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.     

Optimization of bovine serum albumin partition coefficient in aqueous two-phase systems

Partitioning of proteins in aqueous two-phase systems has been shown to provide a powerful method for separating and purifying mixtures of biomolecules by extraction. These 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. There are many factors which influence the partition coefficient K, the ratio of biomolecule concentration in the top phase to that in the bottom phase, in aqueous two-phase systems. The value of the partition coefficient relies on the physico-chemical properties of the target biomolecule and other molecules and their interactions with those of the chosen system. In this work, the partition behavior of pure bovine serum albumin in aqueous two-phase systems was investigated in order to see the effects of changes in phase properties on the partition coefficient K. The concentration of NaCl and pH were considered to be the factors having influence on K. Optimal conditions of these factors were obtained using the Box-Wilson experimental design. The optimum value of K was found as 0.0126 when NaCl concentration and pH were 0.14 M and 9.8, respectively, for a phase system composed of 8% (w/w) polyethylene glycol 3,350 - 9 (% w/w) dextran 37,500 - 0.05 M phosphate at 20 °C.     

Production of pectinases by Polyporus squamosus in aqueous two-phase system

The ability of Polyporus squamosus to grow and produce pectinases in an aqueous two-phase medium composed of polyethylene glycol and crude dextran is reported. Fungal growth was restricted to the bottom phase leaving the top phase cell free. Amounts of produced biomass and endo and exo-pectinase activities were superior or equal to those obtained in homogeneous medium. The partition coefficient for the endo-pectinase was 1.52 followed by a top phase yield of 70.86%. Although the phase system composition favours partition of a greater part of exo-pectinase activity to the bottom phase (K(exo) was 0.6 and yield in top phase 48.56%) the partitioned activity in the top phase was equal to that produced in homogeneous cultivation.     

Release of rosmarinic acid by Lavandula vera MM cell suspension in two-phase culture systems

Studies were conducted on the cultivation of Lavandula vera MM cell suspensions in different culture systems for the release of extracellular rosmarinic acid (RA). It was established that during cultivation with Amberlite XAD-4 as a second phase, 6.4% of the total content of RA was adsorbed. When L. vera MM cell suspension was cultivated in an aqueous two-phase system formed by adding 4% polyethylene glycol (MW 20,000) and 7.5% dextran (MW 70,000), 11.8% of the total RA content was released into the top polyethylene glycol phase.     

Characteristics of an aqueous two-phase system for α-amylase production

The characteristics of an aqueous two-phase system for the overproduction of extracellular enzyme through α-amylase fermentation by Bacillus amyloliquefaciens were investigated. With higher molecular weight of polyethylene glycol (PEG) or lower molecular weight of dextran, the partition coefficient of α-amylase was increased. α-Amylase biosynthesis was increased when PEG 6000 was included in the medium compared to the medium without PEG. Phosphate addition to the PEG-dextran system improved the partition coefficient of α-amylase, but deactivated α-amylase severely. By using sodium sulfate instead of phosphate, α-amylase deactivation was negligible, and high partitioning of the enzyme in the top phase was obtained.     

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.     

Cultivation of Polyporus squamosus for pectinase production in aqueous two-phase system containing sugar beet extraction waste

Cultivation of the fungus Polyporus squamosus for pectinase production was studied in a polyethylene glycol/crude dextran aqueous two-phase system, with sugar beet extraction waste as pectin source. Fungal growth was restricted to the bottom phase and the amounts of biomass and exo-pectinase activity produced were superior to in homogeneous cultivation. The partition coefficients of endo-pectinase and exo-pectinase were 4.26 and 2.78, respectively. The top phase yields in the single extraction step were about 90% for both pectinases.     

Extractive cultivation of xylanase by Penicillium janthinellum in a poly(ethylene glycol)/cashew-nut tree gum aqueous two-phase system

Cultivation of the fungus Penicillium janthinellum for xylanase production was studied in a poly(ethylene glycol)/cashew-nut tree gum aqueous two-phase system, using a two-level fractional factorial design. The parameters studied were initial pH, cultivation time, type of agro-industrial residue (oat husk or corn cob), agitation, temperature, and phase-forming polymers. The xylanase produced during fermentation partitioned into the top phase. The agitation and temperature (negative), cultivation time and initial pH (positive) effects proved statistically significant for xylanase production. The highest percentage yield of the xylanase in the top and its production in the top phase, about 97% and 160.7 U/mL, were obtained in cultures of 120 h, 40 rpm, 25 degrees C, and pH 5.0.     

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.     

Purification of recombinant cutinase by extraction in an aqueous two-phase system facilitated by a fatty acid substrate

Purification of recombinant wild-type cutinase from the culture supernatant of Saccharomyces cerevisiae by extraction in aqueous two-phase system was investigated. The partition of the enzyme in a polyethylene glycol (PEG)-potassium phosphate system to the top phase was increased with lower molecular weight PEG. Enzyme partition in a 20% PEG/15% phosphate two-phase system was studied in the presence of detergents, fatty acids, and alcohols, respectively. Addition of 0.5% (w/w) butyrate increased the partition coefficient from 17 to 135 and the purification factor from 10 to 23. The effect of butyrate was also confirmed by using the countercurrent mode of extraction. Recovery of cutinase from the top phase was achieved by a secondary extraction into a new salt phase at a lower pH or a lower temperature. A specific interaction of butyrate to the active site of the enzyme was demonstrated by fluorescence spectroscopy. Size exclusion chromatography showed the cutinase-butyrate complex to be over two times the size of the free enzyme.     

Analysis of phase composition in aqueous two-phase systems using a two-column chromatographic method: Application to lactic acid production by extractive fermentation

A new chromatographic system for the simultaneous analysis of polyethylene glycol, dextran, sugars, and low-molecular-weight fatty acids was developed. The system is based on a gel exclusion column which allows a first separation between high- and low-molecular-weight compounds, and a cationic exchange column used to further separate the low-molecular-weight compounds. Two applications of the system were demonstrated: (i) after optimizing eluent conditions the gel exclusion column was used to determine the influence of lactic acid, phosphate buffer, and lactic acid bacteria on the ethylene oxide propylene oxide-dextran T40 phase diagram by HPLC; (ii) the ion exchange column was coupled in series with the gel exclusion column and the concentration of polyethylene glycol, dextran, glucose, lactate, acetate, and formate was determined in samples from the fermentative production of lactic acid in a polyethylene glycol 8000-dextran T40 aqueous two-phase system. The fermentation was operated without pH control in a repeated extractive batch mode, where the cell-free top phase was replaced four times, whereas the cell-containing bottom phase was reused repeatedly. The yield was 1.1 mol of lactic acid formed per mole of glucose added and the productivity was 4.7 mM.h(-1). The polymeric composition of the fermentation system was monitored during the five repeated extractive batches, and it showed a progressive depletion in polyethylene glycol and a progressive enrichment in dextran. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 303-311, 1997.     

The Aqueous Two-Phase System Polyethylene Glycol/Dextran as a Reaction Medium for the Microsomal Monooxygenase System

An aqueous two-phase system of dextran and polyethylene glycol was investigated as a reaction medium for pig liver microsomes in order to find out if the partition of the microsomes, of the substrate 7-ethoxycoumarin and of the product 7-hydroxycoumarin favoured any biotechnological perspectives. Cytochrome-P-450 and NADPH-cytochrome P-450 reductase concentrations and the monooxygenase 7-ethoxycoumarin deethylation activity were measured under a variety of the system parameters. Microsomes totally partition into the bottom phase whereas the concentration ratio of substrate to product is higher in the microsome free top phase. An unfavourable effect is the specific partial deactivation of the cytochrome P-450 by polyethylene glycol.     

Biosurfactants and aqueous two-phase fermentation

The partition of surfactants and a biosurfactant-producing microorganism was studied in polyethylene glycol and dextran aqueous two-phase systems. In the presence of sodium phosphate, surfactants distributed themselves according to charge. Cationic surfactants preferred the bottom phase, while anionic surfactants were attracted to the top phase. Incresing the phosphate molarity or the pH resulted in a more 1-sided surfactant partitioning. Biosurfactant partitioning was weaker than synthetic surfactant partitioning due to the weaker effective charge and lack to strong specific affinity for any of the phase-forming polymers. Bacillus Subtilis cells partitioned very storngly to the bottom phase. The bioscurfactant, surfactin, produced by this microorganism partitioned to the top phase. Batch fermentations were carried out in an aqueous 2-phase system. Surfactin was produced in larger quanities in the 2-phase fermentation than in the regular mineral salts medium.     

Extractive fermentation for improved production of endoglucanase by an intergeneric fusant of Trichoderma reesei/Saccharomyces cerevisiae using aqueous two-phase system

Extractive aqueous two-phase fermentation of endoglucanase, a key enzyme for the conversion of cellulosic substances to fermentable sugars, from an intergeneric fusant of Trichoderma reesei/Saccharomyces cerevisiae is a meaningful approach for better production and simple recovery of this enzyme. A phase composition of 6.5% (w/w) dextran and 7.5% (w/w) polyethylene glycol 6000, having a partition coefficient of 2.89 and 1.31 for endoglucanase from an intergeneric fusant of T. reesei/S. cerevisiae and T. reesei (WT) (being a control in this study), respectively, was chosen for extractive fermentation of the enzyme. Endoglucanase production is higher in medium containing polyethylene glycol (PEG) 6000 than in medium without PEG 6000. Comparative analysis of endoglucanase fermentation by fusant and T. reesei was carried out in shake culture and environment-controlled bioreactor conditions. The fusant produced 0.43U of endoglucanase (overall production: 0.34U) in the top phase of an aqueous two-phase system (ATPS), compared to 0.3U in medium without the phase system in shake culture. In a batch reactor, the endoglucanase level for the fusant in the top phase of ATPS was 0.49U (overall production: 0.40U), compared to 0.38U produced in medium without aqueous two-phase components. To corroborate this study, T. reesei produced 8.41U of endoglucanase (overall production: 5.96U) in the top phase of ATPS, compared to 7.18U in the medium without the phase system in shake culture. On the other hand, in a batch bioreactor, T. reesei produced 10.13U of endoglucanase (overall production: 6.90U) in the top phase of ATPS, compared to 8.56U of the enzyme in medium without aqueous two-phase components. The lower overall enzyme production by T. reesei in the two-phase system might be due to limitation in oxygen transfer to the dispersed phase where the enzyme is produced. A higher cell concentration and a reduced lag phase was obtained in ATPS, compared to a similar medium without phase forming polymers for both the intergeneric fusant of T. reesei/S. cerevisiae and T. reesei.     

Vancomycin partitioning in aqueous two-phase systems: effects of pH, salts, and an affinity ligand

The partitioning of vancomycin in polyethylene glycol (PEG)-dextran and PEG-phosphate aqueous two-phase systems was studied at different pHs, at varying concentrations of neutral salts, and with an affinity ligand attached to methoxy polyethylene glycol (MPEG). Vancomycin is found to partition preferentially into the PEG-rich top phase, and its partition coefficient increases nearly exponentially with the addition of water structure-making salts, such as sodium sulfate and sodium chloride, but is independent of sodium phosphate concentration. In the PEG-dextran system the vancomycin partition coefficient increases 3-fold in acidic and neutral solutions, while in the PEG-phosphate system it increases about 30-fold on the addition of the same amount of sodium chloride (1. 5 mol/kg). In basic solution, above its isoelectric point, the vancomycin partition coefficient increases slightly with NaCI concentration in the PEG-dextran system. We also examined the use of the dipeptide D-ala-D-ala as an affinity ligand on MPEG to extract vancomycin into the PEG-rich phase. The vancomycin partition coefficient increased almost 7-fold upon adding the MPEG-ligand in an amount equal to approximately 3% of the total PEG in the system. Finally, fractionation of the polydisperse phase-forming polymers in the two-phase PEG-dextran system was observed. The effect of this polymer fractionation on the partition coefficient of vancomycin is discussed.     

Recovery of extracellular human insulin-like growth factor-I and II as a fusion protein from Escherichia coli culture broth by aqueous two-phase extraction.

The primary purification of human insulin-like growth factor-I (IGF-I) and IGF-II, produced extracellularly in Escherichia coli as a fusion to two domains (ZZ) derived from staphylococcal protein A, has been studied. First, the partitioning of IgG-affinity purified ZZ-IGF-I and ZZ-IGF-II, respectively, to the top phase in poly(ethylene glycol)/potassium phosphate aqueous two-phase systems were investigated. Thereafter, the extraction of ZZ-IGF-I with a poly(ethylene glycol) 1500/potassium phosphate system was performed directly in the bioreactor after the cultivation. This resulted in a reduction of the cultivation volume more than 3-fold with a recovery of about 90% of target protein in a poly(ethylene glycol)-rich phase. The majority of the cells partitioned to the potassium phosphate-rich bottom phase, while a smaller fraction was collected at the interface, and/or as a densely packed cake on top of the interface. Contaminating proteins were also eliminated to some extent, which resulted in an almost 2-fold protein purification. Some obvious benefits offered by the aqueous two-phase system in the primary purification have been demonstrated: Firstly, the possibility to an early process volume reduction and thereby a concentration of the target protein. Secondly, a simultaneous protein purification was achieved. From this work it can be concluded that aqueous two-phase extraction should be considered as an attractive candidate for the primary steps during the design of new purification processes for extracellular proteins.     

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.     

Biosynthesis of acrylamide from acrylonitrile in aqueous two phase system

Summary Acrylamide was produced from acrylonitrile usingBrevibacterium sp in aqueous two-phase systems composed of polyethylene glycol and potassium phosphate. The biocatalysts were almost completely partitioned in the potassium phosphate rich bottom phase. The inhibition of the active enzyme by both substrate and product could be reduced by favorable partition properties. Repeated conversions over five runs were accomplished without a significant loss of enzyme activity. The yields of acrylamide obtained from the top phase were 0.736, 0.834, 0.865, 0.848 and 0.917 mol acrylamide/mol acrylonitrile, respectively.     

Liquid–liquid extraction of an extracellular alkaline protease from fermentation broth using aqueous two-phase and reversed micelles systems

Summary The study of recovery of an extracellular alkaline protease from fermentation broth produced by Norcadiopsis sp, was carried out with liquid–liquid extraction through sodium di-(2-ethylhexyl) sulphosuccinate/isooctane reversed micelles systems and aqueous two-phase systems (polyethylene glycol/potassium phosphate). The best conditions for extraction and back-extraction with the reversed micelles system was obtained at pH 9.0 and pH 5.0, respectively, showing a yield of protein of 6.16%, a specific activity of 4.10 U/ml and a purification factor of 1.80. The studies using aqueous two-phase systems of polyethylene glycol/potassium phosphate at pH 10.0 showed purification factors of 2 and 5, and protein yield of 11 and 4%, respectively, for polyethylene glycol 550/potassium phosphate and polyethylene glycol 8000/potassium phosphate. The results indicate that the aqueous two-phase systems are more attractive as a first step in the isolation and purification processes.     

New Aqueous Two Phase System Comprising Polyethylene Glycol and Xanthan

A new aqueous two phase system comprising polyethylene glycol and xanthan is reported together with its phase diagram. The phase composition of the bottom phase did not vary (PEG 1.6–1.8% w/w; xanthan 0.24–0.28% w/w) while that of the top phase varied significantly (PEG 4–5% w/w, xanthan 0.05–1.37% w/w). Unlike conventional aqueous two phase systems, the viscosity of the top phase is also high and values are comparable to that of the bottom phase. When BSA was used as a model protein, it partitioned entirely into the bottom phase.