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.     

Bovine serum albumin partitioning in an aqueous two-phase system: Effect of pH and sodium chloride concentration

The partitioning of bovine serum albumin (BSA) in a polyethylene glycol 3350 (8% w/w)–dextran 37 500 (6% w/w)–0.05 M phosphate aqueous two-phase was investigated at different pHs, at varying concentrations of sodium chloride at 20°C. The effect of NaCl concentration on the partition coefficient of BSA was studied for the PEG–dx systems with initial pH values of 4.2, 5.0, 7.0, 9.0, and 9.8. The NaCl concentrations in the phase systems with constant pH value were 0.06, 0.1, 0.2, 0.3, and 0.34 M. It was observed that the BSA partition coefficient decreased at concentrations smaller than 0.2 M NaCl and increased at concentrations greater than 0.2 M NaCl for all systems with initial pHs of 4.2, 5.0, 7.0, 9.0, and 9.8. It was also seen that the partition coefficient of BSA decreased as the pH of the aqueous two-phase systems increased at any NaCl salt concentration studied.     

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.     

Optimization of conditions for acid protease partitioning and purification in aqueous two-phase systems using response surface methodology

Aspergillopepsin I, an acid protease, was purified using an aqueous two-phase system that comprised various combinations of polyethylene glycol (PEG), NaH₂PO₄ and NaCl. Partition of the enzyme depended upon the molecular mass of the PEG and the presence of NaCl. With PEG 1500, 4000 and 6000, the partition coefficients were increased by 1,500-, 1,800- and 560-fold compared to values without NaCl. The presence of NaCl (8.75%, w/w) increased purification by 3.8, 9.5 and 2.8 times into these respective PEGs. The optimal aqueous two-phase system for acid protease purification was developed using response surface methodology. This system contained 17.3% of PEG 4000 (w/w), 15% NaH₂PO₄ (w/w) and 8.75% NaCl (w/w) and provided the best partition coefficient (Ke > 1,100) and yield over 99% in the same phase. The optimal ATPS purification factor of acid protease was over 5.     

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.     

牛血清白蛋白在聚乙二醇/葡聚糖双水相体系中分配特性的研究

采用考马斯亮蓝G250染色法测得室温下BSA在PEG/dextran双水相体系中的分配系数。以BSA在PEG/dextran体系的下相富集为目标,研究了PEG的分子量、浓度、dextran浓度以及所加入中性盐的种类与浓度、体系pH诸因素对其分配特性的影响。实验结果表明,在PEG4000/dextran体系中,采用PEG质量分数9%-dextran质量分数9%的浓度组成,同时在pH=7.0,NaC l浓度为0.2 mol.L-1或pH6.0,NaC l浓度为0.34 mol.L-1的工艺条件下萃取BSA均可达最小分配系数,其值为0.014。     

AQUEOUS TWO-PHASE EXTRACTION FOR THE PURIFICATION OF ALKALINE AGARASES FROM CULTURE EXTRACTS OF Pseudomonas aeruginosa AG LSL-11

The agarases were purified for the first time an using aqueous two-phase system (ATPS) consisting of polyethylene glycol (PEG) and phosphate salt. The three extracellular, alkaline agarases produced by Pseudomonas aeruginosa AG LSL-11 were efficiently extracted into the top PEG-rich layer. The influencing factors on the partition of agarases—molecular weight of the PEG, system pH, system temperature, and NaCl concentration—were investigated. All the factors were found to have a significant effect on the partition of agarases except NaCl. The optimal ATPS parameters for the partitioning and purification of agarases were found to be 12% PEG 600 and 11.9% (w/w) phosphate salt at pH 8.0 and 4°C. All three agarases were concentrated in the top PEG phase with 6.19-fold purity and 71.21% recovery. The ATPS was found to be more convenient and economical than the conventional ion-exchange chromatography (IEC) method for extraction of three agarases and could be significantly employed for the purification of agarases from fermentation broth.     

Fundamental studies of biomolecule partitioning in aqueous two-phase systems

Phase diagram data at 4 degrees C was determined for the aqueous two-phase systems composed of polyethylene glycol, dextran, and water. The Flory-Huggins theory of polymer thermodynamics was used to correlate partitioning of biomolecules in these aqueous two-phase systems resulting in a simple linear relationship between the natural logarithm of the partition coefficient and the concentration of polymers in the two phases. This relationship was verified by partitioning a series of dipeptides which differ from one another by the addition of a CH(2) group on the c-terminal amino acid residue and by utilizing a set of low-molecular-weight proteins. The slope of the line could be expressed in terms of the interactions of the biomolecule with the phase forming polymers and water. The main result for the dipeptides was that knowledge of the partition coefficient in any of the PEG/dextran/water systems, regardless of polymer molecular weight, enabled prediction of the coefficient in all of the systems. The dipeptides were also used for determination of the Gibbs free energy of transfer of a CH(2) group between the phases. This quantity was correlated with polymer concentration, thus establishing a hydrophobicity profile for the PEG/ dextran/water systems. The methodology for predicting dipeptide partition coefficients was extended to proteins, where it was found that low-molecular-weight proteins gave a linear relationship with the tie line compositions of a phase diagram.     

Phase diagrams for dextran-PEG aqueous two-phase systems at 22°C

Summary We have determined phase diagrams at 22°C for the aqueous two-phase systems composed of dextran, polyethylene glycol, and water. The effects of polyethylene glycol and dextran molecular weight on phase separation are reported. These phase diagrams provide more complete data for dextran/PEG/water system, and will be needed for the correlation of biomolecule partitioning.     

Purification and Characterization of Polyphenol Oxidase From Waste Potato Peel by Aqueous Two-Phase Extraction

Potato peel from food industrial waste is a good source of polyphenol oxidase (PPO). This work illustrates the application of an aqueous two-phase system (ATPS) for the extraction and purification of PPO from potato peel. ATPS was composed of polyethylene glycol (PEG) and potassium phosphate buffer. Effect of different process parameters, namely, PEG, potassium phosphate buffer, NaCl concentration, and pH of the system, on partition coefficient, purification factor, and yield of PPO enzyme were evaluated. Response surface methodology (RSM) was utilized as a statistical tool for the optimization of ATPS. Optimized experimental conditions were found to be PEG1500 17.62% (w/w), potassium phosphate buffer 15.11% (w/w), and NaCl 2.08 mM at pH 7. At optimized condition, maximum partition coefficient, purification factor, and yield were found to be 3.7, 4.5, and 77.8%, respectively. After partial purification of PPO from ATPS, further purification was done by gel chromatography where its purity was increased up to 12.6-fold. The purified PPO enzyme was characterized by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE), followed by K_m value 3.3 mM, and V_max value 3333 U/mL, and enzyme stable ranges for temperature and pH of PPO were determined. These results revealed that ATPS would be an attractive option for obtaining purified PPO from waste potato peel.     

Fusarium solani pisi recombinant cutinase partitioning in peg/potassium phosphate aqueous two-phase systems

Summary An aqueous two-phase system of polyethylene glycol (PEG) and potassium phosphate was developed for extraction of a cutinase from cell debris of a recombinant Escherichia coli strain. Basic studies to identify the primary factors which affect cutinase partition, namely the influence of polymer molecular weight, polymer concentration and pH were carried out using a purified preparation of the cutinase. The enzyme partition coefficient was enhanced with decreasing PEG molecular weight, increasing tie-line length and pH.     

Direct purification of Burkholderia Pseudomallei lipase from fermentation broth using aqueous two-phase systems

An aqueous two-phase purification process was employed for the recovery of Burkholderia pseudomallei lipase from fermentation broth. The partition behavior of B. pseudomallei lipase was investigated with various parameters such as phase composition, tie-line length (TLL), volume ratio (V_R), sample loading, system pH, and addition of neutral salts. Optimum conditions for the purification of lipase were obtained in polyethylene glycol (PEG) 6000-potassium phosphate system using TLL of 42.2% (w/w), with VR of 2.70, and 1% (w/w) NaCl addition at pH 7 for 20% (w/w) crude load. Based on this system, the purification factor of lipase was enhanced to 12.42 fold, with a high yield of 93%. Hence, the simplicity and effectiveness of aqueous two-phase systems (ATPS) in the purification of lipase were proven in this study.     

Aqueous two-phase systems containing urea: influence on phase separation and stabilization of protein conformation by phase components.

During recombinant Escherichia coli fermentation with high expression levels, inclusion bodies are often formed. Aqueous two-phase systems have been used in the presence of urea for the initial recovery steps. To investigate phase behavior of such systems we determined phase diagrams of poly(ethylene glycol) (PEG)/sodium sulfate/urea/water and PEG/dextran T-500 (DEX)/urea/phosphate buffer/water at different concentrations of urea and different molecular weight of PEG. PEG/Na2SO4 aqueous two-phase systems could be obtained including up to 30% w/w urea at 25 degrees C and PEG/dextran T-500 up to 35% w/w urea. The binodial was displaced toward higher concentrations with increasing urea concentrations. The partition coefficient of urea was near unity. An unstable mutant of T4-lysozyme with an amino acid replacement in the core (V149T) was used to analyze the effect of phase components on the conformation of the enzyme. We showed that partitioning of tryptophan was not dependent on the concentration of urea in the phase system.     

Partitioning studies of α-lactalbumin in environmental friendly poly (ethylene glycol)—citrate salt aqueous two phase systems

Aqueous two-phase systems (ATPS) formed by polymer and salt have been utilized to enrich the desired biomolecule into one of the phase with higher yield and purity. The eco-friendly, biodegradable poly ethylene glycol (PEG) and different citrate salts were chosen as ATPS phase components to investigate the partitioning behavior of α-lactalbumin (α-La). System factors and process parameters such as type and concentration of salt, molecular weight and concentration of PEG, pH, temperature and the effect of additives were studied and the results are discussed in detail. PEG 1000–tri-potassium citrate system yields high partition coefficient of 20 with a better yield of 98 % in the top phase. The addition of NaCl as an additive and acidic pH lowers the yield of α-La in the top phase. Influence of phase volume ratio (V _r) on partitioning was studied and found that the partition coefficient remains almost constant along the tie line. High yield was achieved at a V _r of 3.5 at the tie line length of 50.63 (%, w/w).     

PEG/NaPA aqueous two-phase systems for the purification of proteases expressed by Penicillium restrictum from Brazilian Savanna

The partitioning of proteases expressed by Penicillium restrictum from Brazilian Savanna in an inexpensive aqueous two-phase system composed of poly (ethylene glycol) (PEG) and sodium polyacrylate (NaPA) was studied. The effects of PEG molecular weight and concentration, as well as NaPA concentration and the concentration of fermented broth on protease partitioning were studied. Partitioning into the top PEG-rich phase was increased in systems with smaller PEG-molecular weight, higher NaPA concentration and lower PEG concentration. For most systems studied, purification has been achieved by directing the biomolecule partition to the opposite phase of the other proteins, providing the enzyme purification. The highest partition coefficient was obtained using 20 wt% NaPA, 4 wt% PEG 2000 g mol⁻¹ and 45 wt% fermented broth, leading to a purification factor of 1.98 and partition coefficient of 37.73. The system showed high mass balances and yield, indicating enzyme stability and applicability for industrial processes. The partitioning results using the PEG/NaPA/NaCl system show that this method could be used to purify or concentrate protease from fermented broth.     

Extraction of protease from Aspergillus tamarii URM 4634 in aqueous two-phase system under continuous and discontinuous process

Abstract

Aqueous two-phase systems have been studied for almost a century to separate biomolecules in harmless conditions. Proteases produced by Aspergillus tamarii URM 4634 were extracted in polyethylene glycol (PEG)/phosphate aqueous two-phase system under discontinuous and continuous (perforated rotative discs column) process. On the discontinuous process, it was evaluated the effect of operational conditions (PEG molar mass and its concentration, phosphate concentration and pH) over the partition coefficient, activity yield and purification factor. Protease partitioned to PEG-phase with partition coefficients up to 55.73. The best process parameters were 17.5% of PEG, with molar mass 8000?g·mol^?1, 15% of phosphate salt at pH 6, with 113.15% of activity yield and purification factor of 2.62. Under continuous extraction, hold up data showed that 57.1% of the discontinuous phase was available for protein extraction. Further, separation achieved 90.0% of efficiency. The yields surpassed 100% in almost all runs, and the best purification factor was 1.84, with both flows of 2?mL·min^?1. Thus, the best operational conditions reached an activity yield of 95.3% and 90.0% of separation efficiency. Hence, aqueous two-phase system PEG/phosphate extraction is an efficient process for separation of proteases produced by Aspergillus tamarii URM 4634, under continuous extraction likewise under discontinuous process.     

Partitioning of xylanolitic complex from Penicillium janthinellum by an aqueous two-phase system

This work evaluates the influences of five parameters (pH, PEG molecular mass, PEG concentration, concentration of buffer K₂HPO₄–KH₂PO₄ and NaCl concentration) on xylanolitic complex partitioning produced by P. janthinellum in aqueous two-phase systems, using a 2⁵ factorial experimental design. A mathematical model to quantify the influence of these parameters was attained and statistically tested. The optimum point for total protein extraction was obtained under the following conditions: pH 7.0, PEG 10 000, 3.67% PEG, 10% potassium phosphate and 12.4% NaCl. The partition coefficient (K) value experimentally obtained was 5.25 and that predicted by the model was 5.89.     

Simultaneous biosynthesis and purification of two extracellular Bacillus hydrolases in aqueous two-phase systems

Thermostable a-amylase with temperature optimum at 80 °C, molecular mass 58 kDa and pI point 6.9 was purified from a catabolite resistant Bacillus licheniformis strain. The enzyme was sensitive to inhibition by metal ions and N-bromosuccinimide. The partition behaviour of this enzyme in aqueous two-phase systems (ATPS) of the polymer-polymer-water type was investigated and some effects of type, molecular weight and concentration of phase components were studied. Up to 100% retention in the bottom phase of polyethylene glycol 10,000—20,000/dextran 200 system was reached. Best partition conditions were obtained in PEG 10,000—20,000/polyvinyl alcohol 200 systems, where the partition coefficient K increased 750 times to 7.5. Simultaneous production and purification of a-amylase and serine proteinase in PEG-polymer-water ATPS were examined. In the system PEG 6,000/ficoll, up to 90% of the amylase was retained in the bottom phase, whereas about 95% of the total protein (K = 22.8) and 60—75% of the proteinase were in the top phase. Similar separation of the enzymes from laboratory supernatant was obtained in system PEG/Na₂SO₄.     

Porcine pancreatic lipase partition in potassium phosphate-polyethylene glycol aqueous two-phase systems

This research study examined porcine pancreatic lipase partition in aqueous two-phase systems formed by polyethylene glycol-potassium phosphate at pH 6.0, 7.0 and 8.0, the effect of polymer molecular mass, and NaCl concentration. The enzyme was preferentially partitioned into the polyethylene glycol rich phase in systems with molecular mass 4000-8000, while with polyethylene glycol of 10,000 molecular mass it was concentrated in the phosphate rich phase. The enthalpic and entropic changes found due to the protein partition were negative for all the polyethylene glycol molecular mass systems assessed. Both thermodynamic functions were shown to be associated by an entropic-enthalpic compensation effect suggesting that the water structure ordered in the ethylene chain of polyethylene glycol plays a role in the protein partition. The addition of NaCl increased the lipase affinity to the top phase and this effect was most significant in the system polyethylene glycol 2000-NaCl 3%. This system yielded an enzyme recovery more than 90% with a purification factor of approximately 3.4.     

Cultivation of plant cells in aqueous two-phase polymer systems

Summary Suspension cultures ofNicotiana tabacum have been successfully grown in aqueous, two-phase systems comprised of polyethylene glycol (PEG) and dextran in a modified LS medium. Aqueous two-phase systems may be advantageous for plant tissue cultivation since cells can be immobilized in one phase while secondary products are collected and withdrawn in the other phase, thus enhancing productivity. Culture growth rate was compared in a variety of two-phase systems, covering a range of both polymer molecular weight and concentration. Systems exhibiting relatively higher phase miscibility yielded increased growth rates as compared to less miscible phase formulations. The highest observed growth rate occurred in 3% PEG 20000/5% crude dextran and approached growth rates and cell densities of cultures grown in standard LS medium.