Purification of alcohol dehydrogenase from bovine liver crude extract by dye-ligand affinity counter-current chromatography

Alcohol dehydrogenase (ADH) was extracted from a crude bovine liver homogenate by dye-ligand affinity counter-current chromatography (CCC) using a cross-axis coil planet centrifuge (x-axis CPC). The purification was performed using two types of polymer phase systems composed of 4.4% polyethylene glycol (PEG) 8000-7.0% dextran T500-0.1 M potassium phosphate buffers and 16% PEG 1000-12.5% potassium phosphate buffers, both containing a procion red dye as an affinity ligand at various pH values. The best purification was achieved using the PEG 1000-potassium phosphate system at pH 7.3 containing 0.05% procion red as a ligand. The upper PEG-rich phase containing procion red was used as the stationary phase and a crude bovine liver homogenate was eluted with the potassium phosphate-rich lower phase at 0.5 ml/min. After elution of bovine liver proteins in the homogenate, ADH still retained in the stationary phase was collected from the column by eluting with the PEG 1000-rich upper phase. Collected fractions were analyzed by ADH enzymatic activity and by sodium dodecyl sulfate (SDS)-polyacrylamide gel electrophoresis (PAGE) to detect contaminant proteins in the ADH fractions. The ADH was purified directly from crude bovine liver extract within 6h with minimum loss of its enzymatic activity.     

Purification and aqueous two-phase partitioning properties of recombinant Vitreoscilla hemoglobin.

Soluble recombinant Vitreoscilla hemoglobin was purified from E. coli lysate by sequential two-phase extraction techniques. Extraction of lysate containing VHb in PEG/dextran gave a 3.6-fold increase in VHb purity in the PEG-rich phase via a size exclusion mechanism. Further extraction of the recovered PEG phase in PEG/sodium sulfate gave an additional 2.0-fold increase in purity in the PEG-rich phase due to an electrostatic mechanism. Final extraction of the PEG phase in PEG/magnesium sulfate gave an additional 1.3-fold increase in VHb purity in the magnesium sulfate-rich phase. The final yield from the extractive purification was 47% with purity of VHb estimated to be greater than 95%. Yields from the sulfate salt extractions are essentially quantitative due to the extreme partitioning behavior of VHb in these systems. VHb partition coefficients as large as 46 in PEG/sodium sulfate and as small as 0.06 in PEG/magnesium sulfate were observed. Similar small partition coefficients were obtained with PEG/manganese sulfate extractions. This dramatic effect of divalent cation content on the partition coefficient of VHb in PEG/sulfate salt systems was investigated by pH and magnesium ion titration experiments. Results show the effect to be largest and nearly constant for pH values greater than 6.0 and diminished at lower pH values. A model based on magnesium ion binding to negatively charged amino acids is shown to correlate with the data well. Based on model formulation and the partitioning behavior of contaminant proteins, the observed effect is expected to be applicable to other proteins.     

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%.     

Isolation of plasmid DNA from cell lysates by aqueous two-phase systems

This work presents a study of the partitioning of a plasmid vector containing the cystic fibrosis gene in polyethylene glycol (PEG)/salt (K2HPO4) aqueous two-phase systems (ATPS). The plasmid was extracted from neutralized alkaline lysates using PEG with molecular weights varying from 200 to 8000. The effects of the lysate mass loaded to the ATPS (20, 40, and 60% w/w) and of the plasmid concentration in the lysate were evaluated. The performance of the process was determined by qualitative and quantitative assays, carefully established to overcome the strong interference of impurities (protein, genomic DNA, RNA), salt, and PEG. Plasmid DNA partitioned to the top phase when PEG molecular weight was lower than 400. The bottom phase was preferred when higher PEG molecular weights were used. Aqueous two-phase systems with PEG 300, 600, and 1000 were chosen for further studies on the basis of plasmid and RNA agarose gel analysis and protein quantitation. The recovery yields were found to be proportional to the plasmid concentration in the lysate. The best yields (>67%) were obtained with PEG 1000. These systems (with 40 and 60% w/w of lysate load) were able to separate the plasmid from proteins and genomic DNA, but copartitioning of RNA with the plasmid was observed. Aqueous two-phase systems with PEG 300 concentrated both plasmid and proteins in the top phase. The best system for plasmid purification used PEG 600 with a 40% (w/w) lysate load. In this system, RNA was found mostly in the interphase, proteins were not detected in the plasmid bottom phase and genomic DNA was reduced 7.5-fold.     

Purification of lactic acid dehydrogenase from crude bovine heart extract by pH-peak focusing counter-current chromatography

pH-peak focusing counter-current chromatography (CCC) was applied to the purification of lactic acid dehydrogenase (LDH) from a crude bovine heart extract using a cross-axis coil planet centrifuge (CPC). The experiment was performed with two sets of polymer phase systems composed of 16% (w/w) polyethylene glycol (PEG) 1000-12.5% (w/w) potassium phosphate buffer and 15% (w/w) PEG 1540-15% (w/w) ammonium sulfate each at various pH values. The best result was achieved from the PEG 1540-ammonium sulfate polymer phase system by adding a retainer (10 mM acetic acid) to the upper stationary phase and an eluter (100 mM sodium hydroxide) to the lower mobile phase. At a flow-rate of 0.5 ml/min, LDH was eluted as a sharp peak which was well resolved from other proteins. Collected fractions were analyzed by the LDH enzymatic activity and by sodium dodecyl sulfate-polyacrylamide slab gel electrophoresis to detect contaminated proteins. LDH was purified directly from crude bovine heart extract in a concentrated state.     

Crystallization of IgG1 by mapping its liquid-liquid phase separation curves

Monoclonal antibody therapeutics is an important and fast expanding market. While production of these molecules has been a major area of research, much less is known regarding the stabilization of these proteins for delivery as drugs. Crystallization of antibodies is one such promising route for protein stabilization at high titers, and here we took a systematic approach to initiate crystallization through nucleation in a simple PEG (polyethylene glycol), protein in water solution. A ternary mixture of globular proteins, PEG, and water will undergo a liquid-liquid phase separation (LLPS) as shown in a phase diagram or a Binodal curve. Of particular interest within the phase diagram is the position of the critical point, which is where nucleation occurs most rapidly. Detailed LLPS maps were created by increasing concentrations of PEG (from 5% to 11%) and IgG (from 1 to 20 mg/mL). By increasing the molecular weight (MW) of PEG (and hence its radius of gyration) from 1,000 to 6,000 g/mol, the temperatures of the critical point of nucleation were shown to increase. Once these curves were determined, nucleation experiments were conducted close to a chosen critical point (10.5 mg/mL IgG in 11% PEG 1000) and after 3 weeks, crystals of IgG of approximately 100 microm in size were successfully formed. This is the first example of crystallization of an antibody through systematic mapping of LLPS curves, which is a fundamental step towards the scale-up of antibody crystallization.     

Aqueous two-phase partition and detergent precipitation of a drug-responsive NADH oxidase from the HeLa cell surface

The partitioning behaviour of a drug (capsaicin)-responsive NADH oxidase (tNOX) activity released from HeLa ceIls by low pH treatment followed by heat and proteinase K was determined. When partitioned in a standard 6.4% PEG 3350/6.4% dextran T-500 two-phase system, the bulk of the tNOX activity was in the dextran-rich lower phase. The activity was inhibited by and bound to the triazine dye, Cibacron blue. Affinity partition, where the Cibacron blue was coupled to amino PEG 5000 and added to the first two-phase separation step, resulted in the partitioning of activity to the upper PEG phase. A second partition with PEG-salts resulted in the release of the tNOX from the Cibacron blue–amino PEG enriched phase into the salt-enriched lower phase. The phase-purified protein exhibited anomalous behavior and tended to multimerize in sodium dodecyl sulphate (SDS) prior to SDS-polyacrylamide gel electrophoresis (PAGE). Multimerization appeared to be enhanced by PEG. The multimerization was enhanced with the reduced protein in the presence of detergent prior to SDS–PAGE. In addition, the activity was precipitated by PEG 8000 at concentrations between 6 and 30% by weight. In the presence of or after exposure to PEG 3350 or PEG 8000, the protein could not be detected by Western blot analysis after SDS–PAGE suggesting that the protein failed to enter the gel even though other HeLa cell surface proteins were unaffected. The anomalous multimerization behavior has thus far precluded the use of phase partition as a practical purification step for the oxidase.     

Correlation for the partition behavior of proteins in aqueous two-phase systems: effect of surface hydrophobicity and charge

Correlations to describe the effect of surface hydrophobicity and charge of proteins with their partition coefficient in aqueous two-phase systems were investigated. Polyethylene glycol (PEG) 4000/phosphate, sulfate, citrate, and dextran systems in the presence of low (0.6% w/w) and high (8.8% w/w) levels of NaCl were selected for a systematic study of 12 proteins. The surface hydrophobicity of the proteins was measured by ammonium sulfate precipitation as the inverse of their solubility. The hydrophobicity values measured correlated well with the partition coefficients, K, obtained in the PEG/salt systems at high concentration of NaCl (r = 0.92-0.93). In PEG/citrate systems the partition coefficient correlated well with protein hydrophobicity at low and high concentrations of NaCl (r = 0.81 and 0.93, respectively). The PEG/citrate system also had a higher hydrophobic resolution than other systems to exploit differences in the protein's hydrophobicity. The surface charge and charge density of the proteins was determined over a range of pH (3-9) by electrophoretic titration curves; PEG/salt systems did not discriminate well between proteins of different charge or charge density. In the absence of NaCl, K decreased slightly with increased positive charge. At high NaCl concentration, K increased as a function of positive charge. This suggested that the PEG-rich top phase became more negative as the concentration of NaCl in the systems increased and, therefore, attracted the positively charged proteins. The effect of charge was more important in PEG/dextran systems at low concentrations of NaCl. In the PEG/dextran systems at lower concentration of NaCl, molecular weight appeared to be the prime determinant of partition, whereas no clear effect of molecular weight could be found in PEG/salt systems.     

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.     

Polymorphic phase behavior of lysopalmitoylphosphatidylcholine in poly(ethylene glycol)-water mixtures

The polymorphic phase behavior of 1-palmitoyl-2-lyso-sn-glycero-3-phosphocholine dispersions in excess water has been studied as a function of temperature and poly(ethylene glycol) (PEG) concentration, using proton dipolar-decoupled 31P NMR spectroscopy and turbidity measurements. The phase behavior was found to depend on both lipid concentration and PEG concentration, and most of the NMR experiments were conducted at a lipid concentration of 15 mg/mL. At low PEG concentrations (0-12 wt %), a thermotropic transition occurs at 3-5 degrees C with increasing temperature, from an interdigitated lamellar gel (L beta i) phase to a normal micellar phase. At intermediate PEG concentrations (12-20 wt %), thermotropic transitions take place with increasing temperature, first from the lamellar gel phase to a fluid cubic (Q alpha) phase and then at higher temperatures from the cubic phase to the micellar phase. At intermediate PEG concentrations above the former range (20-30 wt %), thermotropic transitions take place with increasing temperature, first from the lamellar gel phase to the cubic phase, then from the cubic phase to a normal hexagonal (HI) phase, and finally from the hexagonal phase to the micellar phase. At high PEG concentrations (greater than 30 wt %), a thermotropic transition takes place with increasing temperature from the lamellar gel phase directly to the fluid hexagonal phase. At these high PEG concentrations, the micellar phase is not attained within the accessible temperature range (less than or equal to 90 degrees C).(ABSTRACT TRUNCATED AT 250 WORDS)     

Separation of recombinant β-glucuronidase from transgenic tobacco by aqueous two-phase extraction

Transgenic plants hold many promises as viable production hosts for therapeutic recombinant proteins. Many efforts have been devoted to increase the expression level of the proteins, but the efforts for developing economic processes to purify those proteins are lacking. In this report, aqueous two-phase extraction (ATPE) was investigated as an alternative for the separation of an acidic recombinant protein, β-glucuronidase (rGUS), from transgenic tobacco. Screening experiments by fractional factorial designs showed that PEG concentration and ionic strength of the system significantly affected the partitioning of native tobacco proteins and GUS. Response surface methodology was used to determine an optimized aqueous two-phase system for the purification of rGUS from transgenic tobacco. In a 13.4% (w/w) PEG 3400/18% (w/w) potassium phosphate system, 74% of the rGUS was recovered in the top PEG-rich phase while more than 90% of the native tobacco proteins were removed in the interphase and the bottom phase. A purification factor of about 20 was achieved in this process. The most important impurity from tobacco, Rubisco, was largely removed from the rGUS in the recovered phase.     

The application of aqueous two-phase systems to the purification of pharmaceutical proteins from transgenic sheep milk

Transgenic sheep milk containing the protein human₁-Antitrypsin (AAT) was partitioned in Poly(ethyleneglycol) (PEG)-Sulphate and PEG-Phosphate biphasic systems. Individual partition coefficients for AAT and some of the milk proteins were determined in these systems. The effects of PEG molecular weight, pH and the inclusion of NaCl on the partitioning of the proteins were also studied. It was found that increasing the concentration of NaCl and decreasing the molecular weight of the PEG resulted in an increase of the partition coefficients of the proteins to the upper (PEG) phase. This partitioning effect was greater for the more hydrophobic proteins and particularly in systems having a pH close to the isoelectric point of the protein. Solubilities of the proteins in increasing concentrations of ammonium sulphate were measured in order to investigate the effects of hydrophobic and electrostatic interactions on the partitioning of these proteins in aqueous two-phase systems. Those proteins that precipitated at low levels of ammonium sulphate showed an increase in partition coefficient at low concentrations of NaCl, or they were precipitated at the interface of the phases at low concentrations of NaCl. Proteins that had low salting out constants in ammonium sulphate solutions were relatively unaffected by NaCl in ATPS. It is probable however that conformational changes and the state of aggregation of proteins are also important and should be invoked in describing the partitioning behavior observed for -Lg for example. Comparison of theoretical and experimental values for AAT yield and purity showed clearly that partition coefficients are influenced by the degree of purity and values obtained with purified standards are not necessarily the same as for the same protein present in a complex mixture. Under the most favourable conditions using a 4% w/w loading of transgenic ovine milk, we obtained a 91% yield of AAT in the PEG phase with a purity of 73%.This revised version was published online in October 2005 with corrections to the Cover Date.     

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.     

Hydrodynamics and mass transfer in two-phase aqueous extraction using spray columns

Spray columns can be used to isolate and purify proteins using the two-phase aqueous extraction technique based on polyethylene glycol (PEG) and dextran. The fractional dispersed phase (PEG) holdup and overall mass transfer coefficients were measured in a 9.7 mm i.d. spray column. We found that the dispersed phase holdup increased with increasing PEG phase velocity. The overall mass transfer coefficients for bovine serum albumin, normalized for the PEG holdup, were found to be independent of the PEG phase velocity. This result was expected, since true mass transfer coefficients do not vary with phase velocity.     

Application of the response surface methodology for optimization of whey protein partitioning in PEG/phosphate aqueous two-phase system

In order to develop a new strategy for β-lactoglobulin (β-lg) removal from whey protein, partitioning of α-lactalbumin (α-la), β-lg and glycomacropeptide (Gmp) was studied using aqueous two phase systems (ATPS). A system composed of 13% (w/w) polyethylene glycol (PEG, average molar mass 2000 g/mol) and 13% (w/w) potassium phosphate was used at 25°C. A central composite rotatable design (CCRD) associated to the response surface methodology (RSM) was applied to investigate the effects of NaCl concentration and pH on the partition of these proteins. It was found that α-la and Gmp partitioned to the top phase rich in PEG, whereas β-lg partitioned to the bottom phase rich in salt. According to the RSM, optimal conditions for β-lg removal where found where pH was equal to 6.7 and salt concentration was 0.35 mol/L. Under these conditions, the partition coefficient K(α) was 0.48 and K(Gmp) was 0.92. On the other hand, the partition coefficient K(β) was only 0.01. In such conditions β-lg preferentially concentrates in the bottom phase, while the top phase exclusively contains the proteins α-la and Gmp. Fractionation of the proteins from fresh whey was performed in a three stage cross-flow extraction system. The extraction yield for β-lg in the bottom phase was 97.3%, while the yields for α-la and Gmp in the top phase were 81.1% and 97.8%, respectively.     

Purification of green fluorescent protein overexpressed by a mutant recombinant Escherichia coli

Green fluorescent protein was purified from sonicated recombinant Escherichia coli and its mutant obtained after exposure to UV light. The latter overexpresses green fluorescent protein. The two-step procedure consisted of a two-phase aqueous extraction with PEG/salt and precipitation of the proteins from PEG phase by free Zn2+. The recoveries of green fluorescent protein were 73 and 83% in the cases of recombinant E. coli and its mutant, respectively. The corresponding fold purifications were 24 and 9, respectively. In both cases, the purified protein showed a single band on SDS-PAGE corresponding to 28 kDa.     

Relations between hydrophobicity tested by three methods and surface chemical composition of Escherichia coli

The cell surface hydrophobicity of three strains of Escherichia coli cultured in liquid medium and on solid medium was measured using various methods including adsorption to pxylene, partition of cells in a polyethylene glycol/dextran (PEG/DEX) two phase system and contact angle measurements. The percentage adsorbed to pxylene ranged from 1.6% to 67% and the percentage of cells in polyethylene glycol phase ranged from 19% to 64%. The contact angle data of less than 40 degrees C revealed a hydrophylic character of the E. coli strains studied here. No relations were found between paraxylene/water partitioning, PEG/DEX partioning and water contact angles. The linear correlation coefficients between the results of the three hydrophobicity assays and the elemental concentration ratios obtained by X-ray photoelectron spectroscopy (XPS) were calculated. A linear correlation was found between the contact angles and the O/C ratios (r=0.91) and the N/C ratios (0.67). The adsorption to pxylene correlates better with N/C ratios (0.88) but does not correlate with O/C ratios (0.46). However, this test correlates with N/P ratios (0.79). No relation was obtained between partition in PEG/DEX system and any elemental concentration ratios. The surface composition determined by XPS was converted into a molecular composition in terms of proteins, polysaccharides, and hydrocarbon-like compounds. The proteins/polysaccharides and the hydrocarbons/polysaccharides seems to determine the contact angle of E. coli but not the adsorption to paraxylene or partition in the PEG/DEX system.     

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.     

Production of cyclodextrin homologues using aqueous two-phase system

Cyclodextrin homologues (CDs), produced by cyclodextrin glycosyltransferase (CGTase), were simultaneously partitioned in aqueous two-phase system (ATPS). Partition coefficients of CDs were measured in PEG/salt and PEG/dextran systems. Phosphate, citrate, sulfate were tested as salt. ATPS of PEG/salt and PEG/dextran had the partition coefficients of the CDs, larger than unity. However, PEG/dextran system was observed better than PEG/salt as CGTase activity decreased sharply with salt concentration. Enzymatic reaction occurred mainly in PEG-rich bottom phase because of the low partition coefficient of CGTase. The resulting CDs transferred to the PEG-rich top phase, obeying the diffusional partition. In the ATPS of 7% PEG (M.W. 20,000) and 9% dextran (M.W. 40,000), 7 mg/ml of CDs were obtained in top phase at 4.5 hours.     

Preparation, characterization and in vitro bioactivity of N-terminally PEGylated staphylokinase dimers

PEGylation can improve the therapeutic efficacy of proteins by increasing serum half-life of proteins and reducing immunogenicity and antigenicity. However, PEGylation results in a substantial loss of the bioactivity of proteins due to the steric hindrance of polyethylene glycol (PEG). Dimerization of the proteins is an efficient approach to increase the bioactivity of the PEG-protein conjugates. Here, staphylokinase (SAK) was used due to its therapeutic potential for coronary thrombolysis. SAK dimers (dSAK) were prepared by engineering cysteine residue at the C-terminus of SAK and dimerization of the cysteine residue with 1,4-bismaleimidobutane. PEG aldehyde was used for site-specific PEGylation of dSAK at one of its two N-termini. Structural analysis indicated that dimerization of SAK can decrease the steric hindrance of PEG and increase the binding affinity of PEG-SAK to plasminogen. Dimerization of SAK increased the relative bioactivity of PEG-SAK from 39.0% to 62.0%. Therefore, site-specifically PEGylated dSAK at one of its two N-termini has higher bioactivity than the N-terminal PEGylated SAK.