Magnetic aqueous two-phase separation in preparative applications.

Magnetic aqueous two-phase separation is a new technique to speed up the separation of aqueous two-phase systems (Anal. Biochem. 1987, 167, 331-339). It is based on the addition of magnetically susceptible material (e.g. 1-micron iron oxide particles) which induces rapid phase separation when a mixed system is placed in a magnetic field. The technique has been applied to a number of two-phase systems. The time for phase separation was decreased by a factor of 5-240,000, with the largest improvement for systems containing high concentrations of protein and for systems with viscous or nearly isopycnic phases. An apparatus for preparative multistage extraction with magnetic separation was constructed and tested on glycolytic enzymes present in a yeast extract using a dextran/Cibacron blue-polyethylene glycol system. The presence of iron oxide particles did not adversely affect the extracted enzymes. An electromagnet-based apparatus for continuous phase separation on a larger scale was also designed. A phase system containing crude dextran and unpurified cell homogenate was effectively processed. The apparatus also allowed effective separation when the phase containing iron oxide particles was only a small fraction (4%) of the total phase system.     

Preparation of an organic solvent-tolerant strain from baker's yeast

By using immobilized baker's yeast repeatedly in isooctane with occasional reactivation by cultivation, we succeeded in the preparation of an organic solvent-tolerant strain, named KK21, which could grow in the presence of isooctane. This is the first report on an organic solvent-tolerant strain from baker's yeast. Strain KK21 showed high tolerance to organic solvents and maintained a high and stable activity on continuous reduction of n-butyl 3-oxobutanoate in an isooctane-medium two-phase system. Although the morphology of strain KK21 was the same as that of baker's yeast, the saturated fatty acid occupancy (SFA occupancy), which is defined as the percentage of saturated fatty acids in the total fatty acids of phospholipids, of strain KK21 was significantly higher than that of parental baker's yeast when strain KK21 was grown in the presence of isooctane, suggesting that a decrease in fluidity of the cell membrane might play an important role in the tolerance to organic solvents.     

Synthesis of dye conjugates of ethylene oxide-propylene oxide copolymers and application in temperature-induced phase partitioning.

Synthesis of conjugates of the ethylene oxide/propylene oxide copolymer UCON 50-HB-5100 and the triazine dyes Cibacron Blue F3G-A and Procion Yellow HE-3G is described. The UCON-dye conjugate of Procion Yellow HE-3G is used as a ligand for affinity partitioning of glucose-6-phosphate dehydrogenase from bakers' yeast. The enzyme is first partitioned in a two-phase system composed of UCON, UCON-ligand and dextran, and the two phases isolated in separate containers. A small amount of salt is then added to the upper phase, which contains the UCON-ligand-enzyme complex, and the temperature increased above the cloud point of the UCON polymer to give a new two-phase system. The new two-phase system consists of an upper salt/water phase containing free enzyme and a lower UCON/water phase containing free UCON-ligand. Temperature-induced phase partitioning is thus seen to be of much assistance in dissociating enzyme-ligand complex, recovering enzyme and recycling UCON-ligand.     

Preparation of cibacron blue F3G-A (polyethylene glycol) in large scale for use in affinity partitioning

The reaction parameters for preparation of Cibacron Blue F3G-A polyethylene glycol have been studied, including temperature, concentration of reactants, and addition of neutral salt (Na(2)SO(4)) as well as ethanol. The yield of dypolymer is strongly dependent on temperature and time of reaction. Preparation in large scale has been done under optimal conditions binding more than 30% of the dye to polyethylene glycol in a low-cost procedure. The effectiveness of this dye-polymer for use in liquid-liquid extraction of enzymes is demonstrated by partition of glucose 6-phosphate dehydrogenase and phosphofructokinase when an extract of baker's yeast is included in a dextran-polyethylene glycol-water two-phase system.     

Influence of system and molecular parameters upon fractionation of intracellular proteins from Saccharomyces by aqueous two-phase partition.

The interaction of molecular characteristics of proteins with the physicochemical properties of PEG-phosphate aqueous two-phase systems has been studied. This has involved characterization of protein molecular weight, charge, and hydrophobicity and study of PEG molecular weight and concentration, phosphate concentration, and pH. System characterization has been conducted in the context of limited stage fractionation procedures for protein recovery from baker's yeast. Results are presented which show that the degree of purification achieved is dependent on macromolecular surface properties rather than system operating conditions. A simple conceptual model of partitioning in PEG-phosphate aqueous two-phase systems is presented which is applicable in the rational design of fractionation procedures and serves to limit the amount of empirical experimentation necessary for the establishment of practical operations.     

两相分配法制备南极红酵母质膜

用葡聚糖 T-500(Dextran T-500)和聚乙二醇(PEG-3350)两相体系制备南极红酵母(Rhodotorula sp.)菌株 NJ298 的质膜.首先在 2 mmol/L KCl 浓度下,选用5种不同的聚合物浓度(5.6%、5.8%、6.0%、6.2%、6.4%,W/W),研究了 NJ298 质膜在两相体系中的分配情况,在此基础上进一步研究了 KCl 浓度(2 mmol/L、4 mmol/L、6 mmol/L、8 mmol/L、10 mmol/L)对 NJ298 质膜的纯度及得率的影响.结果表明,选用6.0%聚合物浓度,4 mmol/LKCl 的两相分配体系,分离3次可得到相对纯度在 78.2%的南极红酵母质膜组分,标志酶鉴定及磷钨酸染色电镜检测均表明获得了高纯度密实的正向型的质膜囊泡.这为进一步研究该菌株的南极极端环境适应机制奠定了基础.     

两相分配法制备南极红酵母质膜

用葡聚糖T-500(Dextran T-500)和聚乙二醇(PEG-3350)两相体系制备南极红酵母(Rhodotorula sp.)菌株 NJ298的质膜。首先在2 mmol/L KCl浓度下, 选用5种不同的聚合物浓度(5.6%、5.8%、6.0%、6.2%、6.4 %, W/W), 研究了NJ298质膜在两相体系中的分配情况, 在此基础上进一步研究了KCl浓度(2 mmol/L、4 mmol/L、6 mmol/L、8 mmol/L、10 mmol/L)对NJ298质膜的纯度及得率的影响。结果表明, 选用6.0%聚合物浓度, 4 mmol/L KCl的两相分配体系, 分离3次可得到相对纯度在78.2%的南极红酵母质膜组分, 标志酶鉴定及磷钨酸染色电镜检测均表明获得了高纯度密实的正向型的质膜囊泡。这为进一步研究该菌株的南极极端环境适应机制奠定了基础。     

Identification of yeast strains isolated from a two-phase decanter system olive oil waste and investigation of their ability for its fermentation

A dynamic fed-batch microcosm system is described which permits assessment of the progressive growth of yeasts through olive oil waste. We report on its application to measure the effects of the growth of yeast strains upon the chemical composition of "alpeorujo", the waste of a two-phase decanter system used for the extraction of olive oil. Six phenotypically distinct groups of yeasts were isolated. Three selected isolates were identified as being most closely related to Saccharomyces sp., Candida boidinii and Geotrichum candidum using biochemical tests and partial 18S rDNA gene sequence analysis. This is the first report of yeast growth on "alpeorujo" by the use of a fed-batch microcosm system, resulting in the change of the initial chemical composition of "alpeorujo" and in the decrease of the toxic substances such as phenols.     

Liquid-liquid partitioning of some enzymes, especially phosphofuctokinase, from Saccharomyces cerevisiae at subzero temperature

The effects of low temperature (−18°C) on the stability and partitioning of some glycolytic enzymes within an aqueous two-phase system were studied. The enzymes were phosphofructokinase, glyceraldehyde-3-phosphate dehydrogenase and alcohol dehydrogenase present in a crude extract of bakers' yeast. The partitioning of pure phosphofructokinase, isolated from bakers' yeast, was also examined. The two-phase systems were composed of water, poly(ethylene glycol), dextran, and ethylene glycol and buffer. The influence on the partitioning of the presence of ethylene glycol, phenylmethylsulfonyl fluoride and poly(ethylene glycol)-bound Cibacron Blue F3G-A was investigated at −18, 0 and (in some cases) 20°C. The presence of ethylene glycol, phase polymers and low temperature stabilized all three enzyme activities. Cibacron Blue, an affinity ligand for phosphofructokinase, increased its partitioning into the upper phase with decreasing temperature. Depending on the conditions, various amounts of the enzymes were recovered at the interface, also in systems not containing ethylene glycol. The implications of the observed effects on the use of aqueous two-phase systems for the extraction and fractionation of proteins are discussed.     

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.     

Studies on the extraction of DesPro(2)-Val15-Leu17-aprotinin from the culture broth of a recombinant Saccharomyces cerevisiae.

The application of an aqueous two-phase system is described for the extraction of DesPro(2)-Val15-Leu17-aprotinin from yeast culture supernatant, using native chymotrypsin as affinity ligand. The interaction is driven by hydrophobic forces and leads to the accumulation of the aprotinin-chymotrypsin complex in the salt-rich (bottom) phase of a polyethyleglycol/salt system. The complex may be dissociated at low pH values. The separation of the recombinant aprotinin and the protease required chromatographic processes, which proved difficult to interface with the affinity extraction.     

Biodegradation of xylene and butyl acetate using an aqueous-silicon oil two-phase system

A stable microbial population, consisting of seven bacterial strains and three yeast strains, was selected in batch cultures on a mixture of ortho and meta-xylene and butyl acetate as the sole source of carbon and energy. This population can completely degrade up to 10 g/L of a mixture of these xenobiotics (70% xylene and 30% butyl acetate wt/wt) in a two-phase aqueous-silicone oil system (70%/30% vol/vol) within 96 h, while for the usual one-phase system very low growth degradation rates were observed. Further organic solvents were tested and finally, silicon oil was selected as the best organic phase for such a two-phase system. With periodical pH adjustments to 6.0 in fed-batch mode, the culture showed a global degradation rate of 63 mg L^-1 h^-1.     

Phase diagrams of a CTAB/organic solvent/buffer system applied to extraction of enzymes by reverse micelles

A partial pseudo-ternary phase diagram has been studied for the cethyltrimethylammonium bromide/isooctane:hexanol:butanol/potassium phosphate buffer system, where the two-phase diagram consisting of the reverse micelle phase (L2) in equilibrium with the solvent is indicated. Based on these diagrams two-phase systems of reverse micelles were prepared with different compositions of the compounds and used for extraction and recovery of two enzymes, and the percentage of enzyme recovery yield monitored. The enzymes glucose-6-phosphate dehydrogenase (G6PD) and xylose redutase (XR) obtained from Candida guilliermondii yeast were used in the extraction procedures. The recovery yield data indicate that micelles having different composition give selective extraction of enzymes. The method can thus be used to optimize enzyme extraction processes.     

Partitioning of yeast RNA in aqueous two-phase system

Summary The partition behaviour of RNA extracted from yeast was examined using three types of aqueous two-phase systems: potassium phosphate—polyethyleneglycol (PEG) system, ammonium sulphate—PEG system and dextran sulphate—PEG—NaCl system. The molecular weight of PEG showed rather remarkable effects of RNA partition than did the electrolyte. High molecular weight RNA was concentrated at the interface in these systems. This suggests the possibility of its simple concentration or extraction.     

Extractive bioconversion of 2-phenylethanol from L-phenylalanine by Saccharomyces cerevisiae

The bioconversion of L-phenylalanine (L-Phe) to 2-phenylethanol (PEA) by the yeast Saccharomyces cerevisiae is limited by the toxicity of the product. PEA extraction by a separate organic phase in the fermenter is the ideal in situ product recovery (ISPR) technique to enhance productivity. Oleic acid was chosen as organic phase for two-phase fed-batch cultures, although it interfered to some extent with yeast viability. There was a synergistic inhibitory impact toward S. cerevisiae in the presence of PEA, and therefore a maximal PEA concentration in the aqueous phase of only 2.1 g/L was achieved, compared to 3.8 g/L for a normal fed-batch culture. However, the overall PEA concentration in the fermenter was increased to 12.6 g/L, because the PEA concentration in the oleic phase attained a value of 24 g/L. Thus, an average volumetric PEA production rate of 0.26 g L(-1) h(-1) and a maximal volumetric PEA production rate of 0.47 g L(-1) h(-1) were achieved in the two-phase fed-batch culture. As ethanol inhibition had to be avoided, the production rates were limited by the intrinsic oxidative capacity of S. cerevisiae. In addition, the high viscosity of the two-phase system lowered the k(l)a, and therefore also the productivity. Thus, if a specific ISPR technique is planned, it consequently has to be remembered that the productivity of this bioconversion process is also quickly limited by the k(l)a of the fermenter at high cell densities.     

A study of the fatty acid metabolism of the yeast Pityrosporum ovale

The yeast Pityrosporum ovale, a skin saprophyte, will only grow if fatty acids of chain length greater than C(10) are added to the culture medium. 9-Hydroxypalmitic acid is the major product of metabolism of even-carbon-number fatty acids; 9-hydroxystearic acid is also found. The optimum pH for this conversion is pH4.5. The hydroxy fatty acids produced are found bound in a polar form in the aqueous phase of the culture medium. Growth of the organisms is facilitated by presentation of the substrate as a two-phase liquid system.     

A membrane bioreactor for biotransformations of hydrophobic molecules

The Membrane Bioreactor for Biotransformations (MBB) is based on the aqueous/organic two-phase system, and uses a tubular silicone rubber membrane to separate the two liquid phases. This avoids the key problem associated with direct contact two-phase processes, specifically, product emulsification. The baker's yeast mediated reduction of geraniol to citronellol was used as a model biotransformation to demonstrate MBB operation. Values for the overall mass transfer coefficient were determined for geraniol, (2.0 x 10(-5) ms-1), and for citronellol, (2.1 x 10(-5) ms-1) diffusion across the silicone rubber membrane. Using these values, and the specific activity of the biocatalyst (5 nmols-1g biomass-1), a suitable membrane surface area: biomass ratio was determined as 2.4 x 10(-3) m2g biomass-1. The bioreactor was operated at this surface area: biomass ratio and achieved a product accumulation rate 90-95% that of a conventional direct contact two-phase system. The slight reduction in product accumulation rate was shown not to be due to mass transfer limitations with respect to reactant delivery or product extraction. Copyright 1998 John Wiley & Sons, Inc.     

Aqueous two-phase protein partitioning using textile dyes as affinity ligands.

A simple and inexpensive aqueous two-phase system for the affinity partitioning of proteins is introduced. An aqueous solution consisting of maltodextrin (M100; molecular mass, 1800) and polyvinylpyrrolidone (PVP360; molecular mass, 360,000) formed two phases at 4 degrees C when the concentration of the polymers was 22.5% (w/w) and 4.0% (w/w), respectively. When the amino derivatives of chlorotriazine textile dyes or other azo textile dyes were added to the two-phase system they partitioned asymmetrically, favoring the upper, less dense, PVP360-rich phase. The association of the textile dyes with PVP360 did not prevent them from acting as affinity ligands for proteins. Three of the dyes screened increased the partition coefficient of purified lysozyme nearly 50-fold over a control containing no dye. Parameters such as pH, ionic strength, and dye concentration modulated the affinity-partitioning effect of the system. The partition coefficient of lysozyme in an egg white protein mixture increased severalfold as the total protein content of the system approached 4% (w/w), indicating that protein concentration is also important in determining the partitioning characteristics of this two-phase system. Proteins were efficiently freed of PVP360 and textile dye by recovery in a high-salt solution when another two-phase system was formed upon the addition of a solution of concentrated potassium phosphate to the isolated upper phase of a PVP360/M100/textile dye two-phase system. The affinity-partitioning system presented here allows one to screen large numbers of potentially useful protein ligands to optimize protein separation, followed by direct scaleup to a system size determined by the user.     

IN SITU SEPARATION OF ETHANOL WITH AQUEOUS TWO-PHASE SYSTEM AND ASSESSMENT OF KLa FOR YEAST GROWTH IN BATCH CULTIVATION

In the fermentation process, the separation of product and its purification is the most difficult and exigent task in the ground of biochemical engineering. Another major problem that is encountered in the fermentation is product inhibition, which leads to low conversion and low productivities. Extractive fermentation is a technique that helps in the in situ removal of product and better performance of the fermentation. An aqueous two-phase system was employed for in situ ethanol separation since the technique was biofriendly to the Saccharomyces cerevisiae and the ethanol produced. The two-phase system was obtained with polyethylene glycol 4000 (PEG 4000) and ammonium sulfate in water above critical concentrations, with the desire that the ethanol moves to the top phase while cells rest at the bottom. The overall mass transfer coefficient (K_La) was also estimated for the yeast growth at different rpm. The concentration and yield of ethanol were determined for conventional fermentation to be around 81.3% and for extractive fermentation around 87.5% at the end of the fermentation. Based on observation of both processes, extractive fermentation was found to be the best.