Practical application of aqueous two-phase partition to process development for the recovery of biological products

The practical application of aqueous two-phase systems (ATPS) to process development has been exploited for several years for the recovery of biological products. Unfortunately, this has not resulted in an extensive presence of the technique in commercial processes. Some of the main identified reasons for such situation involve the full understanding of the mechanism governing phase formation and the behaviour of solute partitioning in ATPS processes, the cost of phase forming polymers and the necessary extended time to understand the technique for process development. In this review paper, some of the practical disadvantages attributed to ATPS are addressed. The practical approach exploited to design ATPS processes, the application to achieve process integration, the increasing use for the recovery of high-value products and the recent development of alternative low cost ATPS, are discussed. It is proposed that the potential trend in the application of ATPS processes for the recovery of biological products will involve the recovery of high-value bio-particulate products with medical applications. This proposed trend in the application of ATPS will address the urgent need to rapidly and economically bring new biopharmaceutical products to market using scaleable and efficient bioprocess technology.     

Different functional states of ram spermatozoa analysed by partition in an aqueous two-phase system

The surface of spermatozoa plays a critical role in many stages involved in fertilisation. The plasma membrane undergoes important alterations in the male and female reproductive tract, which result in the ability of spermatozoa to fertilise eggs. One of these membrane modifications is sperm capacitation, a process by which sperm interacts with the zona pellucida receptors leading to the acrosome reaction. It has been proposed that the freezing process induces capacitation-like changes to spermatozoa, and that this premature capacitation could explain the reduction in longevity and fertilising capacity of cryopreserved mammalian spermatozoa. Our research focused on the relationship between membrane alterations occurring throughout freezing-thawing and the processes of capacitation and acrosome reaction. We used centrifugal countercurrent distribution (CCCD) analysis to compare the partition behaviour of ram spermatozoa that was either subjected to cold-shock or frozen-thawed with capacitated and acrosome reacted samples. In addition, the effect of the induced acrosome reaction on membrane integrity of ram spermatozoa was studied using biochemical markers and electron microscopy scanning. The CCCD analysis revealed important similarities between the surface characteristics of capacitated and cold-shocked sperm as well as between acrosome-reacted and frozen-thawed sperm. Cold-shocked and capacitated sperm showed an increased cell affinity for the lower dextran-rich phase as well as a decreased heterogeneity. Likewise, the induction of the acrosome reaction resulted in a loss of viability and an important decrease in cell surface heterogeneity compared to the untreated-control sample. Similar surface changes were found when semen samples were frozen with either Fiser or milk-yolk extender. These results confirm those obtained for membrane integrity by fluorescence markers. Thus, the high cell viability value found in the control sample (74.5%) was greatly decreased after cold-shock (22.2%), cryopreservation (26.38% Fiser medium, 24.8% milk-yolk medium) and acrosome reaction (6.6%), although it was preserved after inducing capacitation (46.7%). The study using electron microscopy scanning revealed dramatic structural alterations provoked by the induction of the acrosome reaction.     

Protein partition between the different phases comprising poly(ethylene glycol)-salt aqueous two-phase systems, hydrophobic interaction chromatography and precipitation: a generic description in terms of salting-out effects

The solution behaviour of selected proteins has been studied under conditions promoting precipitation, binding to mildly hydrophobic adsorbents or partition. Solvophobic theory may be used to describe these forms of protein partition. The tendency of a protein to partition therein is dependent upon surface properties of the protein solute mediated by the concentration and nature of added salts. As applied to partitioning in poly(ethylene glycol) (PEG)-salt systems this implies that linear (Brönsted) relationships apply only to proteins partitioned close to the critical point. At longer tie-line lengths protein partitioning is increasingly influenced by salting-out forces. This is confirmed by the observed behaviour of the proteins. The point at which this behaviour changes has been unambiguously defined enabling the direct comparison of phase transition of proteins during partition in all systems. The results obtained show that phase transition during adsorption and partition occur at similar concentrations of salt. This is less than that required to promote precipitation. It appears, from these limited studies, that top-phase preferring proteins are partitioned at salt concentrations above those required to cause adsorption. Proteins preferring the lower phase are partitioned at salt concentrations close to or below those required for adsorption. This raises questions regarding the solvated molecular form of the partitioned proteins and the definition of the partition coefficient.     

Aqueous two-phase systems with a liquid protein (bovine serum albumin) phase for partitioning of enzymes

New aqueous liquid-liquid two-phase systems based on bovine serum albumin and sodium thiocyanate in combination with either poly(vinyl alcohol) or poly(ethylene glycol) were investigated. Phase diagrams are presented. Lactate dehydrogenase and some mitochondrial enzymes were partitioned in the systems. All the phase components used influenced, either positively or negatively, the activity of lactate dehydrogenase. The enzymes showed a strong preference for the albumin phase. Possible scientific and biotechnological uses are discussed.     

A single partitioning step in aqueous polymer two-phase systems reduces hypotonized rat erythrocyte heterogeneity

Rat carrier erythrocytes prepared by hypotonic dialysis (80 mOsm/kg) are a heterogeneous cell population that can be fractionated into two-well-defined cell subpopulations by a single partition step, in charge-sensitive dextran-poly(ethylene glycol) aqueous two-phase systems. One subpopulation (65% of total cells) has a decreased cell surface charge and is partitioned at the interface in a single step and then fractionated by counter-current distribution as a low-G subpopulation. The other subpopulation (35% of total cells) has charge surface properties more like those of the untreated control rat erythrocytes. These last cells are partitioned in the top phase in a single step and then fractionated by counter-current distribution as a high-G subpopulation. Partitioning is more effective in reducing cell heterogeneity in hypotonized rat erythrocyte populations than is density separation in Ficoll-paque which only separates a small less dense cell subpopulation (5% of total cells), with the most fragile cells, from a larger and more dense cell subpopulation (95% of total cells), with a mixture of fragile and normal cells. This simple cell separation procedure quickly reduces carrier erythrocyte heterogeneity in a single partitioning step so it can be used to prepare cells for in vivo studies.     

Fractionation of wheat proteins by counter-current distribution using aqueous two-phase systems containing propionic acid

Wheat proteins, soluble in diluted acid (glutenins), have been fractionated by counter-current distribution (CCD) using an aqueous two-phase system. The phase system is based on poly(ethylene glycol) and dextran but contains also 1% propionic acid and 6 mM magnesium sulfate. Approximately half of the bulk proteins partitioned to the upper phase while starch and other particles were recovered only into the lower phase. Whole wheat flour could be applied as sample for the CCD and 57 transfers were carried out. Starch and insoluble proteins remained stationary, while proteins followed the mobile phase to various degrees giving rise to a distribution pattern. The CCD pattern of the proteins showed distinct differences when various kinds of wheat flour were analysed. The patterns indicate that at least six subpopulations of proteins can be obtained by using two-phase extraction.     

Aqueous two-phase systems

Biphasic systems formed by mixing of two polymers or a polymer and a salt in water can be used for separation of cells, membranes, viruses, proteins, nucleic acids, and other biomolecules. The partitioning between the two phases is dependent on the surface properties and conformation of the materials, and also on the composition of the two-phase system. The mechanism of partitioning is, however, complex and not easily predicted. Aqueous two-phase systems (ATPS) have proven to be a useful tool for analysis of biomolecular and cellular surfaces and their interactions, fractionation of cell populations, product recovery in biotechnology, and so forth. Potential for environmental remediation has also been suggested. Because ATPS are easily scalable and are also able to hold high biomass load in comparison with other separation techniques, the application that has attracted most interest so far has been the large-scale recovery of proteins from crude feedstocks. As chemicals constitute the major cost factor for large-scale systems, use of easily recyclable phase components and the phase systems generated by a single-phase chemical in water are being studied.     

Purification of hyperthermophilic archaeal amylolytic enzyme (MJA1) using thermoseparating aqueous two-phase systems

Purification of a recombinant, thermostable alpha-amylase (MJA1) from the hyperthermophile, Methanococcus jannaschii, was investigated in the ethylene oxide-propylene oxide random copolymer (PEO-PPO)/(NH(4))(2)SO(4), and poly(ethylene glycol) (PEG)/(NH(4))(2)SO(4) aqueous two-phase systems. MJA1 partitioned in the top polymer-rich phase, while the remainder of proteins partitioned in the bottom salt-rich phase. It was found that enzyme recovery of up to 90% with a purification factor of 3.31 was achieved using a single aqueous two-phase extraction step. In addition, the partition behavior of pure amyloglucosidase in polymer/salt aqueous two-phase systems was also evaluated. All of the studied enzymes partitioned unevenly in these polymer/salt systems. This work is the first reported application of thermoseparating polymer aqueous two-phase systems for the purification of extremophile enzymes.     

Ucon-benzoyl dextran aqueous two-phase systems: protein purification with phase component recycling

Benzoyl dextran with a degree of substitution of 0.18 was synthesized by reacting dextran T500 with benzoyl chloride. A new type of aqueous two-phase system composed of benzoyl dextran as bottom phase polymer and the random copolymer of ethylene oxide and propylene oxide (Ucon 50-HB-5100) as top phase polymer has been formed. The phase diagram for the system Ucon 50-HB-5100-benzoyl dextran with a degree of substitution of 0.18 was determined at room temperature. This two-phase system has been used to purify 3-phosphoglycerate kinase from bakers' yeast. The top-phase polymer (Ucon) can be separated from target enzyme by increasing the temperature. The bottom-phase polymer (benzyol dextran) could be recovered by addition of salt. Yeast homogenate was partitioned in a primary Ucon 50-HB-5100-benzoyl dextran aqueous two-phase system. After phase separation the top phase was removed and temperature-induced phase separation was used for formation of a water phase and a Ucon-rich phase. The benzoyl dextran-enriched bottom phase from the primary system was diluted, and the polymer was separated from water by addition of Na₂SO₄.     

Separation and purification of methoxypoly(ethylene glycol) grafted red blood cells via two-phase partitioning

Alloimmunization to donor blood group antigens remains a significant problem in transfusion medicine. To attenuate the risk of alloimmunization, we have pioneered the membrane grafting of methoxypoly(ethylene glycol) (mPEG) to produce immunocamouflaged red blood cells (RBC). Grafting of the mPEG was accomplished using cyanuric chloride activated mPEG (CmPEG; M(r) = 5000), benzotriazole carbonate methoxyPEG (BTCmPEG; M(r) = 2000, 5000 or 20000); or N-hydroxysuccinimidyl ester of mPEG propionic acid (SPAmPEG; M(r) = 5000, or 20000). Because of the heterogeneity of grafting, a crucial tool in developing the stealth RBC is an ability to purify the modified RBC from unmodified (immunogenic) donor cells. As demonstrated, a (5, 4) dextran:PEG aqueous two-phase polymer partitioning system cleanly separated the immunologically silent mPEG-grafted human RBC from control or lightly modified cells. Cell mixing experiments employing varying ratios of mPEG-modified and control RBC confirmed the purification efficacy of the phase partitioning system. Proportional changes in PEG-rich phase partitioning were achieved by increasing either the quantity of surface mPEG or the mPEG molecular weight. The biological viability of purified mPEG-RBC (BTCmPEG; [M(r) = 20000) was demonstrated by their normal in vivo survival at immunoprotective grafting concentrations (相似文献   

Pectinase partitioning in polyethylene glycol 1000/Na2SO4 aqueous two-phase system: statistical modeling of the experimental results

Statistical models concerning partitioning of pectinase in polyethylene glycol 1000/Na₂SO₄ aqueous two-phase system were established with response surface methodology. Concentrations of polyethylene glycol 1000 and Na₂SO₄ were selected as independent variables to evaluate their impact on parameters of partitioning in aqueous two-phase system—the partition coefficient of pectinase, purification factor and pectinase yield. An experimental space where over 2.5-fold purification was achieved, followed by over 90% yield of pectinase. The established models showed good prediction of partitioning parameters.     

Aqueous two-phase fractionation of biological suspensions for protein recovery from bovine blood

The practical application of a two-stage aqueous two-phase systems (ATPS) for the fractionation and recovery of proteins from biological suspensions is described. A model process for the recovery of proteins from whole bovine blood was selected to study the implementation of an ATPS process. Recycling of used PEG into the initial extraction stage did not significantly influence the partition behaviour of serum albumin in subsequent cycles. © Rapid Science Ltd. 1998     

Ovomucoid partitioning in aqueous two-phase systems

This study evaluated the partitioning of ovomucoid from egg white, in aqueous two-phase systems (ATPS) composed of PEG 1500 and inorganic salt (lithium sulfate, sodium sulfate, magnesium sulfate, sodium carbonate or sodium citrate) at 25 °C. The results showed a great effect of the electrolyte nature on the partition coefficient. The partition coefficient value ranges from 0.02 to 6.0. The highest partition coefficients were obtained from systems composed of sodium carbonate and the lowest in systems composed of magnesium sulfate. In the system containing magnesium sulfate, a recovery percentage greater than 90% was obtained.     

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.     

Recovery in aqueous two-phase systems of lutein produced by the green microalga Chlorella protothecoides

The objective of this study was to develop a chromatographic method for the analysis of the anti-androgen vinclozolin (V) and its metabolites 2-[[(3,5-dichlorophenyl)-carbamoyl]oxy]-2-methyl-3-butenoic acid (M1), 3',5'-dichloro-2-hydroxy-2-methylbut-3-enanilide (M2) and 3,5-dichloroaniline (M3) in rat serum. V, M1-M3 were resolved using an HPLC gradient program with a mobile phase consisting of 60-75% methanol:acetonitrile (70:30) and 0.05 M monobasic sodium phosphate buffer pH 3.3 at 1 ml/min, a C18 column, and monitored at 212 nm. Incubates of 0.01 M monobasic potassium phosphate buffer (PB) pH 7.4 and rat serum were spiked with V and its metabolites and processed by diluting samples (1:4) with 0.1M PB pH 3.3, to limit methodological hydrolysis of analytes, followed by addition of acetonitrile. Recoveries of V, M1 and M2 ranged from 85 to 105%, whereas recovery of M3 was <25%. V was hydrolyzed to M1 and M2 after incubation in PB pH 7.4 and rat serum, with M1 the predominant metabolite. This method was successfully applied in the analysis of V and its metabolites in the serum of a male rat after oral administration of V (100 mg/kg).     

Aggregation and denaturation of antibodies: a capillary electrophoresis, dynamic light scattering, and aqueous two-phase partitioning study

Protein denaturation and aggregation are well-known problems in the pharmaceutical industry. As the protein aggregates, it loses its biological activity and creates problems in its administration to patients. In this paper, we explore the use of aqueous two-phase systems, capillary zone electrophoresis, and dynamic light scattering for the monitoring of protein denaturation and aggregation. Our studies focus on human IgG and HSA. Capillary zone electrophoresis was used to monitor changes in the charge to size ratio of the proteins upon denaturation and dynamic light scattering was used to detect the presence of any aggregates and to monitor the size of the proteins. The information obtained from aqueous two-phase partitioning is similar to that obtained from capillary zone electrophoresis. The simplicity of aqueous two-phase system and its low cost (compared to the other analytical techniques) suggest that it can be routinely used for the quality control of some pharmaceutical preparations.     

Surface changes associated with ram sperm cryopreservation revealed by counter-current distribution in an aqueous two-phase system effect of different cryoprotectants

Ram sperm was frozen in the presence of the most commonly used cryoprotectants. After thawing, the overall cell surface changes provoked by freezing were assessed by centrifugal counter-current distribution (CCCD). In addition, cell membrane integrity (viability) of all the treated sperm was estimated by fluorescent staining. Fresh and refrigerated sperm were used as controls. Our results show no improvement of the cooling-induced cell surface damage by freezing in the presence of bovine seminal plasma, proline, glycine-betaine and phosphatidylcholine. Better results were obtained with vitamin E and cholesterol. However, the best protective effects were found by employing seroalbumin and lactalbumin. Furthermore, freezing in the presence of bovine lactalbumin resulted in a good maintenance of the cellular viability and of the CCCD heterogeneity in respect to fresh cells.     

Metal ion separations in polyethylene glycol-based aqueous biphasic systems: correlation of partitioning behavior with available thermodynamic hydration data

Solvent extraction, utilizing an oil-water mixture (e.g, chloroform-water) and a suitable complexant, is a proven technology for the selective removal and recovery of metal ions from aqueous solutions. Aqueous biphasic systems (ABS), formed by mixing certain inorganic salts and water-soluble polymers, or by mixing two dissimilar water-soluble polymers, have been studied for more than 40 years for the gentle, non-denaturing separation of fragile biomolecules, yet ABS have been virtually ignored as a possible extraction technology for metal ions. In this report we review our metal ion partitioning work and discuss the three major types of partitioning: (1) those rare instances that the metal ion species present in a given solution partitions to the PEG-rich phase without an extractant; (2) the use of halide salts which produce a metal anion complex that partitions to the PEG-rich phase; and (3) the use of a water-soluble extractant which distributes to the PEG-rich phase. In addition, we correlate the partitioning behavior we observed with available thermodynamic data for metal ions and their complexes.     

Bioprocess intensification: a potential aqueous two-phase process for the primary recovery of B-phycoerythrin from Porphyridium cruentum

A process for the primary recovery of B-phycoerythrin from Porphyridium cruentum exploiting aqueous two-phase systems (ATPS) was developed in order to reduce the number of unit operations and benefit from an increased yield of the protein product. The evaluation of system parameters such as poly(ethylene glycol) (PEG) molecular mass, concentration of PEG as well as salt, system pH and volume ratio was carried out to determine under which conditions the B-phycoerythrin and contaminants concentrate to opposite phases. PEG 1450-phosphate ATPS proved to be suitable for the recovery of B-phycoerythrin because the target protein concentrated to the top phase whilst the protein contaminants and cell debris concentrated in the bottom phase. An extraction ATPS stage comprising volume ratio (Vr) equal to 1.0, PEG 1450 24.9% (w/w), phosphate 12.6% (w/w) and system pH of 8.0 allowed B-phycoerythrin recovery with a purity of 2.9 (estimated as the relation of the 545-280 nm absorbances). The use of ATPS resulted in a primary recovery process that produced a protein purity of 2.9 +/- 0.2 and an overall product yield of 77.0% (w/w). The results reported demonstrated the practical implementation of ATPS for the design of a primary recovery process as a first step for the commercial purification of B-phycoerythrin produced by P. cruentum.