Partitioning of caseinomacropeptide in aqueous two-phase systems

This study evaluates the influence of type of salt and temperature on the partition coefficient of caseinomacropetide (CMP) to determine the best conditions for the recovery of CMP in aqueous two-phase systems (ATPS) composed by poly(ethylene glycol) (PEG) 1500 and an inorganic salt (potassium phosphate, sodium citrate, lithium sulfate or sodium sulfate). In all systems, CMP presented affinity for the PEG-rich phase. The PEG1500+lithium sulfate showed the highest values of partitioning coefficient. In addition, thermodynamic parameters (DeltaH degrees , DeltaS degrees , DeltaG degrees) as a function of temperature, were calculated for the system PEG1500-sodium citrate at different PEG concentrations and the results imply thermodynamic differences between partitioning of CMP in this system.     

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.     

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.     

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.     

Aqueous two-phase partition of complex protein feedstocks derived from brain tissue homogenates

This study describes the application of aqueous two-phase partition using polyethylene glycol (PEG)-potassium phosphate systems for the direct recovery of proteins, and aggregates thereof, from mammalian brain tissue homogenates. Investigation of established methodologies for the purification of prion proteins (PrP) from bovine brain affected with transmissible spongiform encephalopathy (BSE) has identified an alternative purification regime based on aqueous two-phase partition. This circumvents energy-intensive and rate-limiting unit operations of ultracentrifugation conventionally used for isolation of PrP. Selectivity of various PEG-phosphate systems varied inversely with polymer molecular mass. The maximum protein recovery from bovine brain extracts was obtained with systems containing PEG 300. Manipulation of the aqueous environment, to back-extract protein product from the PEG-rich top phase into the phosphate-rich lower phase, enabled integration of ATPS with conventional hydrophobic interaction chromatography (HIC) which selectively removes obdurate contaminating proteins (i.e. ferritin).     

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.     

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.     

Optimisation of aqueous two-phase extraction of human antibodies

The purification of human antibodies in an aqueous two-phase system (ATPS) composed of polyethylene glycol (PEG) 6000 and phosphate was optimised by surface response methodology. A central composite design was used to evaluate the influence of phosphate, PEG and NaCl concentration and of the pH on the purity and extraction yield of IgG from a simulated serum medium. The conditions that maximise the partition of IgG into the upper phase were determined to be high concentrations of NaCl and PEG, low concentrations of phosphate and low pH values. An ATPS composed of 12% PEG, 10% phosphate, 15% NaCl at pH 6 was further used to purify human monoclonal antibodies from a Chinese Hamster Ovary (CHO) concentrated cell culture supernatant with a recovery yield of 88% in the upper PEG-rich phase and a purification factor of 4.3. This ATPS was also successfully used to purify antibodies from a hybridoma cell culture supernatant with a recovery yield of 90% and a purification factor of 4.1.     

Production of immobilized penicillin acylase using aqueous polymer systems for enzyme purification and in situ immobilization

A novel approach for the isolation and purification of penicillin acylase (PA), which couples aqueous two-phase partitioning and enzyme immobilization has been investigated.A PA yield of 90% was achieved by treating E. coli cells with 4% butyl acetate, freeze-thawing step, and pressure homogenization. PA purification (93% recovery) was achieved by (1) removing cell debris via precipitation with polyethylene glycol (PEG 2000); (2) aqueous two-phase partitioning using a PEG 2000 + phosphate system (87% recovery).An in situ enzyme immobilization approach, using oxirane acrylic or aldehyde-agarose beads dispersed in the PEG-rich phase, was explored for the conversion of penicillin G to 6-aminopenicillanic acid. An appropriate immobilization reaction time was found. The catalytic performance of the enzyme, when immobilized, was found not to be affected by recycling of the phase-forming components.     

Novel approach towards recovery of glycosaminoglycans from tannery wastewater

Poly ethylene glycol (PEG)-poly acrylic acid (PAA) based aqueous two-phase system (ATPS) was selected as a practical model to recover glycosaminoglycans (GAGs) from tannery wastewater. The influence of PEG molecular weight, tie line length (TLL), pH, temperature and NaCl concentration on the partition coefficient of glycosaminoglycans from tannery wastewater was studied. Partition coefficient of glycosaminoglycan decreases on increase of PEG molecular weight, NaCl concentration and temperature, whereas it increases with increase of pH. In the PEG-rich phase, increased partitioning of GAGs was observed with increase in TLL. The partitioning of GAGs was better in PEG 4000 at pH 8.0, 20 °C with a yield of 91.50%. This study demonstrates the potential application of ATPS processes for the recovery of GAGs from complex biological suspensions.     

Purification and in situ immobilization of lipase from of a mutant of Trichosporon laibacchii using aqueous two-phase systems

The crude intracellular lipase (cell homogenate) from Trichosporon laibacchii was subjected to partial purification by aqueous two-phase system (ATPS) and then in situ immobilization by directly adding diatomites as carrier to the top PEG-rich phase of ATPS. A partition study of lipase in the ATPS formed by polyethylene glycol–potassium phosphate has been performed. The influence of system parameters such as molecular weight of PEG, system phase composition and system pH on the partitioning behaviour of lipase was evaluated. The ATPS consisting of PEG 4000 (12%) and potassium phosphate (K₂HPO₄, 13%) resulted in partition of lipase to the PEG-rich phase with partition coefficient 7.61, activity recovery 80.4%, and purification factor of 5.84 at pH of 7.0 and 2.0% NaCl. Moreover, the in situ immobilization of lipase in PEG phase resulted in a highest immobilized lipase activity of 1114.6 U g^?1. The above results show that this novel lipase immobilization procedure which couples ATPS extract and enzyme immobilization is cost-effective as well as time-saving. It could be potentially useful technique for the purification and immobilization of lipase.     

Extraction and purification of amyloglucosidase produced by solid state fermentation with Aspergillus niger

Summary Aqueous two-phase extraction was employed, as a new approach, for the recovery of amyloglucosidase (AMG) after solid state fermentation. In an aqueous two-phase system of PEG 6000 and potassium phosphate, 95% of the AMG was recovered in the bottom salt phase, with all visible particles from solid fungal bran in the interface, giving a purification factor of 11. Affinity purification of AMG was also done by adsorption onto crosslinked starch, in the presence of PEG or salt. Both were found to enhance the adsorption. In the presence of PEG 6000 (10% w/w), two fold increase in AMG adsorption, 85% of AMG recovery and 6.0 fold of purification were achieved/The purified AMG was found homogeneous by SDS polyacrylamide gel electrophoresis.     

Partitioning of whey proteins, bovine serum albumin and porcine insulin in aqueous two-phase systems

Partitioning of the proteins from cheese whey, bovine serum albumin and porcine insulin were analysed using aqueous two-phase systems (ATPS) prepared with PEG–phosphate, PEG–citrate and PEG–maltodextrin (MD). Proteins were quantified through one of the following methods: FPLC, Bradford and spectrophotometry at 280 nm. Results showed that whey proteins partitioned unevenly on the phases of the systems used, with α-lactoalbumin (α-La) concentrated in the upper phase and β-lactoglobulin (β-Lg) in the lower. Albumin in PEG–MD systems concentrated in the MD-rich lower phase. Porcine insulin showed great affinity with the PEG-rich phase, its partition coefficient was always over 10 and increases with PEG molecular mass.     

Recovery of laccase from the residual compost of Agaricus bisporus in aqueous two-phase systems

The potential use of aqueous two-phase systems (ATPS) to establish a viable protocol for the recovery of laccase from the residual compost of Agaricus bisporus was evaluated. The evaluation of system parameters such as poly (ethylene glycol) (PEG) molecular mass, concentration of PEG as well as salt and system pH was carried out to determine under which conditions the laccase concentrates predominantly to the top PEG-rich phase. PEG 1000–phosphate ATPS proved to be suitable for the primary recovery of laccase. An extraction ATPS stage comprising volume ratio equal to 1.0, PEG 1000 18.2% (w/w), phosphate 15.0% (w/w), system pH of 7.0 and loaded with 5% (w/w) of crude extract from residual compost allowed the laccase recovery. The use of ATPS resulted in one-single primary recovery stage process that produced an overall yield of 95%. The results reported here demonstrated the potential application of ATPS for the valorisation of residual material and the potential establishment of a downstream process to obtain value added products with commercial application.     

Affinity separation by protein conjugated IgG in aqueous two-phase systems using horseradish peroxidase as a ligand carrier

A novel affinity separation method in an aqueous two-phase system (ATPS) is suggested, using protein conjugated IgG as a ligand. For verification of the proposed approach, horseradish peroxidase (HRP) and human IgG was used as a ligand carrier and affinity ligand, respectively. The partition of the affinity ligand, human IgG, was controlled by the conjugation of HRP. Two ATPSs, one consisting of potassium phosphate (15%, w/w) and polyethylene glycol (PEG, M.W. 1450, 10%, w/w) and the other of dextran T500 (5%, w/w) and PEG (M.W. 8000, 5%, w/w), were used. The conjugated human IgG-HRP favored a PEG-rich top phase, whereas human IgG, rabbit anti-human IgG and goat anti-mouse IgG preferred a salt or dextran-rich bottom phase. Using the conjugated human IgG-HRP, rabbit anti-human IgG was successfully separated into a PEG-rich top phase from the mixture with goat anti-mouse IgG. The appropriate molar ratio between human IgG-HRP and rabbit anti-human IgG was around 3:1 and 1:1 for the salt and dextran-based ATPS, respectively. The dextran-based ATPS showed a better recovery yield and purity than the salt-based ATPS for the range of test conditions employed in this experiment. The yield and purity of the recovered rabbit anti-human IgG were 90.8 and 87.7%, respectively, in the dextran-based ATPS, while those in the salt-based ATPS were 78.2 and 73.2%.     

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

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

Purification and stabilization of ricin B from tobacco hairy root culture medium by aqueous two-phase extraction

Ricin B (RTB), the non-toxic lectin subunit of ricin, is a promising mucosal adjuvant and carrier for use in humans. RTB fusion proteins have been expressed in tobacco hairy root cultures, but the secreted RTB component of these proteins was vulnerable to protease degradation in the medium. Moreover, castor bean purified RTB spiked into tobacco hairy root culture media showed significant degradation after 24 h and complete loss of product after 72 h. Aqueous two-phase extraction (ATPE) was tested for fast recovery of RTB not only to partially purify the protein but also to improve its stability. Two different polyethylene glycol (PEG)/salt/water systems including PEG/potassium phosphate and PEG/sodium sulfate, were studied. RTB was shown to be favorably recovered in PEG/sodium sulfate systems. Statistical analysis indicated that the ionic strength of the system and the sodium sulfate concentration were important in optimizing the partition coefficient of RTB. A selectivity of almost three could be achieved for RTB in optimized systems, and RTB partitioned in the PEG-rich phase exhibited extended stability. Therefore, ATPE was shown to be effective in initial recovery/purification and stabilization of RTB and may hold promise for other unstable secreted proteins from hairy root culture.     

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.     

Production and Partial Purification of Tannase from Aspergillus ficuum Gim 3.6

A novel fungal strain, Aspergillus ficuum Gim 3.6, was evaluated for its tannase-producing capability in a wheat bran-based solid-state fermentation. Thin-layer chromatography (TLC) analysis revealed that the strain was able to degrade tannic acid to gallic acid and pyrogallol during the fermentation process. Quantitation of enzyme activity demonstrated that this strain was capable of producing a relatively high yield of extracellular tannase. Single-factor optimization of process parameters resulted in high yield of tannase after 60 hr of incubation at a pH of 5.0 at 30°C, 1 mL of inoculum size, and 1:1 solid–liquid ratio in the presence of 2.0% (w/v) tannic acid as inducer. The potential of aqueous two-phase extraction (ATPE) for the purification of tannase was investigated. Influence of various parameters such as phase-forming salt, molecular weight of polyethylene glycol (PEG), pH, and stability ratio on tannase partition and purification was studied. In all the systems, the target enzyme was observed to preferentially partition to the PEG-rich top phase, and the best result of purification (2.74-fold) with an enzyme activity recovery of 77.17% was obtained in the system containing 17% (w/w) sodium citrate and 18.18% (w/w) PEG1000, at pH 7.0.     

Liquid-liquid extraction of a Schistosoma mansoni recombinant protein from an Escherichia coli extract in aqueous two-phase system

This work describes the partition of a Schistosoma mansoni tegumental antigen produced by a recombinant Escherichia coli strain using an aqueous two-phase system composed of polyethylene glycol (PEG) and potassium phosphate. The effects of the polymer molecular weight, tie line length and pH on antigen partitioning were investigated. The detection of the antigen in both phases were determined by ELISA. The system composed of PEG 3550 (19.7% w/w) and potassium phosphate (17.7% w/w) led to a yield of 59% and an antigen purification factor of 3 in the PEG-rich phase. It was observed that the antigen partition in ATPS was strongly affected by the pH value and tie line length. In addition, it was possible in a single step, to remove the cell debris, that precipitated at the interface of the system.