Partitioning behavior of amino acids in aqueous two-phase systems with recyclable volatile salts

As part of an ongoing research effort on aqueous two-phase systems (ATPSs) with volatile salts, this work describes the partitioning behavior of a series of amino acids, namely -serine, glycine, -alanine, -valine, -methionine, -isoleucine, and -phenylalanine, in these systems. The results show that amino acids partition in a similar way in polymer–volatile salt ATPSs and in traditional polymer–salt ATPSs. Increasing amino acid hydrophobicities lead to increasing partition coefficients. Moreover, the common linear relationship between the logarithm of the partition coefficient and the tie line length is observed here as well. Furthermore, the relation between relative partition coefficients and relative hydrophobicities of amino acids in the extraction systems investigated in this work is comparable to that in other extraction systems.     

Partitioning of recombinant human granulocyte-macrophage colony stimulating factor (hGM-CSF) from plant cell suspension culture in PEG/sodium phosphate aqueous two-phase systems

Partitioning of human granulocyte-macrophage colony stimulating factor (hGM-CSF) was achieved in the aqueous two-phase systems (ATPSs) using a crude extract of transgenic tobacco cell suspension culture. This study examined the effects of polyethylene glycol (PEG) molecular weight and concentration and the effects of sodium phosphate concentration in different PEG/sodium phosphate systems on the partition coefficient,K. The best ATPS system was 5% PEG 8,000/1.6 M sodium phosphate after 2 h of incubation at room temperature. In this system, hGM-CSF was partitioned in the PEG-rich phase with a yield of 57.99% andK _hGM-CSF of 8.12. In another system, 3% PEG 10,000/1.6 M sodium phosphate, hGM-CSF was also partitioned primarily in the top phase with a yield of 45.66% andK _hGM-CSF of 7.64 after 2 h of incubation at room temperature.     

Determinants of liposome partitioning in aqueous two-phase systems: Evaluation by means of a factorial design

This article evaluates the influence of five parameters on liposome partitioning in aqueous two-phase systems (ATPSs), composed of poly(ethyleneglycol) (PEG)/dextran (Dx), using the factorial experimental design together with a multiple regression. Mathematical models to quantify the influence of these parameters, individually and/or jointly, on liposome partitioning in ATPS were developed. The models were statistically tested and verified by experimentation. This approach was then used to define the conditions for the preferential accumulation of liposomes in the top PEG-rich phase. The models predicted a significant effect of liposome surface charge, PEG molecular weight, phase-forming polymer concentration, and phosphate ion concentration on the partition behavior of liposomes. For negatively charged liposomes, it was found that the smaller the molecular weight of PEG and polymer concentration and the larger the phosphate ion concentration, the greater the partition coefficient of the liposomes. No significant effect of pH, at the range of 6-8, on liposome partitioning was noted. This approach has led to the development of an optimal two-phase system where 90% of negatively charged liposomes accumulated in the PEG phase. In addition to the general scientific value of this research, it has a technological importance as ATPSs may be useful for removing the unentrapped drug from liposomes during their preparation for pharmaceutical applications. (c) 1996 John Wiley & Sons, Inc.     

Aspergillus oryzae alpha-amylase partition in potassium phosphate-polyethylene glycol aqueous two-phase systems

The aim of this work is to study the partitioning of alpha-amylase from Aspergillus oryzae in polyethylene glycol-potassium phosphate systems formed by polymers of different molecular masses with different total concentrations, several NaCl concentrations and different volume ratio between the phases and at different temperatures. The enzyme was partitioned towards the top phase in the 2000-molecular-mass polyethylene glycol systems and towards the bottom phase in the other systems analyzed with higher molecular mass. The protein-medium interaction parameter (A) was determined; it increased in the same way as PEG molecular mass. The enthalpic and entropic changes found, in general, were negative and were shown to be associated by an entropic-enthalpic compensation effect suggesting that the ordered water structure in the chain of polyetyleneglycol plays a role in protein partition. The recovery in each of the phases was calculated in order to choose the best systems to be applied to enzyme isolation either from a polymer-rich or a polymer-poor phase.Enzymatic activity, circular dichroism and fluorescence were studied for the protein alone and in the presence of the different phases of the aqueous two-phase systems (ATPSs) in order to understand how they affect the enzymatic structure and the role of the protein-polymer interaction in the partitioning process. Secondary structure is not affected, in general, by the presence of the phases that do affect the enzymatic activity; therefore, there should be a change in the tertiary structure in the enzyme active site. These changes are more important for PEG 8000 than for PEG 2000 systems according to the results of the quenching of the intrinsic fluorescence. In a bio-separation process, the A. oryzae alpha-amylase could be isolated with ATPSs PEG 2000/Pi or PEG 8000/Pi with a high recovery, in the top or bottom phases, respectively.     

Distribution of cells between solid/liquid and liquid/liquid interfaces

The use of aqueous two-phase systems (ATPSs) and each system's individual phase-forming species to prevent Streptococcus sanguis attachment onto hydroxyapatite discs was explored. The strategy that we followed was to attach the cells to a solid surface in the presence of an additional interface. Conditions under which, simultaneously, the phase-forming species form two phases and the cells proliferate were identified. Growth curves were constructed in the presence of various polymers and salts commonly used to prepare ATPSs. Several aqueous two-phase systems were selected such that bacterial growth was comparable to that observed in pure medium. Cells were allowed to attach to hydroxyapatite discs for 7 days in the presence of varying concentrations of media, media with polymer, media with salt, and media with ATPS. Streptococcus sanguis attachment to the disks was evaluated by scanning electron microscopy. The addition of a PEG/Na(2)SO(4) ATPS to high concentrations of yeast-tryptone (YT) media (>65%) and of a PEG/MgSO(4) ATPS to nutrient-limited media reduces surface coverage of S. sanguis to less than 10%. Comparison of the attachment levels for the systems containing PEG/Na(2)SO(4) to media containing the individual phase-forming species and to the YT reference systems indicated that nutrient availability did not affect attachment.     

Effects of low urea concentrations on protein-water interactions

Solvent properties of aqueous media (dipolarity/polarizability, hydrogen bond donor acidity, and hydrogen bond acceptor basicity) were measured in the coexisting phases of Dextran–PEG aqueous two-phase systems (ATPSs) containing .5 and 2.0 M urea. The differences between the electrostatic and hydrophobic properties of the phases in the ATPSs were quantified by analysis of partitioning of the homologous series of sodium salts of dinitrophenylated amino acids with aliphatic alkyl side chains. Furthermore, partitioning of eleven different proteins in the ATPSs was studied. The analysis of protein partition behavior in a set of ATPSs with protective osmolytes (sorbitol, sucrose, trehalose, and TMAO) at the concentration of .5 M, in osmolyte-free ATPS, and in ATPSs with .5 or 2.0 M urea in terms of the solvent properties of the phases was performed. The results show unambiguously that even at the urea concentration of .5 M, this denaturant affects partitioning of all proteins (except concanavalin A) through direct urea–protein interactions and via its effect on the solvent properties of the media. The direct urea–protein interactions seem to prevail over the urea effects on the solvent properties of water at the concentration of .5 M urea and appear to be completely dominant at 2.0 M urea concentration.     

Cutinase purification on poly(ethylene glycol)–hydroxypropyl starch aqueous two-phase systems

The partition behaviour of cutinase on poly(ethylene glycol) (PEG)–hydroxypropyl starch aqueous two-phase systems was characterized. The effect of molecular mass of PEG, the pH of the system and tie-line length on cutinase partition coefficient and cutinase yield to the top phase was investigated for systems prepared with a purified hydroxypropyl starch (Reppal PES 100) and a crude one (HPS). The effect of the presence of different salts, such as sodium chloride, sodium sulphate and ammonium sulphate, on cutinase partition was also studied. The results lead to the conclusion that aqueous two-phase systems composed of PEG and hydroxypropyl starch are not efficient in the purification of cutinase. In the majority of cases, the partition coefficients were very close to 1, with pH being the factor which affects most cutinase partition. Partition coefficients were significantly improved when salts were added to the systems. For PEG 4000–Reppal PES 100 [at pH 4.0; 0.5 M (NH₄)₂SO₄], the partition coefficient for cutinase was 3.7, while a value of 12 was obtained for PEG 4000–HPS (at pH 4.0; 1 M NaCl). An isoelectric point (pI) of 7.8 was confirmed for cutinase by constructing a cross partition graphic from the results obtained in the experiments with different salts.     

An aqueous hydroxypropylstarch-poly(ethylene glycol) two-phase system for extraction of alpha-lactalbumin and beta-lactoglobulin from bovine whey.

The partitioning of alpha-lactalbumin and beta-lactoglobulin from bovine whey has been studied in an aqueous poly(ethylene glycol) (PEG)-hydroxypropylstarch two-phase system. The influence of several parameters including concentrations of polymers, sodium phosphate buffer, KSCN, and of PEG palmitate, with and without the presence of Ca2+, on the partitioning of the proteins has been investigated. The separation of the two proteins was demonstrated by counter-current distribution. A purification procedure for both proteins has been developed by using PEG-hydroxypropylstarch two-phase system. This system is compared with the more costly standard system based on PEG and dextran. The possible use of the aqueous two-phase systems for batch extraction for large scale purification of these whey proteins is discussed.     

Xylanase mass transfer studies in aqueous two-phase systems using spray and sieve plate columns

Aqueous two-phase systems (ATPSs) have long been used for biomolecule partitioning; these systems offer the possibility of using continuous or semicontinuous extraction processes. They require relatively simple equipment like spray or sieve plate columns that can be adapted for use in ATPSs. The aim of this work was to study the semicontinuous extraction of a model enzyme, xylanase, in spray and sieve plate columns, since, unlike centrifugal contactors, the cost of construction and maintenance of this equipment is low and it is easy to operate. For the spray column, the dispersed phase hold-up and overall mass transfer coefficients K(D) a were evaluated for different column heights and for different superficial velocities of the dispersed phase (light phase). Results indicated that an increase in superficial velocity in the range of 0-0.18 mm/s of the dispersed phase had a positive effect on K(D) a and on hold-up in all column heights studied, 75, 161 and 246 mm. For the same superficial velocity of the dispersed phase, the larger the hold-up was, the shorter the column. For the sieve plate column, the effects of the superficial velocity of the dispersed phase and the number of plates were also studied. Results showed that the K(D) a and hold-up increased with an increase in both parameters. The selectivity of separation of xylanase and BSA (model contaminant) was very high, since 60% of the enzyme was extracted in the light phase, whereas no significant amount of BSA was extracted. The possibility of using the sieve plate column in continuous operation for enzyme extraction was studied because previous work had only addressed the semicontinuous extraction of enzyme. The residence time distribution of the PEG phase using different superficial velocities of the salt phase was studied in continuous operation. The time required to reach the steady state was 40 min, and 70% of the xylanase was recovered. It was found that the Modified Power Spline software was well adjusted to the experimental results.     

Extractive partition of L-aspartase and fumarase fromEscherichia coli using aqueous polyethylene glycol-ammonium sulfate systems

Summary Inorganic sulfate salts are used to form aqueous two-phase systems with polyethylene glycol (PEG) for enzyme purification. Two enzymes, L-aspartase and fumarase produced byEscherichia coli are efficiently separated into different phases in spite of the high degree of similarity in molecular weight and amino acid sequence between them. The ratio of L-aspartase to fumarase in the PEG-rich phase is more than sixty (60) times the ratio before extraction. A high degree of purification in a single extraction step can be achieved by careful selections of PEG molecular weight, pH, cation of the salts, and sodium chloride levels. Cations of sulfate-containing salts in the following order: NH ₄ ⁺ >Na⁺>Mg²⁺ tend to increase the partition of L-aspartase in the PEG-rich phase. The maximal degree of enzyme purification is obtained by using PEG 4000 and ammonium sulfate as a phase system at a stable pH for both enzymes.     

螺旋槽圆盘柱高速逆流色谱及其在多肽和蛋白分离中的应用

本研究重点考察了实验室自行设计研制的J型螺旋槽圆盘柱逆流色谱系统对正丁醇-醋酸-水体系和聚乙二醇(PEG1000)-磷酸盐-水双水相体系的固定相保留能力,并研究了流动相流速(F)、柱转速(w)和温度(T)等因素对固定相保留率(Sf)的影响。结果表明,该新型分离柱可使两种溶剂体系在L-I-T、U-O-H和L-I-H三种洗脱模式下都可获得较高的Sf,即以下相为流动相,采用由螺旋槽内端(I)向外端(O)的流通方式,或以上相为流动相,采用由螺旋槽外端(O)向内端(I)的流通方式可以获得较高的固定相保留。其保留能力较传统的螺旋管逆流色谱柱有显著提高。Sf随着w的增加而升高,随着F的增加而降低,且Sf与F1/2/w线性相关。20oC～45oC之间温度对Sf影响不明显,但低于20oC不利于双水相体系的保留。应用研究表明,采用正丁醇-醋酸-水(4:1:5,V/V/V)和PEG1000-磷酸钾盐-水(12.5:12.5:75,W/W/W)(pH9.0)体系可以在较高的流动相流速和较高的固定相保留下分别实现对亮氨酸-酪氨酸(Leu-Tyr)和缬氨酸-酪氨酸(Val-Tyr)二肽混合物、细胞色素C与肌红蛋白混合物、肌红蛋白与溶菌酶...     

Extractive fermentation of clavulanic acid by Streptomyces DAUFPE 3060 using aqueous two-phase system

The influence of four variables, specifically PEG molar mass (400, 1,000, and 8,000 g/mol), concentrations of PEG and phosphate salts (15, 20, and 25% for both), and agitation intensity (110, 150, and 200 rpm), on clavulanic acid (CA) extraction by extractive fermentation with PEG/phosphate salts aqueous two-phase system was investigated in shaken flasks using a 2(4-1) -fractional factorial design. After selection of the two most significant variables (agitation intensity and PEG molar mass), an optimization study conducted according to a 2(2) -central composite design revealed that 25% PEG 8,000 g/mol and phosphate salts at 240 rpm (run 6) were the best conditions for the extractive fermentation, leading to the best results in terms of partition coefficient (k = 8.2), yield of CA in the PEG-rich phase (η(T) = 93%) and productivity (P = 5.3 mg/Lh). As a first attempt to make a scale-up of these results, the effectiveness of the extractive fermentation was then checked in a bench-scale bioreactor under conditions as close as possible to the optimum ones determined in flasks. The highest CA concentration obtained in the PEG-rich phase (691 mg/L) was 30% higher than in flasks, thus demonstrating the potential of such a new process, integrating the production and extraction steps, as a promising, low-cost tool to obtain high yields of this and similar products.     

Compatibilization effect of poly(epsilon-caprolactone)-b-poly(ethylene glycol) block copolymers and phase morphology analysis in immiscible poly(lactide)/poly(epsilon-caprolactone) blends

The miscibility and phase behavior of two stereoisomer forms of poly(lactide) (PLA: poly (L-lactide) (PLLA) and poly(DL-lactide) (PDLLA)) blends with poly(epsilon-caprolactone)-b-poly(ethylene glycol) (PCL-b-PEG) and PCL-b-monomethoxy-PEG (PCL-b-MPEG) block copolymers have been investigated by differential scanning calorimetry (DSC). The DSC thermal behavior of both the blend systems revealed that PLA is miscible with the PEG segment phase of PCL-b-(M)PEG but is still immiscible with its PCL segment phase although PCL was block-copolymerized with PEG. On the basis of these results, PCL-b-PEG was added as a compatibilizer to PLA/PCL binary blends. The improvement in mechanical properties of PLA/PCL blends was achieved as anticipated upon the addition of PCL-b-PEG. In addition, atomic force microscopy (AFM) measurements have been performed in order to study the compositional synergism to be observed in mechanical tests. AFM observations of the morphological dependency on blend composition indicate that PLA/PCL blends are immiscible but compatible to some extent and that synergism of compatibilizing may be maximized in the compositional blend ratio before apparent phase separation and coarsening.     

Extractive fermentation for enhanced gellan-hydrolysing enzyme production by Bacillus thuringiensis H14

A new extractive fermentation process using PEG and potassium phosphate aqueous two-phase system (ATPS) was developed for enhanced production of gellan-hydrolysing enzyme by Bacillus thuringiensis H14. Five different Bacillus sp. were tested for their ability to synthesize gellan-hydrolysing enzyme. Bacillus thuringiensis H14 was found to be the best organism for gellan-hydrolysing enzyme production. The enzyme showed maximum activity at pH 7.5 and 40 °C. The partition studies of gellan-hydrolysing enzyme in the system using PEG X (X = 9000, 6000, 4000) and potassium phosphate–water and PEG–sodium citrate–water system indicated at PEG (4000)– potassium phosphate–water is the best system for partitioning of gellan-hydrolysing enzyme into the PEG phase (K = 4.99). Gellan-hydrolysing enzyme production by Bacillus thuringiensis H14 was studied in ATPSs composed of PEG X (X = 9000, 6000, 4000) and potassium phosphate. The top phase is continuous and rich in PEG while the bottom phase is dispersed and is rich in phosphate, microbial cells being mainly retained in the bottom phase. The gellan-hydrolysing enzyme produced during fermentation partitioned into the upper PEG phase and total gellan-hydrolysing enzyme produced was 2.12, 2.29 and 2.40 times higher than that of homogeneous fermentation when the fermentations were carried out using PEG 9000–potassium phosphate–water, PEG 6000–potassium phosphate–water, PEG 4000–potassium phosphate–water systems respectively.     

Influence of partition parameters on a recombinant antigen of Schistosoma mansoni expressed on E. coli using poly(ethylene glycol)–hydroxypropyl starch aqueous two-phase system

This work describes the partition of a Schistosoma mansoni tegumental antigen produced by a recombinant Escherichia coli strain using an aqueous two-phase system (ATPS) composed of polyethylene glycol (PEG) and purified hydroxypropyl-starch (Reppal PES 100). The effects of the polymer molecular weight, tie line length and pH on antigen partitioning were investigated. The detection of the antigen in both phases was determined by ELISA. The system composed of PEG 8000 (5.1% w/w) and Reppal PES 100 (13.0% w/w) led to a yield of 92% and a purification factor of 12 concerning the antigen in the PEG-rich phase. It was observed that antigen partition in ATPSs was strongly affected by the pH and tie line length. In addition, it was possible in a single step, to remove the cell debris, which precipitated at the interface of the system.     

Isolation of a Aspergillus niger lipase from a solid culture medium with aqueous two-phase systems

The aim of this work is to find the best conditions to isolate lipase from a solid culture medium of Aspergillus niger NRRL3 strains using aqueous two-phase systems formed with polyethylene glycol and potassium phosphate or polyethylene glycol and sodium citrate. We studied the partitioning of a commercial lyophilizate from A. niger. Also, the lipase enzymatic activity was studied in all the phases of the systems and the results indicate that citrate anion increases lipase activity. An analysis by fluorescence spectroscopy of the interaction between lipase and the bottom and top phases of the systems shows that the protein tryptophan-environments are modified by the presence of PEG and salts. Separation of the enzyme from the rest of the proteins that make up the lyophilized was achieved with good yield and separation factor by ATPS formed by PEG 1000/Pi at pH 7, PEG 2000/Ci at pH 5.2 and PEG 4000/Ci at pH 5.2. The above mentioned systems were used in order to isolate extracellular lipase from a strain of A. niger in submerged culture and solid culture. The best system for solid culture, with high purification factor (30.50), is the PEG 4000/Ci at pH 5.2. The enzyme was produced in a solid culture medium whose production is simple and recovered in a phase poor in polymer, bottom phase. An additional advantage is that the citrate produces less pollution than the phosphate. This methodology could be used as a first step for the isolation of the extracellular lipase from A. niger.     

The potential application of aqueous two-phase systems for in situ recovery of 6-pentyl-infinity-pyrone produced by Trichoderma harzianum

Commercial production of aroma compounds by de novo microbial biosynthesis has been principally limited by the low productivity so far achieved. Production of 6-pentyl-alpha-pyrone (6PP), a coconut-like aroma compound, by Trichoderma harzianum has been limited by the toxic effect that occurs even at low concentration (<100 ppm). This work evaluated the feasibility of the use of aqueous-two phase systems (ATPS), as in situ extraction systems, in order to overcome the toxic effects of 6PP and to improve culture productivity. The partition behaviour of 6-pentyl-alpha-pyrone and Trichoderma harzianum mycelium in polyethylene glycol (PEG)-salt and PEG-dextran two-phase systems was investigated and it is reported for the first time. The evaluation of system parameters such as PEG molecular mass, concentration of PEG as well as salt, volume ratio (Vr) and dextran molecular mass, was carried out to determine under which conditions the 6PP partitions to the opposite phase that mycelium does. PEG-dextran systems proved to be unsuitable for the in situ recovery of 6PP because either 6PP and biomass partitioned to the same phase or a large extraction phase was required for the process. ATPS extraction comprising Vr = 0.26, PEG 1450 (7.2% w/w) and sulphate (16.6% w/w) provided the best conditions for the maximum accumulation of the biomass into the bottom phase and concentrated the 6PP in the opposite phase (i.e. 86% of biomass and 56% of 6PP of the total amount loaded from the fermentation extract into the ATPS) for ex situ bioseparation. However, this system caused complete inhibition of the growth of the microorganism during the in situ bioseparation, probably as a consequence of the high ionic strength resulting from the salt concentration. Consequently, two ATPS PEG 8000-sulphate (12%/7% and 6%/14%) were evaluated and proved to be more suitable in the potential application for the in situ recovery of 6PP.     

Application of an aqueous two‐phase systems high‐throughput screening method to evaluate mAb HCP separation

Aqueous two‐phase systems (ATPSs) as separation technique have regained substantial interest from the biotech industry. Biopharmaceutical companies faced with increasing product titers and stiffening economic competition reconsider ATPS as an alternative to chromatography. As the implementation of an ATPS is material, time, and labor intensive, a miniaturized and automated screening process would be beneficial. In this article such a method, its statistical evaluation, and its application to a biopharmaceutical separation task are shown. To speed up early stage ATPS profiling an automated application of the cloud‐point method for binodal determination was developed. PEG4000–PO₄ binodals were measured automatically and manually and were found to be identical within the experimental error. The ATPS screening procedure was applied to a model system and an industrial separation task. PEG4000–PO₄ systems at a protein concentration of 0.75 mg/mL were used. The influence of pH, NaCl addition, and tie line length was investigated. Lysozyme as model protein, two monoclonal antibodies, and a host cell protein pool were used. The method was found to yield partition coefficients identical to manually determined values for lysozyme. The monoclonal antibodies were shifted from the bottom into the upper phase by addition of NaCl. This shift occurred at lower NaCl concentration when the pH of the system was closer to the pI of the distributed protein. Addition of NaCl, increase in PEG4000 concentration and pH led to significant loss of the mAb due to precipitation. Capacity limitations of these systems were thus demonstrated. The chosen model systems allowed a reduction of up to 50% HCP with a recovery of greater than 95% of the target proteins. As these values might not be industrially relevant when compared to current chromatographic procedures, the developed screening procedure allows a fast evaluation of more suitable and optimized ATPS system for a given task. Biotechnol. Bioeng. 2011; 108:69–81. © 2010 Wiley Periodicals, Inc.     

Correlations for the partition behavior of proteins in aqueous two-phase systems: effect of overall protein concentration

The effect of protein concentration in partitioning in PEG/salt aqueous two-phase systems has been investigated. PEG 4000/phosphate systems in the presence of 0% w/w and 8.8% w/w NaCl have been evaluated using amyloglucosidase, subtilisin, and trypsin inhibitor. Also, a PEG 4000/phosphate system with 3% w/w NaCl was used for alpha-amylase. The concentration of the protein in each of the phases affected its partition behavior. The pattern for the individual proteins was dependent on their physicochemical properties. In the top phase, maximum protein concentration was determined mainly by a steric exclusion effect of PEG, and hydrophobic interaction between PEG and proteins. In the bottom phase, maximum concentration was determined mainly by a salting-out effect of the salts present. As the ionic strength was increased in the systems the concentration in the top phase increased for all proteins. In the bottom phase an increase in ionic strength increased the salting-out effect. Amyloglucosidase had a very low maximum concentration in the PEG-rich top phase which was probably due to its large size (steric exclusion) and low hydrophobicity, and a high concentration in the salt-rich bottom phase due to its high hydrophilicity. In the case of subtilisin and trypsin inhibitor, their high concentrations in the top phase were due to their hydrophobic nature (hydrophobic interaction with PEG) and small size (negligible steric exclusion). The maximum concentration in the bottom phase for trypsin inhibitor was lower than that of subtilisin which was probably due to its higher hydrophobicity and, hence, a stronger salting-out effect. The protein concentration in each of the two phases was correlated with a "saturation"-type equation. The partition coefficient could be satisfactorily predicted, as a function of the overall protein concentration, by the ratio between the "saturation" equations of the two individual phases. Better correlations were obtained when an empirical sigmoidal Boltzmann equation was fitted to the data, since in virtually all cases the partition coefficient is constant at low protein concentration (true partitioning) and changes to a different constant value at a high overall protein concentration. (c) 1996 John Wiley & Sons, Inc.     

Hydrodynamics and mass transfer in aqueous two-phase protein extraction using a continuous perforated rotating disc contactor

A continuous perforated rotating disc contactor was used to extract bovine serum albumin (BSA) with aqueous two-phase systems based on polyethylene glycol (PEG) and phosphate salts. The dispersed phase holdup and mass transfer coefficient were determined. It was found that the dispersed phase holdup increased with increasing PEG phase velocity. The overall mass transfer coefficient for BSA was independent of the PEG phase velocity.