, including lysozyme, BSA, chymotrypsinogen and the DNA polymerase from Thermus aquaticus. Partitioning was pH-dependent, and was successfully used for protein isolation from a mixture. Varying degrees of enzymatic activities were maintained.