Physical and rheological characterisation of polyethylene glycol-cashew-nut tree gum aqueous two-phase systems

The characterisation of the polyethylene glycol-cashew-nut tree gum aqueous two-phase system is described. Factors which affect the phase diagram including polymer molecular mass, pH and temperature were analysed. The physico-chemical properties of the system such as density, viscosity, volume ratio and phase separation times were also described. The characteristics of the system studied indicate it to be very attractive as a separation technique.     

Evaluation of viscosities of polymer-water solutions used in aqueous two-phase systems

The dynamic viscosities of dilute aqueous poly(ethylene glycol) and dextran, and poly(ethylene glycol)-dextran-water solutions have been measured. The poly(ethylene glycol) and dextran samples had average molecular masses of 8000 Da and 580 000 Da, respectively. To estimate the values of viscosity of poly(ethylene glycol)-dextran-water solutions, a Grunberg like equation has been proposed which takes into account the influence of poly(ethylene glycol) and dextran concentrations. The relative errors vary between 0.76 and 11.64 in absolute value.     

Evaluation of the effects of the parameters involved in the purification of clavulanic acid from fermentation broth by aqueous two-phase systems

The purification of clavulanic acid (CA), which is an important β-lactam antibiotic produced by submerged cultivation of Streptomyces clavuligerus, was studied through the use of phosphate and polyethylene glycol-based aqueous two-phase systems. The parameters’ effect on the yield and purification was evaluated through an experimental design and the preliminary results showed that the polyethylene molecular mass and tie-line length and phase volume ratio exerted the strongest effect on the yield and distribution coefficient in the range tested. In addition, the response surface methodology was used to optimize the distribution coefficient, yield, and purification factor. The optimal conditions of yield and purification factor are in the regions where polyethylene has a low molecular mass, pH close to the isoelectric point, and lower top phase volume. A 100% yield and a 1.5-fold purification factor are obtained when extracting CA by maximizing the conditions of an aqueous two-phase system.     

On the kinetics of phase separation in aqueous two-phase systems

The effect of the tie-line location (phase volume ratio) on the kinetics of phase separation in batch PEG/salt aqueous two-phase systems (ATPS) has been investigated. PEG/sulphate systems with a stability ratio (sr) of 0.34 and 0.37 and relative tie-line lengths in the range 0.1 to 0.6 for a continuous top phase and in the range 0.03 to 0.15 for a continuous bottom phase were used in the batch studies. A continuous settler was designed with three different inlet geometries. Phase separation is much faster when the bottom phase is continuous and in this case the location on the tie-line and the presence or absence of Bacillus subtilis extract makes little difference. When the top phase is continuous the relative sizes of the phases (phase ratio, R, relative distance on tie-line, rd) has an important effect, the larger the top phase (larger R and rd) the slower the phase separation. The presence of Bacillus extract also makes the operation slower which is more marked at the largest values of R (and rd). At the largest volume ratios (R or rd) three different settling regions have been recognised, a region of coalescence, a region of drops moving to the interphase and a region where drops queue at the interphase to coalesce into the large phase. A modified correlation that takes into account the location on the tie-line and thus volume ratio (R) and relative distance (rd) has been proposed and successfully tested. The behavior of batch and continuous systems in the presence and absence of Bacillus subtilis extract in systems with continuous bottom phase was also studied. The settling velocity was lower in the continuous than in the batch systems, and in both cases the initial rate was lower in the presence of Bacillus extract.     

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   

Application of surface response analysis to the optimization of penicillin acylase purification in aqueous two-phase systems

Penicillin acylase purification from an Escherichia coli crude extract using PEG 3350–sodium citrate aqueous two-phase systems (ATPS) was optimized. An experimental design was used to evaluate the influence of PEG, sodium citrate and sodium chloride on the purification parameters. A central composite design was defined centred on the previously found conditions for highest purification from an osmotic shock extract. Mathematical models for the partition coefficient of protein and enzyme, balance of protein and enzyme, yield and purification were calculated and statistically validated. Analysis of the contours of constant response as a function of PEG and sodium citrate concentrations for three different concentrations of NaCl revealed different effects of the three factors on the studied parameters. A maximum purification factor of 6.5 was predicted for PEG 3350, sodium citrate and NaCl concentrations of 15.1, 11.0 and 8.52% respectively. However, under these conditions the predicted yield was 61%. A better compromise between these two parameters can be found by superimposing the contour plots of the purification factor and yield for 10.3% NaCl. A region in the experimental space can be defined where the purification factor is always higher than 5.5 with yields exceeding 80%.     

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.     

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.     

Characterization of storage cell wall polysaccharides from Brazilian legume seeds and the formation of aqueous two-phase systems

Cell wall storage polysaccharides from Brazilian legume seeds of Dimorphandra mollis, Schizolobium parahybum (galactomannans), Copaifera langsdorffii, Hymenaea courbaril (xyloglucans) and the galactan from cotyledons of the Mediterranean species Lupinus angustifolius were extracted and their apparent molecular masses were determined by high-performance size exclusion chromatography analysis. They were, to a large degree, polydisperse, showing molecular masses that varied from 100 000 to 2 000 000. Polyethylene glycol (PEG, 1500, 4000, 6000 and 8000), sodium citrate and dextran (73 000, 60 000–90 000, 505 000 and 2 000 000) were used for investigating phase formation with the seed polysaccharides. Galactomannans and xyloglucans demonstrated phase formation with sodium citrate concentrations lower than 30%, as well as dextrans and polyethylene glycol, and formed gels in the presence of high concentrations of sodium citrate (above 30%). Galactan did not promote phase formation with any of the reagents used. On the basis of the results obtained, the possibility of using legume seed polysaccharides for the partitioning and purification of polysaccharide enzymes in aqueous two-phase systems is suggested.     

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).     

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.     

Production,extraction, and thermodynamics protease partitioning from Aspergillus tamarii Kita UCP1279 using PEG/sodium citrate aqueous two-phase systems

Abstract

The protease from Aspergillus tamarii Kita UCP1279 extraction by aqueous two-phase PEG-Citrate (ATPS) systems, using a factorial design 2⁴, was investigated. Then, the variables studied were polyethylene glycol (PEG) molar mass (M_PEG), concentrations of PEG (C_PEG) and citrate (C_CIT), and pH. The responses analyzed were the partition coefficient (K), activity yield (Y) and purification factor (PF). The thermodynamic parameters of the ATPS partition were estimated as a function of temperature. ATPS was able to pre-purify the protease (PF = 1.6) and obtained 84% activity yield. The thermodynamic parameters ΔG°_m (?10.89?kJ mol^?1), ΔH_m (?5.0?kJ?mol^?1) and partition ΔS_m (19.74?J mol^?1 K^?1) showed that the preferential migration of almost all protein contaminants of the crude extract to the salt-rich phase, while the preferred protease was the PEG rich phase. The extracted enzyme presents optimum temperature and pH at range of 40–50?°C and 9.0–11.0, respectively. Moreover, the enzyme was identified as serine protease based on inhibition profile. ATPS showed the satisfactory performance as the first step for Aspergillus tamarii Kita UCP1279 protease pre-purification.     

Cutinase purification on poly(ethylene glycol)–hydroxypropyl starch aqueous two-phase systems

The partition behaviour of cutinase on poly(ethylene glycol) (PEG)–hydroxypropyl starch aqueous two-phase systems was characterized. The effect of molecular mass of PEG, the pH of the system and tie-line length on cutinase partition coefficient and cutinase yield to the top phase was investigated for systems prepared with a purified hydroxypropyl starch (Reppal PES 100) and a crude one (HPS). The effect of the presence of different salts, such as sodium chloride, sodium sulphate and ammonium sulphate, on cutinase partition was also studied. The results lead to the conclusion that aqueous two-phase systems composed of PEG and hydroxypropyl starch are not efficient in the purification of cutinase. In the majority of cases, the partition coefficients were very close to 1, with pH being the factor which affects most cutinase partition. Partition coefficients were significantly improved when salts were added to the systems. For PEG 4000–Reppal PES 100 [at pH 4.0; 0.5 M (NH₄)₂SO₄], the partition coefficient for cutinase was 3.7, while a value of 12 was obtained for PEG 4000–HPS (at pH 4.0; 1 M NaCl). An isoelectric point (pI) of 7.8 was confirmed for cutinase by constructing a cross partition graphic from the results obtained in the experiments with different salts.     

Evaluation of viscosities of aqueous two-phase systems containing protein

The dynamic viscosities of aqueous polyethylene glycol, aqueous bovine serum albumin, and polyethylene glycol-bovine serum albumin-water solutions were measured at temperatures of 15, 20, 25, 30 and 35 degree C. To estimate the viscosity values of polyethylene glycol-bovine serum albumin-water solutions, a one parameter Grunberg-like model which was satisfactorily used earlier by the present author for polyethylene glycol-dextran-water solutions was employed. The disposable parameter a for our temperature range was estimated as 3.71. The relative errors varying from 0.29 to 18.98 in absolute value indicates that the Grunberg-like model works perfectly for polymer-protein solutions as well.     

Physico-chemical features of solvent media in the phases of aqueous polymer two-phase systems

Solvent polarity and pH in the coexisting aqueous phases of aqueous dextran-poly(ethylene glycol) and dextran-Ficoll two-phase systems of varied polymer concentrations were examined using the solvatochromic technique and potentiometric measurements, respectively. The relative solvent polarity of the phases, as measured by the solvatochromic technique, is suggested as a measure of the hydration power of water in the phases of aqueous polymer systems. Partitioning of a series of sulphonephthalein dyes in aqueous dextran-poly(ethylene glycol) and dextran-Ficoll two-phase systems of fixed polymer composition containing 0.01 mol/L universal buffer, pH 7.15, was studied. The results obtained are discussed together with those reported earlier on the physico-chemical features of aqueous media in the coexisting phases of the systems. It is suggested that the two phases of aqueous polymer systems should be viewed as two immiscible water-like solvents. The implications of the suggestion for the theoretical treatment of aqueous polymer two-phase systems are discussed.     

Technological aspects of extractive fermentation using aqueous two-phase systems

World Journal of Microbiology and Biotechnology -     

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.     

Partition of rat erythrocytes in aqueous polymer twophase systems

The partition of rat erythrocytes between the top phase and interface of aqueous poly(ethylene glycol)-dextran two-phase systems containing 0.15 M NaCl and 0.01 M sodium phosphate depends on the association of the cells with microscopic globules of dextran that persist in the poly(ethylene glycol)-rich top phase after the horizontal interface between the two phases has formed.     

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.     

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.