Evaluation of recombinant phenylalanine dehydrogenase behavior in aqueous two-phase partitioning

Recombinant Bacillus sphaericus phenylalanine dehydrogenase (PheDH) partitioning was studied in polyethylene glycol (PEG) and ammonium sulfate aqueous two-phase systems (ATPS). The objectives of this work were to investigate influences; varying the molecular mass and concentration of PEG, pH, phase volume ratio (V_R), tie-line length (TLL) and concentration of (NH₄)₂SO₄ on the partition behavior of PheDH. It was revealed that the partitioning was not affected by V_R, while PEG molecular mass and concentration and (NH₄)₂SO₄ concentration had significant effects on enzyme partitioning. Longer TLL and higher pH resulted in better partitioning into the top phase. Under the most favorable partition conditions with 8.5% (w/w) PEG-6000, 17.5% (w/w) (NH₄)₂SO₄ and V_R = 0.25 at pH 8.0, partition coefficient (K_E), recovery (R%), yield (Y%) and TLL were achieved 58.7%, 135%, 94.42% and 39.89% (w/w), respectively. Overall, the promising results obtained in this research indicated that the ATPS partitioning can be provided an efficient and powerful tool for recovery and purification of recombinant PheDH.     

Purification of recombinant phenylalanine dehydrogenase by partitioning in aqueous two-phase systems

This study presents the partitioning and purification of recombinant Bacillus badius phenylalanine dehydrogenase (PheDH) in aqueous two-phase systems (ATPS) composed of polyethylene glycol 6000 (PEG-6000) and ammonium sulfate. A single-step operation of ATPS was developed for extraction and purification of recombinant PheDH from E. coli BL21 (DE3). The influence of system parameters including; PEG molecular weight and concentration, pH, (NH(4))(2)SO(4) concentration and NaCl salt addition on enzyme partitioning were investigated. The best optimal system for the partitioning and purification of PheDH was 8.5% (w/w) PEG-6000, 17.5% (w/w) (NH(4))(2)SO(4) and 13% (w/w) NaCl at pH 8.0. The partition coefficient, recovery, yield, purification factor and specific activity values were of 92.57, 141%, 95.85%, 474.3 and 10424.97 U/mg, respectively. Also the K(m) values for L-phenylalanine and NAD(+) in oxidative deamination were 0.020 and 0.13 mM, respectively. Our data suggested that this ATPS could be an economical and attractive technology for large-scale purification of recombinant PheDH.     

Partitioning of host and recombinant cells in aqueous two-phase polymer systems

The separation of host and recombinant Escherichia coli bacterial cells has been studied using the surface-sensitive technique of partitioning in aqueous two-phase polymer systems. Experiments were designed to probe charge-and hydrophobicity-related property differences of antibiotic-resistant recombinant cells and their antibiotic-sensitive hosts. Differential partitioning was observed in both charge-sensitive and non-charge-sensitive phase systems for three host-recombinant cell systems, but the non-charge-related effects appear to have a greater impact on partitioning behavior. This result suggests that plasmid-encoded products related to antibiotic resistance modify the surface hydrophobicity of the E. coli bacterial cell and that these differences can be exploited for cell separation.     

Improved partitioning in aqueous two-phase system of tyrosine-tagged recombinant lactate dehydrogenase

The partitioning of Bacillus stearothermophilus lactate dehydrogenase (LDH) in an aqueous two-phase system was studied. Particularly, the influence of tyrosine tags on the partitioning was evaluated. The hydrophobic effect, caused by the addition of tyrosine residues, was determined in a system based on dextran and the thermoseparating ethylene oxide-propylene oxide random copolymer (EO30PO70). Five different LDH variants were constructed with N-terminal tags containing tyrosines (Y3 and Y6), tyrosines and prolines (Y3P2 and Y6P2), and only prolines (P2). LDH fused with tags containing tyrosines increased the partitioning coefficient, and the more tyrosines added to the protein, the larger improvement in partitioning. When prolines were added between the tyrosine-rich tag and the protein, a further increased partitioning was obtained. The enhanced partitioning was attributed to the rigid structure of the proline, which in turn led to an increase in the exposure of the tag to the surroundings. The best tyrosine tag, Y6P2, increased the partition coefficient four times and additionally, a higher thermostability was observed.     

Simultaneous quantification of polymer and salt in polyethylene glycol / phosphate aqueous two-phase systems by HPLC

Summary A simple method for the determination of phase composition in polyethylene glycol / phosphate aqueous biphasic systems was developed. A single HPLC analysis allows the simultaneous quantification of polymer and salt in the top phase. Phosphate concentration in the bottom phase was also accurately determined but the method was not sensitive enough for PEG quantification in this phase.     

Impact of cell disruption and polymer recycling upon aqueous two-phase processes for protein recovery

A practical study is presented of the influence of cell debris and polymer recycling upon the operation of two-stage acqueous two-phase systems (ATPS) for the recovery of yeast bulk protein, pyruvate kinase and fumarase. Brewers' yeast was disrupted using one of two types of high-pressure homogenisers or a bead mill. The different cell debris suspensions were partitioned in a single PEG-phosphate ATPS extraction and the efficiency of solid-liquid separation was examined. A continuously operated two-stage ATPS process, using spray columns, is presented and practical problems of polymer recycling are discussed. Conclusions are drawn concerning the generic implementation and operational stability of ATPS in practical protein recoveries.     

Aqueous two-phase extraction for downstream processing of amyloglucosidase

A polymer/salt aqueous two-phase system has been successfully employed for separation and purification of amyloglucosidase. The effects of system pH, molecular weight of polymer and composition of the two-phase system on amyloglucosidase partition behaviour in polyethylene glycol (PEG 4000, 6000)/disodium hydrogen phosphate were investigated. Experimental data are explained based on Kim's theoretical model for the prediction of biomolecule partitioning in a PEG/salt system.     

Integration of bioconversion and downstream processing: starch hydrolysis in an aqueous two-phase system

Integration of bioconversion and the first step(s) of down stream processing can be used as a means to increase the productivity of bioprocesses. This integration also gives the possibility to run the bioconversion in a continuous mode. We demonstrate the use of an aqueous two-phase system in combination with ultrafiltration to accomplish this. Conversion of native starch to glucose by alpha-amylase and glucoamylase was carried out in an aqueous two-phase system in connection with a membrane filtration unit. In this way, a continuous stream of glucose in buffer solution was obtained; the phase-forming polymers as well as the starch-degrading enzymes were recycled, and clogging of the ultrafiltration membrane was avoided. The process was carried out continuously in a mixer-settler reactor for a period of 8 days. The enzyme activities in the top and bottom phases and in the mixing chamber were monitored intermittently throughout the experiment. The optimum pH, temperature, and ionic strength for the activity of the enzyme mixture were determined. The settling time of phase systems containing varying amounts of PEG, crude dextran, and solid starch was studied. The activity and stability of enzyme mixtures was studied both in buffer medium and in the medium containing the polymers. The enzymes were found to be more active and stable in medium containing polymers than in the buffer solutions.     

Surface charge engineering of PQQ glucose dehydrogenase for downstream processing

The ion-exchange chromatography behavior of recombinant glucose dehydrogenase harboring pyrroloquinoline quinone (PQQGDH) was modified to greatly simplify its purification. The surface charge of PQQGDH was engineered by either fusing a three-arginine tail to the C-terminus of PQQGDH (PQQGDH+Arg3) or by substituting three residues exposed on the surface of the enzyme to Arg by site-directed mutagenesis (3RPQQGDH). During cation exchange chromatography, both surface charge-engineered enzymes eluted at much higher salt concentrations than the wild-type enzyme. After the chromatography purification step, both PQQGDH+Arg3 and 3RPQQGDH appeared as single bands on SDS-PAGE, while extra bands appeared with the wild-type protein sample. Although all tested kinetic parameters of both engineered enzymes are similar to those of wild type, both modifications resulted in enzymes with increased thermal stability. Our achievements have resulted in the greater production of an improved quality PQQGDH by a simplified process.     

Choice of an aqueous polymer two-phase system for cell partition

Partition of human erythrocytes in aqueous two-phase polymer systems produced by Ficoll and different molecular weight fractions of dextran and polyethylene glycol and the influence of the ionic composition on the cells' partition in the systems was studied. It is found that the Ficoll-dextran-40 system is characterized by a number of advantages as compared with the common dextran-polyethylene glycol system or the others systems under study. The main advantage of the system appears to be that it is possible to concentrate the red cells in the top phase or in the bottom phase of the system, depending on the system ionic composition. The influence of the nature and the concentration of salt additives on this two-phase system formation is examined.     

Purification of glucosyltransferase from cell-lysate of Streptococcus mutans by counter-current chromatography using aqueous polymer two-phase system

Counter-current chromatography (CCC) using a cross-axis coil planet centrifuge (X-axis CPC) was applied to the purification of glucosyltransferase (GTF) from a cell-lysate of cariogenic bacteria. The purification was performed using an aqueous polymer two-phase system composed of 4.4% (w/w) polyethylene glycol (PEG) 8000-6% (w/w) dextran T500 containing 10mM phosphate buffer at pH 9.2 by eluting the upper phase (UP) at 1.0ml/min. The bacterial GTF in the cell-lysate of Streptococcus mutans was selectively retained in the dextran-rich lower stationary phase. The column contents were diluted and subjected to hydroxyapatite (HA) chromatography to remove the polymers from the GTF. Fractions eluted with 500mM potassium phosphate buffer were analyzed by GTF enzymatic activity as well as sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE). The GTF purity in the final product was increased about 87 times as that in the cell-lysate with a good recovery rate of about 79% through this purification process.     

Enrichment separation of recombinant human CCR3 using detergent/polymer two-phase system

Studies on the structure and functions of membrane proteins are impeded by their lability, hydrophobicity, difficulty in purification and low yields. Human chemokine receptor 3 (CCR3) is a G protein-coupled receptor related to allergic diseases. A Triton X-100/PEG20000 two-phase system was employed for enrichment separation of CCR3 over-expressed in E. coli. Optimal CCR3 partitioning with partition coefficient around 8 was obtained at pH 7.0, ionic strength of 0.3 mol/kg and 3 h equilibration time. Total recovery of CCR3 reached 102 ± 15%, which was much higher than 32 ± 5% of the normally used ultracentrifugation method. The recovered CCR3 was finally purified by two chromatography steps giving a final protein of 87 kDa.     

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.     

Optimization of conditions for bacteriocin extraction in PEG/salt aqueous two-phase systems using statistical experimental designs

The bacteriocin nisin was extracted in PEG/salt aqueous two-phase systems (ATPS) using the property that the systems can extract hydrophobic proteins. The concentrations of the phase-forming components, PEG 4000 and Na(2)SO(4), were optimized for nisin recovery by means of statistical experimental designs, and it was found that they strongly influenced nisin recovery. The optimal composition of ATPS was found to be 15.99% (w/w) PEG 4000 and 15.85% (w/w) Na(2)SO(4) (pH 2), and the optimal ATPS allowed an 11.60% increase of nisin recovery compared to the standard method of nisin assay.     

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.     

Investigation of mathematical methods for efficient optimisation of aqueous two-phase extraction

Mathematical strategies were applied to optimise the extraction of recombinant leucine dehydrogenase from E. coli homogenates and endoglucanase 1 from culture filtrates of Trichoderma reesei in polyethylene glycol–phosphate systems. The goal was to test mathematical tools which could facilitate the optimisation procedure in aqueous two-phase systems. A modified simplex approach, the method of steepest ascent and a genetic algorithm were successfully applied and compared. The methods differ in the height of the optimum found, the number of experiments and the time required. The genetic algorithm proved to be an optimisation procedure which can be used well in aqueous two-phase systems. The simplex procedure has to be further improved.     

Distribution of free and antibody-bound peptide hormones in two-phase aqueous polymer systems

Peptide hormones labelled with radioactive iodine were partitioned into the aqueous two-phase polymer systems developed by Albertsson (1960) and the conditions required for separation of free from antibody-bound hormone have been worked out. Hormones studied included insulin, growth hormone, parathyroid hormone and [arginine]-vasopressin. Free and antibody-bound hormones show different distribution coefficients in a number of systems tested; two systems, the dextran-polyethylene glycol and dextran sulphate-polyethylene glycol system, give optimum separation. Free hormones distribute readily into the upper phase of these systems, whereas hormone-antibody complexes, as well as uncombined antibody, are found almost completely in the lower phase. Various factors including the polymer concentration, the ionic composition of the system, the nature of the hormone and the nature of added serum protein differentially affect the distribution coefficients for free and antibody-bound hormone. These factors can be adequately controlled so as to improve separation. The two-phase partition method has been successfully applied to measure binding of labelled hormone to antibody under standard radioimmunoassay conditions. It exhibits several advantages over the method of equilibration dialysis and can be applied to the study of non-immunological interactions.     

Large scale production and downstream processing of a recombinant porcine parvovirus vaccine

Porcine parvovirus (PPV) virus-like particles (VLPs) constitute a potential vaccine for prevention of parvovirus-induced reproductive failure in gilts. Here we report the development of a large scale (25 l) production process for PPV-VLPs with baculovirus-infected insect cells. A low multiplicity of infection (MOI) strategy was efficiently applied avoiding the use of an extra baculovirus expansion step. The optimal harvest time was defined at 120 h post-infection at the MOI used, with the cell concentration at infection being 1.5x10(6) cells/ml. An efficient purification scheme using centrifugation, precipitation and ultrafiltration/diafiltration as stepwise unit operations was developed. The global yield of the downstream process was 68%. Baculovirus inactivation with Triton X-100 was successfully integrated into the purification scheme without an increase in the number of process stages. Immunogenicity of the PPV-VLPs tested in guinea pigs was similar to highly purified reference material produced from cells cultured in the presence of serum-containing medium. These results indicate the feasibility of industrial scale production of PPV-VLPs in the baculovirus system, safety of the product, and the potency of the product for vaccine application.     

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.