Aqueous two-phase metal affinity extraction of heme proteins

An iminodiacetic acid derivative of poly(ethylene glycol) (PEG-IDA) that chelates metal cations has been synthesized and used to extract proteins in metal affinity aqueous two-phase PEG/dextran systems. With less than 1% of the PEG substituted with chelated copper, partition coefficients are shown to increase by factors of up to 37 over extraction with unsubstituted PEG. The proteins studied are preferentially extracted into the Cu(II)PEGIDA phase in proportion to the number of accessible histidine residues on their surface. The affinity contribution to partitioning is proportional to the number of exposed histidine over a very wide range. The partition coefficients of heme-containing proteins measured in the Cu(II)PEG-IDA/dextran systems increase with the pH of the extraction mixture from pH 5.5 to pH 8.0, while partition coefficients in the unsubstituted PEG/dextran systems are very nearly independent of pH. The strong pH dependence of the metalaffinity extraction can be utilized in the recovery of the extracted protein.     

A mathematical model for metal affinity protein partitioning

A mathematical model of metal affinity partitioning has been derived and used to describe protein partitioning in Cu (II)PEG/dextran systems. A working model has been extended to account for inhibition, which for metal affinity extraction is the inhibition of protein-metal binding by hydrogen ion. PEG/dextran partitioning experiments were performed on four proteins, tuna heart cytochrome c, Candida krusei cytochrome c, horse myoglobin, and sperm whale myoglobin. The partition coefficients for these proteins are increased by the addition of Cu (II)PEG-IDA, due to the affinity between the chelated copper atom and metal-coordinating histidine residues on the protein surface. The results of experiments to determine the effects of the number of binding sites on the protein, the copper concentration, and pH on partitioning are all well-described by the mathematical model. The pK(a) value of the metal binding site was determined to be 6.5, which is in the range of pK(a) values commonly observed for surface histidines. The average association constant for the binding of Cu (II)PEG-IDA to accessible histidines was found to be 4.5 x 10(3). This value is comparable to stability constants measured by conventional potentiometry techniques for analogous small complexes.     

Optimization of bovine serum albumin sorption and recovery by hydrogels

Aqueous two-phase systems are composed of aqueous solutions of either two water-soluble polymers, usually polyethylene glycol (PEG) and dextran (Dx), or a polymer and a salt, usually PEG and phosphate or sulfate. Partitioning of proteins in such systems provides a powerful method for separating and purifying mixtures of biomolecules by extraction. If one of the phase forming polymers is a crosslinked gel, then the solution-controlled gel sorption may be considered as a modification of aqueous two-phase extraction. Since PEG/dextran systems are widely used in aqueous two-phase extraction and dextran gels (Sephadex) are common chromatographic media, we choose a PEG/dextran gel system as a model system in this study. The partitioning behavior of pure bovine serum albumin (BSA) in PEG/dextran gel systems is investigated to see the effects of variations in PEG and NaCl concentrations on the partition coefficient K. By making use of the Box-Wilson experimental design, K is shown to be maximized at 9.8 (%, w/w) PEG and 0.2 M NaCl concentrations, respectively, as 182.     

Enhanced metal-affinity partitioning of genetically engineered hirudin variants in polyethylene glycol/dextran two-phase systems

Hirudin variants were constructed to exhibit an increased metal-binding affinity in an attempt to apply a metal-affinity partitioning process in a primary separation step for purification of hirudin. The hirudin variants were genetically engineered to contain additional surface-accessible histidines and produced by recombinant Saccharomyces cerevisiae. The partitioning behavior of these variants was compared with that of the wild type with a single surface-accessible histidine at position 51. Upon the addition of a small amount of Cu(II)IDA-PEG (Cu(II)iminodiacetic acid-polyethylene glycol) ligand to PEG/dextran two-phase systems, the hirudin variants with two or three surface-accessible histidines were more selectively partitioned into the PEG-rich phase than the wild type. Integrating protein engineering to metal-affinity partitioning offers the potential for general application of this technique to facilitate protein isolation, but the genetically engineered protein variants should be carefully constructed in a manner to minimize reduction of native protein activity.     

Mutation of surface-exposed histidine residues of recombinant human granulocyte-colony stimulating factor (Cys17Ser) impacts on interaction with chelated metal ions and refolding in aqueous two-phase systems

Site directed mutagenesis of Cys17-->Ser17 form of recombinant human granulocyte colony stimulating factor (rhG-CSF C17S) for sequential replacing of surface His(43) and His(52) with alanine was used to identify residues critical for the protein interaction with metal ions, in particular Ni(2+) chelated by dye Light Resistant Yellow 2 KT (LR Yellow 2KT)-polyethyleneglycol (PEG), and refolding after partitioning of inclusion bodies in aqueous two-phase systems. Strong binding of rhG-CSF (C17S) to PEG-LR Yellow 2KT-Cu(II) complex allowed for the adoption of affinity chromatography on Sepharose-LR Yellow 2KT-Cu(II) that appeared to be essential for the rapid isolation of mutated forms of rhG-CSF. Efficiency of that purification stage is exemplified by isolation of rhG-CSF (C17S, H43A) and rhG-CSF (C17S, H43A, H52A) mutants in correctly folded and highly purified state. Affinity partitioning of rhG-CSF histidine mutants was studied in aqueous two-phase systems containing Cu(II), Ni(II) and Hg(II) chelated by LR Yellow 2KT-PEG at pH 7.0 and Cu(II)-at pH 5.0. It was determined, that affinity of rhG-CSF mutants for metal ions decreased in the order of C17S>C17S, H43A>C17S, H43A, H52A for Cu(II), and C17S=C17S, H43A>C17S, H43A, H52A for Ni(II) ions, while affinity of all rhG-CSF mutants for Hg(II) ions was of the same order of magnitude. Influence of His(43) and His(52) mutation on protein refolding was studied by partitioning of the respective inclusion body extract in aqueous two-phase systems containing Ni(II) and Hg(II) ions. Data on rhG-CSF histidine mutant partitioning and refolding indicated, that His(52) mutation is crucial for the strength of protein interaction with chelated Ni(II) ions and refolding efficiency.     

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.     

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.     

Metal affinity extraction of human hemoglobin in an aqueous polyethylene glycol-sodium sulfate two-phase system

Summary We have developed a protein extraction technique which uses metal affinity ligands in PEG/salt aqueous two-phase systems. Cu(II)IDA-PEG will partition proteins according to their surface histidine contents in two-phase systems formed from sodium sulfate and polyethylene glycol. The nearly complete separation of human hemoglobin and human serum albumin in a single stage is presented as a demonstration of the effectiveness of metal affinity extraction in PEG/salt systems.     

Effect of surface histidine mutations and their number on the partitioning and refolding of recombinant human granulocyte-colony stimulating factor (Cys17Ser) in aqueous two-phase systems containing chelated metal ions

High-level expression of recombinant proteins in Escherichia coli frequently leads to the formation of insoluble protein aggregates, termed inclusion bodies. In order to recover a native protein from inclusion bodies, various protein refolding techniques have been developed. Column-based refolding methods and refolding in aqueous two-phase systems are often an attractive alternative to dilution refolding due to simultaneous purification and improved refolding yields. In this work, the effect of surface histidine mutations and their number on the partitioning and refolding of recombinant human granulocyte-colony stimulating factor Cys17Ser variant (rhG-CSF (C17S)) from solubilized inclusion bodies in aqueous two-phase systems polyethylene glycol (PEG)-dextran, containing metal ions, chelated by dye Light Resistant Yellow 2KT (LR Yellow 2KT)-PEG derivative, was investigated. Human G-CSF is a growth factor that regulates the production of mature neutrophilic granulocytes from the precursor cells. Initially, the role of His156 and His170 residues in the interaction of rhG-CSF (C17S) with Cu(II), Ni(II) and Hg(II) ions, chelated by LR Yellow 2KT-PEG, was investigated at pH 7.0 by means of affinity partitioning of purified, correctly folded rhG-CSF (C17S) mutants. It was determined that both His156 and His170 mutations reduced the affinity of rhG-CSF (C17S) for chelated Cu(II) ions at pH 7.0. His170 mutation significantly reduced the affinity of protein for chelated Ni(II) ions. However, histidine mutations had only a small effect on the affinity of protein for Hg(II) ions. The influence of His156 and His170 mutations on the refolding of rhG-CSF (C17S) from solubilized inclusion bodies in aqueous two-phase systems PEG-dextran, containing chelated Ni(II) and Hg(II) ions, was investigated. Reversible interaction of protein mutants with chelated metal ions was used for refolding in aqueous two-phase systems. Both histidine mutations resulted in a significant decrease of protein refolding efficiency in two-phase systems containing chelated Ni(II) ions, while in the presence of chelated Hg(II) ions their effect on protein refolding was negligible. Refolding studies of rhG-CSF variants with different number of histidine mutations revealed that a direct correlation exists between the number of surface histidine residues and refolding efficiency of rhG-CSF variant in two-phase systems containing chelated Ni(II) ions. This method of protein refolding in aqueous two-phase systems containing chelated metal ions should be applicable to other recombinant proteins that contain accessible histidine residues.     

Partition of proteins in aqueous two-phase systems containing charged dextran or hydrophobic PEG

Summary The electrochemical effect of a charged dextran derivative and the hydrophobic effect of hydrophobic chain PEG derivative on partitioning of six types of proteins in PEG/dextran aqueous two-phase systems were investigated- When 1. 6%(w/w)DEAE-dextran was present in the system,the partition coefficient decreased quickly with increasing pH value;when 0. 4% (w/w)PEG pentadecanoic acid ester was present in the system, the partition coefficient of protein with strong hydrophobicity was greatly increased. The experimental results show that the influence of hydrocarbon chain PEG derivative on partition coefficient is closely related to the hydrophobicity of proteins.     

Partitioning and characterization of tyrosine-tagged green fluorescent proteins in aqueous two-phase systems

The green fluorescent protein GFPuv has been genetically engineered to investigate the influence of N-terminal tyrosine extensions in aqueous two-phase systems. Fusions in the N-terminus affected the protein expression, and tags containing three tyrosines and prolines influenced the expression favorably. This effect is probably due to changes in mRNA stability, because the amounts of corresponding mRNAs correlated with the amounts of GFPuv proteins. The partitioning was investigated in two different aqueous two-phase systems, a two-polymer system composed of EO30PO70/dextran and a PEG/salt system with potassium phosphate. Partitioning in the PEG/salt system generally was more favorable than in the EO30PO70/dextran system. Tags with three tyrosines resulted in higher partitioning toward the EO30PO70- and PEG-rich phases, respectively. The effect of adding proline residues to the tag was also investigated, and the partitioning effect of the tag was enhanced when prolines were included in the tags with three tyrosines. The best tyrosine tag, Y3P2, increased the partition coefficient 5 times in the PEG/salt system. Thermoseparation of the EO30PO70 phase allowed recovery of 83% Y3P2-GFPuv protein in a water phase.     

Polymer fractionation in aqueous two-phase polymer systems.

We consider the effects of the addition of poly(ethylene glycol) (PEG) of different molecular weights to aqueous two-phase system of PEG 8000 and dextran 500. The first purpose of this study was to determine the molecular weight partitioning of the polymers themselves so that, for example, aqueous two-phase separations using affinity ligands can be improved. The second purpose was to examine whether this molecular weight partitioning could be predicted by using solution thermodynamic models so that it would be possible to optimize affinity partitioning without extensive laboratory work. Experimentally, we find that, by increasing the PEG concentration of any molecular weight in the feed, the high molecular weight PEG concentration in the dextran-rich phase is reduced. This observation can be used to reduce the loss of expensive ligated PEG used in affinity partitioning. Further, there is generally good agreement between our experimental data and the predictions of a solution thermodynamic model.     

An improved purification procedure of alkaline phosphatase from calf intestine by applying partition in aqueous two-phase systems and dye-ligand chromatography.

Aqueous two-phase partitioning has been elaborated in order to improve the purification of alkaline phosphatase from calf intestine in larger scale. The laborious precipitation and centrifugation steps for the removal of the enzyme from the cell debris and from the bulk protein were replaced by this technique yielding a high recovery (88%) and a significant lower time requirement. For the preparation of 100.000 units (46 mg) of a homogeneous enzyme 2.0 kg of a system containing 200 g PEG 4000 and only 10 g dextran M 70 is necessary. Affinity partitioning in aqueous two-phase systems was used to screen 41 dyes for selecting a suitable ligand for the dye-ligand chromatography of the enzyme. In the case of alkaline phosphatase the results obtained by affinity partitioning coincide with the experimental requirements for the affinity chromatography of the enzyme. Procion Navy HE-R (Blue 171) exhibits a high affinity, selectivity and binding capacity for the enzyme compared with other dyes investigated. The purification procedure provided the same degree in purity (2200 U/mg) and yield (59%) if mucosa or chyme was applied as starting material. In the range of practical use the purified enzyme contains no detectable activities of DNAses (endonucleases) and DNA-nicking activities. The contamination with phosphodiesterase I (EC. 3.1.4.1.) is less than 0.01%.     

Use of chemically modified proteins to study the effect of a single protein property on partitioning in aqueous two-phase systems: Effect of surface charge

A series of charge-modified thaumatins with different values of surface charge were partitioned in aqueous two-phase systems (ATPS) to study the effect of surface charge as a single property on partitioning. Electrophoretic mobility of the proteins in titration curves was used as a measure of surface charge. Four modified proteins derived from thaumatin with the following values of isoelectric point: 8.70, 8.15, 5.60, and 4.50 were used for partitioning. The resolution of the systems in terms of protein surface charge was calculated. Partitioning of modified thaumatins in PEG 4000/dextran systems with phosphate buffer, Tris buffer, NaCl, KCl, and sulfate salts was carried out. Among the sulfate salts tested, the addition of 50 mM Li(2)SO(4) to the system buffered with phosphate gave the highest value of resolution for differences in surface protein charge (RSPC). It shows a decrease in the value of K (partition coefficient) with an increase in the protein's charge. The addition of 100 mM KCl to the system promoted the opposite effect on the RSPC value. Charge-modified proteins were partitioned in PEG/salt systems to investigate the ability of these systems for resolving differences in surface charge. The PEG/citrate system seemed to have almost no ability for resolving proteins on the basis of surface charge differences; PEG/phosphate systems had some capability for resolving differently charged proteins. The more negative proteins tended to have higher values of K than the more positively charged fractions. The use of charge-modified proteins allowed the investigation of the effect of protein surface charge on partitioning in aqueous two-phase systems independently from other protein parameters as they were prepared from a common parent protein thaumatin. This technique provides an interesting novel tool to investigate the effect of protein surface charge on partitioning in ATPS taking protein charge as an independent parameter. (c) 1996 John Wiley & Sons, Inc.     

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.     

Hybridization-based affinity partitioning of nucleic acids using PEG-coupled oligonucleotides.

Polyethylene glycol (PEG)-coupled oligonucleotides are partitioned in an aqueous two-phase system PEG/dextran. The affinity of the oligonucleotide for the PEG-rich phase increases proportionally to the length of the coupled PEG polymer. After hybridization, the PEG-coupled oligonucleotide is able to force a complementary nucleic acid strand into the PEG-rich phase. This property can be used for the sequence-specific isolation of nucleic acids through hybridization-based affinity partitioning. The dependence of the partition coefficient in this system on various parameters is described. The application of this principle to multistage chromatographic separations is demonstrated.     

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.     

Use of chemically modified proteins to study the effect of a single protein property on partitioning in aqueous two-phase systems: Effect of surface hydrophobicity

Two different series of hydrophobically modified proteins were partitioned in a number of aqueous two-phase systems (ATPS) to investigate the effect of hydrophobicity as a single property on partitioning. The modified proteins were derived from beta-lactoglobulin and bovine serum albumin (BSA). Measurement of the surface hydrophobicity of the proteins is important; hydrophobic interaction chromatography (HIC) was used for this purpose. The resolution of the systems (R) in terms of protein surface hydrophobicity and the intrinsic hydrophobicity (log P(0)) of the systems was established. The effect of the addition of NaCl to PEG/phosphate and PEG/dextran systems was analyzed in terms of the hydrophobicity difference between the phases and their ability to promote hydrophobic interactions between the protein surface and the PEG molecules. The values for R and log P(0) differed somewhat depending on which group of modified proteins was used for partitioning. The addition of NaCl to PEG/phosphate systems promoted an increase in the values of R, showing an important effect on the resolution of the systems for protein surface hydrophobicity (twice as high when compared with systems without NaCl). For PEG/dextran systems, the addition of 9% NaCl (w/w) promoted an improvement in the resolution toward surface hydrophobicity with an increase of 60% on the value of R. (c) 1996 John Wiley & Sons, Inc.     

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.     

Purification of protein C from human plasma by precipitation and aqueous two-phase partitioning

Summary Precipitation with PEG and partitioning in PEG/dextran aqueous two-phase systems are applied to the purification of protein C, a human plasma protein with a key role in anti-coagulation. Tandem application of precipitation followed by partitioning yields a purification factor for protein C greater than that using either process individually. The results are discussed using the hypothesis that the mechanism of solvation of protein C by PEG is similar, while that for total plasma proteins is different, in the two processes.