On protein partitioning in two-phase aqueous polymer systems.

The partitioning of proteins between the coexisting phases of two-phase aqueous polymer systems reflects an intricate and delicate balance of interactions between proteins, polymers, salts and water. Experimental investigations have suggested that a large number of factors influence protein partitioning, including the types of polymers, their molecular weight and concentration; the protein sizes, conformation and composition; salt type and concentration, and solution pH; and the presence of ligands attached to the polymer which may interact with surface sites of the protein. Complementary modelling attempts have been successful in illuminating several molecular-level mechanisms influencing protein partitioning using lattice-model techniques, viral expansions and a scaling-thermodynamic approach. In spite of these experimental and modelling approaches, many of the physical phenomena associated with these complex systems are not well understood. Notably, the precise nature of the protein-polymer interactions and the potent effect of inorganic salts on the partitioning of proteins in these systems remains poorly understood.     

Analysis of protein association by partitioning in aqueous two-phase polymer systems: Applications to the tetramer-dimer dissociation of hemoglobin

A new simple and rapid method for the determination of protein-protein association constants is described. By maximizing experimental conditions in which size becomes the controlling variable, analysis of the effect of protein concentration on the partitioning behavior of proteins in aqueous two-phase polymer systems permits an accurate estimate of protein association constants. When employed to investigate the tetramer-dimer dissociation of human oxy- and methemoglobin in the presence and absence of high salt concentration, values for the dissociation constant are obtained that are consistent with those obtained by other methods.     

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.     

Three phase partitioning of carbohydrate polymers: separation and purification of alginates

Three phase partitioning, a technique described for protein purification, has been employed for precipitation and purification of three different commercial preparations of alginates. Three phase partitioning works by the addition of t-butanol to aqueous solution of the polymer containing 20–30% ammonium sulphate (w/v). Three phases formed are: upper t-butanol layer, interfacial polymer precipitate and lower aqueous phase. In all the three cases, the process optimization was carried out by varying ammonium sulphate concentration, volume of t-butanol, alginate concentration and temperature. Fluorescence spectroscopy was used to show that repeated cycles of TPP also resulted in considerable reduction in polyphenol content of a crude alginate preparation.     

Extracellular enzyme loss during polyelectrolyte flocculation of cells from fermentation broth

Association of extracellular protein product with flocculated cells reduces product yield. Here, partitioning of the enzyme subtilisin between the liquid and polyelectrolyte-flocculated and sedimented Bacillus increased as the polymer dosage was increased beyond that necessary to obtain optimum floc character (brain floc) for cell removal by centrifugation. Partitioning to the cell floc is partly physical entrapment at all polymer dosages; however, at higher levels there is also direct interaction between the polyelectrolyte and enzyme. Enzyme loss was not likely due to pH denaturation during the flocculation process because conditions were within the stable pH range of the enzyme. The direct interaction between polyelectrolyte and enzyme was characterized through turbidimetric titrations and partitioning studies. Neither changes in the polymer feed concentration nor the method of polymer addition reduced the enzyme loss at dosages optimal for cell removal.     

Effect of salt additives on protein partition in polyethylene glycol–sodium sulfate aqueous two-phase systems

Partitioning of 15 proteins in polyethylene glycol (PEG)–sodium sulfate aqueous two-phase systems (ATPS) formed by PEG of two different molecular weights, PEG-600 and PEG-8000 in the presence of different buffers at pH 7.4 was studied. The effect of two salt additives (NaCl and NaSCN) on the protein partition behavior was examined. The salt effects on protein partitioning were analyzed by using the Collander solvent regression relationship between the proteins partition coefficients in ATPS with and without salt additives. The results obtained show that the concentration of buffer as well as the presence and concentration of salt additives affects the protein partition behavior. Analysis of ATPS in terms of the differences between the relative hydrophobicity and electrostatic properties of the phases does not explain the protein partition behavior. The differences between protein partitioning in PEG-600–salt and PEG-8000–salt ATPS cannot be explained by the protein size or polymer excluded volume effect. It is suggested that the protein–ion and protein–solvent interactions in the phases of ATPS are primarily important for protein partitioning.     

Recovery of endo-polygalacturonase using polyethylene glycol-salt aqueous two-phase extraction with polymer recycling

The partitioning behaviour of endo-polygalacturonase (endo-PG) and total protein from a clarified Kluyveromyces marxianus fermentation broth in polyethylene glycol (PEG)-ammonium sulfate and PEG-potassium phosphate (pH=7) aqueous two-phase systems was experimentally investigated. Both the enzyme and total protein partitioned in the bottom phase for these two kinds of systems. The enzyme partitioning coefficient can be lower than 0.01 in PEG8000-(NH₄)₂SO₄ ATPS with a large phase volume ratio and a moderate tie-line length, which implies the possibility of concentration operation using aqueous two phase partitioning. An ion-exchange separation of high purification efficiency was applied to analyze the clarified and dialyzed fermentation broth. A total purification factor of only 2.3 was obtained, which indicated the high enzyme protein content in the total protein of the fermentation broth. Consequently, the main purpose for separating endo-PG is concentration rather than purification. A separation scheme using an aqueous two-phase extraction process with polymer recycling and a dialysis was proposed to recover endo-PG from the fermentation supernatant of K. marxianus for commercial purpose. A high enzyme recovery up to 95% and a concentration factor of 5 to 8 with a purification factor of about 1.25 were obtained using the single aqueous two-phase extraction process. More than 95% polymer recycled will not affect the enzyme recovery and purification factor. Dialysis was used mainly to remove salts in the bottom phase. The dialysis step has no enzyme loss and can further remove small bulk proteins. The total purification factor for the scheme is about 1.7.     

Thermoseparating water/polymer system: a novel one-polymer aqueous two-phase system for protein purification

In this study we show that proteins can be partitioned and separated in a novel aqueous two-phase system composed of only one polymer in water solution. This system represents an attractive alternative to traditional two-phase systems which uses either two polymers (e.g., PEG/dextran) or one polymer in high-salt concentration (e.g., PEG/salt). The polymer in the new system is a linear random copolymer composed of ethylene oxide and propylene oxide groups which has been hydrophobically modified with myristyl groups (C(14)H(29)) at both ends (HM-EOPO). This polymer thermoseparates in water, with a cloud point at 14 degrees C. The HM-EOPO polymer forms an aqueous two-phase system with a top phase composed of almost 100% water and a bottom phase composed of 5-9% HM-EOPO in water when separated at 17-30 degrees C. The copolymer is self-associating and forms micellar-like structures with a CMC at 12 microM (0.01%). The partitioning behavior of three proteins (lysozyme, bovine serum albumin, and apolipoprotein A-1) in water/HM-EOPO two-phase systems has been studied, as well as the effect of various ions, pH, and temperature on protein partitioning. The amphiphilic protein apolipoprotein A-1 was strongly partitioned to the HM-EOPO-rich phase within a broad-temperature range. The partitioning of hydrophobic proteins can be directed with addition of salt. Below the isoelectric point (pI) BSA was partitioned to the HM-EOPO-rich phase and above the pI to the water phase when NaClO(4)was added to the system. Lysozyme was directed to the HM-EOPO phase with NaClO(4), and to the water phase with Na-phosphate. The possibility to direct protein partitioning between water and copolymer phases shows that this system can be used for protein separations. This was tested on purification of apolipoprotein A-1 from human plasma and Escherichia coli extract. Apolipoprotein A-1 could be recovered in the HM-EOPO-rich phase and the majority of contaminating proteins in the water phase. By adding a new water/buffer phase at higher pH and with 100 mM NaClO(4), and raising the temperature for separation, the apolipoprotein A-1 could be back-extracted from the HM-EOPO phase into the new water phase. This novel system has a strong potential for use in biotechnical extractions as it uses only one polymer and can be operated at moderate temperatures and salt concentrations and furthermore, the copolymer can be recovered.     

Partitioning of peptide-tagged proteins in aqueous two-phase systems using hydrophobically modified micelle-forming thermoseparating polymer

Genetic engineering has been used to construct hydrophobically modified fusion proteins of cutinase from Fusarium solani pisi and tryptophan-containing peptides. The aim was to enhance the partitioning of the tagged protein in a novel aqueous two-phase system formed by only one water-soluble polymer. The system was based on a hydrophobically modified random copolymer of ethylene oxide (EO) and propylene oxide (PO) units, HM-EOPO, with myristyl groups (C(14)H(29)) at both ends. The HM-EOPO polymer is strongly self-associating and has a lower critical solution temperature (cloud point) at 12 degrees C in water. At temperatures above the cloud point a two-phase system is formed with a water top phase and a polymer-enriched bottom phase. By adding a few percent of hydroxypropyl starch polymer, Reppal PES 200, to the system, it is possible to change the densities of the phases so the HM-EOPO-enriched phase becomes the top phase and Reppal-enriched phase is the bottom phase. Tryptophan-based peptides strongly preferred the HM-EOPO rich phase. The partitioning was increased with increasing length of the peptides. Full effect of the tag as calculated from peptide partitioning data was not found in the protein partitioning. When a short spacer was introduced between the protein and the tag the partitioning was increased, indicating a better exposure to the hydrophobic core of the polymer micelle. By adding a hydrophilic spacer between the protein and trp-tag, it was possible to increase the partitioning of cutinase 10 times compared to wild-type cutinase partitioning. By lowering the pH of the system and addition of NaCl, the partitioning of tagged protein was further increased towards the HM-EOPO phase. After isolating the HM-EOPO phase, the temperature was increased and the protein was back-extracted from the HM-EOPO phase to a fresh water phase.     

Genetically engineered charge modifications to enhance protein separation in aqueous two-phase systems: Charge directed partitioning

This report continues or examination of the effect of genetically engineered charge modifications on the partitioning behavior of proteins in aqueous two-phase extration. The genetic modifications consisted of the fusion of charged peptide tails to beta-galactosidase and charge-change point mutations to T4 lysozyme. Our previous article examined the influence of these charge modifications on partitioning as a function of interfacial potential difference. In this study, we examined charge directed partitioning behavior in PEG/dextran systems containing small amounts of the charged polymers diethylaminoethyl-dextran (DEAE-dextran) or dextran sulfate. The best results were obtained when attractive forces between the protein and polymer were present. Nearly 100% of the beta-galactosidase, which carries a net negative charge, partitioned to the DEAE-dextran-rich phase regardless of whether the phase was dextran or PEG. In these cases, cloudiness of the protein-rich phases suggest that strong charge interactions resulted in protein/polymer aggregation, which may have contributed to the extreme partitioning. Unlike the potentialdriven partitioning reported previously, consistent partitioning trends were observed as a result of the fusion tails, with observed shifts in partition coefficient (K(p)) of up to 37-fold. However, these changes could not be solely attributed to charge-based interactions. Similarly, T4 lysozyme, carrying a net positive charge, partitioned to the dextran sulfate-containing phase, and displayed four- to sevenfold shifts in K(p) as a result of the point mutations. These shifts were two to four times stronger than those observed for potential driven partitioning. Little effect on partitioning was observed when the protein and polymer had the same charge, with the exception of beta-galactosidase with polyarginine tails. The high positive charge density of these tails provided for a localized interaction with the dextran sulfate, and resulted in 2- to 15-fold shifts in K(p). (c) 1995 John Wiley & Sons, Inc.     

Partitioning of Proteins using a Hydrophobically Modified Ethylene Oxide/SDS Aqueous Two-phase System

Summary A novel aqueous two-phase system containing hydrophobically modified ethylene oxide (HM-EO) and sodium dodecyl sulphate (SDS) was developed to enhance the selectivity of protein partitioning in two phases. Phase diagrams of HM-EO/H₂O and HM-EO/SDS/H₂O were measured, and the mechanism of interaction between HM-EO polymer and the anionic surfactant sodium dodecyl sulphate (SDS) was also discussed. It was found that the improvement of selectivity of protein partitioning was related to the increase of electrostatic potential difference between the two phases because of the charged network formed by mixed micelles of HM-EO and SDS in the bottom phase. With bovine serum albumin (BSA) and lysozyme as model proteins, some factors, such as pH, SDS concentration, conductivity and temperature of the system, were investigated for the influences of protein partition in HM-EO/SDS/H₂O systems. The results showed that the addition of SDS not only changed the phase behaviour, but also played an important role in protein partitioning.     

Protein sorption and recovery by hydrogels using principles of aqueous two-phase extraction

Use of the thermodynamic principles of aqueous two-phase extraction (ATPE) to drive protein into a crosslinked gel is developed as a protein isolation and separation technique, and as a protein loading technique for drug delivery applications. A PEG/dextran gel system was chosen as a model system because PEG/dextran systems are widely used in aqueous two-phase extraction and dextran gels (Sephadex(R)) are common chromatographic media. The effects of polymer concentrations and molecular weights, salts, and pH on the partitioning of ovalbumin matched ATPE heuristics and data trends. Gel partition coefficients (Cgel/Csolution) increased with increasing PEG molecular weight and concentration and decreasing dextran concentration (increased gel swelling). The addition of PEG to the buffer solution yielded partition coefficients more than an order of magnitude greater than those obtained in systems with buffer alone, or added salt. A combined salt/PEG system yielded an additional order of magnitude increase. For example, when ovalbumin solution (2.3 mg/mL) was equilibrated with Sephadex(R) G-50 at pH 6.75, the partition coefficients were 0.13 in buffer, 0.11 in buffer with 0.22M KI, 2.3 in 12 wt% PEG-10,000 and 32.0 in 12 wt% PEG-10, 000 with 0.22M KI. The effect of anions and cations as well as ionic strength and pH on the partitioning of ovalbumin also matched ATPE heuristics. Using the heuristics established above, partition coefficients as high as 80 for bovine serum albumin and protein recoveries over 90% were achieved. In addition, the wide range of partition coefficients that were obtained for different proteins suggests the potential of the technique for separating proteins. Also, ovalbumin sorption capacities in dextran were as high as 450 mg/g dry polymer, and the sorption isotherms were linear over a broad protein concentration range.     

Protein partitioning in aqueous two-phase systems composed of a pH-responsive copolymer and poly(ethylene glycol)

The effect of pH and salt concentration on the partitioning behavior of bovine serum albumin (BSA) and cytochrome c in an aqueous two-phase polymer system containing a novel pH-responsive copolymer that mimics the structure of proteins and poly(ethylene glycol) (PEG) was investigated. The two-phase system has low viscosity. Depending on pH and salt concentration, the cytochrome c was found to preferentially partition into the pH-responsive copolymer-rich (bottom) phase under all conditions of pH and salt concentrations considered in the study. This was caused by the attraction between the positively charged protein and negatively charged copolymer. BSA partitioning showed a more complex behavior and partitioned either to the PEG phase or copolymer phase depending on the pH and ionic strength. Extremely high partitioning levels (partition coefficient of 0.004) and very high separation ratios of the two proteins (up to 48) were recorded in the new systems. This was attributed to strong electrostatic interactions between the proteins and the charged copolymer.     

Stathmin Regulates Centrosomal Nucleation of Microtubules and Tubulin Dimer/Polymer Partitioning

Stathmin is a microtubule-destabilizing protein ubiquitously expressed in vertebrates and highly expressed in many cancers. In several cell types, stathmin regulates the partitioning of tubulin between unassembled and polymer forms, but the mechanism responsible for partitioning has not been determined. We examined stathmin function in two cell systems: mouse embryonic fibroblasts (MEFs) isolated from embryos +/+, +/−, and −/− for the stathmin gene and porcine kidney epithelial (LLCPK) cells expressing stathmin-cyan fluorescent protein (CFP) or injected with stathmin protein. In MEFs, the relative amount of stathmin corresponded to genotype, where cells heterozygous for stathmin expressed half as much stathmin mRNA and protein as wild-type cells. Reduction or loss of stathmin resulted in increased microtubule polymer but little change to microtubule dynamics at the cell periphery. Increased stathmin level in LLCPK cells, sufficient to reduce microtubule density, but allowing microtubules to remain at the cell periphery, also did not have a major impact on microtubule dynamics. In contrast, stathmin level had a significant effect on microtubule nucleation rate from centrosomes, where lower stathmin levels increased nucleation and higher stathmin levels reduced nucleation. The stathmin-dependent regulation of nucleation is only active in interphase; overexpression of stathmin-CFP did not impact metaphase microtubule nucleation rate in LLCPK cells and the number of astral microtubules was similar in stathmin +/+ and −/− MEFs. These data support a model in which stathmin functions in interphase to control the partitioning of tubulins between dimer and polymer pools by setting the number of microtubules per cell.     

Affinity partitioning of phosphofructokinase from baker's yeast using polymer-bound Cibacron blue F3G-A

1. Phosphofructokinase from baker's yeast is partitioned between the phases of an aqueous two-phase system, containing dextran (Mr = 500000) and poly(ethyleneglycol) (Mr = 6000), in favour of the dextran-rich phase. By covalent binding of the dye Cibacron blue F3G-A to poly(ethyleneglycol) the enzyme can be extracted to the phase rich in this polymer, i.e. affinity partitioning. 2. The affinity partitioning effect, measured as the logarithmic increase of the partition coefficient by introducing polymer-bound Cibacron blue, depends on several factors. The influence of dye-polymer concentration, polymer concentration, polymer molecular weight, kind of salt and salt concentration, pH and temperature has been studied. 3. The effect of ATP, ADP, AMP, ITP, fructose 1,6-bis-phosphate and fructose 6-phosphate show large differences in the binding strength of these substances to the Cibacron blue binding sites. AMP cannot compete with Cibacron blue while ATP is strongly competing. 4. The use of affinity partitioning for enzyme isolation and determination of ligand binding is discussed, as well as possible mechanisms concerning this type of liquid/liquid extraction.     

Features of the acid protease partition in aqueous two-phase systems of polyethylene glycol-phosphate: chymosin and pepsin

The partitioning of chymosin (from Aspergilus niger) and pepsin (from bovine stomach) was carried out in aqueous-two phase systems formed by polyethyleneglycol-potassium phosphate. The effects of polymer concentration, molecular mass and temperature were analysed. The partition was assayed at pH 7.0 in systems of polyethyleneglycol of molecular mass: 1450, 3350, 6000 and 8000. Both proteins showed high affinity for the polyethyleneglycol rich phase. The increase of polyethyleneglycol concentration favoured the protein transfer to the top phase, suggesting an important protein-polymer interaction. Polyethyleneglycol proved to have a stabilizing effect on the chymosin and pepsin, increasing its protein secondary structure. This finding agreed with the enhancement of the milk clotting activity by the polyethyleneglycol. The method appears to be suitable as a first step for the purification of these proteins from their natural sources.     

Partitioning of α-lactalbumin and β-lactoglobulin in aqueous two-phase systems of polyvinylpyrrolidone and potassium phosphate

In the present study, the partitioning of α-lactalbumin, β-lactoglobulin, and cheese whey proteins in aqueous two-phase system of polyvinylpyrrolidone-potassium phosphate is investigated. The partitioning of proteins in this system depends on the polymer and salt weight percents in feed, temperature, and pH. The orthogonal central composite design is used to study the effects of different parameters on partitioning of α-lactalbumin and β-lactoglobulin. A second order model is proposed to determine the impact of these parameters. The results of the model show that the weight percent of the salt in feed has a large effect on the protein partitioning. The weight percent of polyvinylpyrrolidone in the feed increases the partitioning coefficients. By increasing the temperature, the viscosity of polyvinylpyrrolidone is reduced and the protein can easily be transferred from one phase to the other phase. The pH of the aqueous two phase system can alter the protein partitioning coefficient through the variation of the protein net charge.     

Dye-affinity techniques for bioprocessing: Recent developments

Textile or triazine dyes play an important role as affinity ligands in protein purification. Each step of the protein purification protocol can be divided into three stages, partitioning between two phases, separation of these phases and recovery of the target protein from the enriched phase. Now developments in dye-affinity techniques are discussed emphasizing the innovations in all three stages of the protein purification process. Dye-affinity chromatography has become a routine step in protein purification. New dyes have been developed and used successfully in both traditional chromatographic mode and new modes like affinity precipitation, polymer aqueous two-phase partitioning or expanded bed chromatography. The specificity of dye techniques has been increased by both purposeful designing of new dyes and decreasing non-specific protein–dye interactions with polymer shielding. One can envisage further development and ramification of dye-affinity techniuqes in protein purification.     

Protein partitioning at the isoelectric point: influence of polymer molecular weight and concentration and protein size

We report the partition coefficient, K(p') at the isoelectric point of lysozyme, chymotrypsinogen A, albumin, transferrin, and catalase in 64 different polyethylene(PEG)/ dextran(Dx)/water systems. We study the trends of the partition coefficient with protein type, polymer concentration, and polymer molecular weight. We find that the partition coefficient decreases with increasing tie line length for lysozyme, albumin, transferrin, and catalase for which K(p) is less than 1, but increases for chymotrysinogen for which K(p) is larger than 1. The effect of the tie line length on the partition coefficient is larger for the large proteins than for the small proteins. The partition coefficient decreases with increasing protein molecular weight except for lysozyme suggesting that lysozyme is present as a dimer or a trimer. The partition coefficient decreases with increasing PEG molecular weight, but the magnitude of the increase is larger for the smaller PEG molecular eights and tends to level of at high PEG molecular weight. The partition coefficient increases with increasing dextran (Dx) molecular weight for chymotrypsinogen but decreases for catalase. The partition coefficients of lysozyme, albumin, and transferrin increase with increasing Dx molecular weight from Dx 10(4) to Dx 1.1 x 10(5) and then slightly decrease from Dx 1.1 x 10(5) to Dx 5 x 10(5). The experimental results are analyzed using a statistical thermodynamics model. The experimental results are analyzed using a statistical thermodynamics model. The experiments suggest that protein partitioning at the isoelectric point in aqueous two-phase systems is strongly related to the size of the proteins and polymers. Finally, the impossibility of obtaining data completely independent of polymer concentration is emphasized.     

3',5'-二磷酸核苷酸酶在亲和双水相胶束系统中分配行为研究

以高分子表面活性剂HM-EO为主成相剂,金属螯合表面活性剂Triton X-114-IDA-Cu(Ⅱ)(TX-Cu(Ⅱ))为辅成相剂,构建新型亲和双水相胶束系统(ATPMS)以提高目标产物的萃取选择性,并考察重组蛋白3',5'-二磷酸核苷酸酶(YND)在系统中分配行为。结果表明,系统中不含亲和配基时YND主要分配于胶束缺失相;随着亲和配基含量的增加,YND与TX-Cu(Ⅱ)亲和结合而逐渐分配到胶束富集相并且在系统中显示出优异的稳定性;调节溶液p H能够影响YND亲和分配,最适萃取条件为pH 9.0;增大无机盐浓度,导致更多杂蛋白分配到胶束缺失相,然而对YND分配影响较小。在2.5%HM-EO、0.125%TX-Cu(Ⅱ)、p H 9.0、50 mmol/L Na Cl条件下,实验获得65.8%的酶活回收率。因此亲和ATPMS可以有效用于对富组氨酸蛋白YND的分离纯化,为该体系在重组蛋白的分离纯化试验提供相应的基础依据。