Enzymatic hydrolysis of soluble starch in a polyethylene glycol-dextran aqueous two-phase system

Hydrolysis of soluble starch by glucoamylase and β-amylase was investigated as a model reaction in an aqueous two-phase system consisting of polyethylene glycol (PEG) and dextran (DEX). Changes in glucose concentration observed in the batch reaction experiments with glucoamylase were almost identical for the aqueous two-phase and pure water systems, showing that the enzymic reactions investigated were not influenced by the presence of PEG and DEX. The partition of β-amylase into the DEX phase was insufficient compared to that of glucoamylase. Hence, the former enzyme was crosslinked with glutaraldehyde to increase its apparent molecular weight and, as a consequence, the partition coefficient, defined as the concentration ratio of the component partitioned into the PEG phase to that into the DEX phase, was decreased to 17% of that of the original enzyme. In the operation in which the enzyme and substrate are partitioned selectively into the DEX phase and allowed to react there while the product, thus transferring to the PEG phase, is recovered, the aqueous two-phase system with a smaller partition coefficient provided longer operational stability.     

Bioconversion with whole cell penicillin acylase in aqueous two-phase systems

The deacylation of Pen G was carried out by using recombinant E. coli in an aqueous two-phase system consisting of polyethylene glycol and potassium phosphate solution, which partitions the cells to the bottom phase and the products to the top phase. Bioconversion and product separation were carried out in the same reactor. Repeated batch conversion was employed ten times and enzymic activity showed only a slight decline. When pure enzyme was used for bioconversion in an aqueous two-phase system, the decline was fast and bioconversion using whole cell penicillin acylase was better than that obtained using the pure acylase.     

Affinity-specific protein separations using ligand-coupled particles in aqueous two-phase systems: II. Recovery and purification of pyruvate kinase and alcohol dehydrogenase from Saccharomyces cerevisiae

The novel approach of using aqueous two-phase systems for the elution of protein from ligand-coupled particles is investigated using pyruvate kinase and alcohol dehydrogenase from recombinant Saccharomyces cerevisiae and Cibacron blue F3G-A-coupled Sepharose CL6B (Blue-Sepharose) particles as a model system. The ligand-coupled particles distribute quantitatively to the polyethylene glycol-(PEG-) rich top phase and the recovered enzymes partition selectively to the dextran-(DEX-) rich bottom phase. An effective recovery and partial purification of pyruvate kinase and alcohol dehydrogenase from Blue-Sepharose particles using PEG8000-DEXT500 aqueous two-phase systems are demonstrated through a modest increase of salt concentration. The bioselective eluting agent, MgADP, which is useful in chromatographic operations, is not required for the process using aqueous two-phase systems. Recovery of pyruvate kinase, which is bound to ligand-coupled particles, in the DEX-rich bottom phase of aqueous two-phase systems can be up to 95% in one-step operations. The mixing time of ligand-coupled particles with aqueous two-phase systems is a major controlling variable. The salt concentration, the molecular weight of polymer, and the total volume of aqueous two-phase systems also influence the recovery of pyruvate kinase from ligand-coupled particles. The recovered enzymes in the DEX-rich bottom phase remain biologically stable over a long period of storage time. The concentration of product protein in a reduced volume and the easy separation from ligand-coupled particles are added advantages of the process using aqueous two-phase systems. Preliminary studies with goat polyclonal anti-pyruvate kinase-coupled Sepharose particles indicate that the process also may be applicable when a high-affinity ligand such as antibody is used. The experimental results and a theoretical derivation based on equilibrium models for binding/dissociation of ligands and proteins show that the process results in better recovery as compared to that of conventional bulk elution techniques.     

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.     

Synthesis of alkyl glycosides, catalyzed by beta-glycosidases in a reversed micelle system]

A basic possibility of enzymic synthesis of alkyl glycosides in a system of the Aerosol-OT (AOT) reverse micelles was studied. Octyl beta-D-galactopyranoside and octyl beta-D-glucopyranoside were synthesized from the corresponding sugars (lactose or glucose) and octyl alcohol under catalysis with glycolytic enzymes, beta-galactosidase and beta-glucosidase, respectively. The transglycosylation/hydrolysis ratio was shifted toward transglycosylation by using octyl alcohol, one of the substrates, as an organic solvent. The alkyl glycosides were thus obtained in one step from a hydrophilic mono- or disaccharide and a hydrophobic aliphatic alcohol. The direction of the reaction was shown to depend on the pH of aqueous solution immobilized in nerves micelles. The maximum yields were 45% and 40% for octyl galactoside and octyl glucoside, respectively; they markedly exceeded the yields of enzymic syntheses in a two-phase system reported previously.     

Applications of pullulan in aqueous two-phase systems for enzyme production,purification and utilization

Summary Pullulan, a microbial polysaccharide, was employed with polyethylene glycol (PEG) to form an aqueous two-phase system. The phase diagram of the PEG-Pullulan systems as well as the partition of enzymes depended strongly on the molecular weight of PEG. This behavior provided a basis for the separation of cellulase from -galactosidase. The extractive hydrolysis of lactose, using a commercial preparation of -galactosidase, could also be performed in a PEG-Pullulan system (16% PEG 1400, 14% Pullulan). The enzyme was effectively contained in the bottom phase while a high percentage of the glucose produced could be removed in the top phase. The enzyme activity was preserved very well after several repeated hydrolyses.Furthermore, it was demonstrated that the PEG-Pullulan system was capable of retaining Trichoderma reesei in the bottom phase, allowing the production of cellulase which could be intermittently removed in the top phase. Such a system permitted a semicontinuous production scheme although the enzyme production was observed to decrease after five cycles.In view of the low cost and low viscosity of pullulan, this polysaccharide could be considered a suitable replacement for dextran, a component widely used in aqueous two-phase formulation.     

Extraction of proteins from material rich in anionic mucilages: partition and fractionation of vanadate-dependent bromoperoxidases from the brown algae Laminaria digitata and L. saccharina in aqueous polymer two-phase systems

For various reasons extraction of proteins from plant material is difficult. In particular phenolic compounds and polyanionic cell-wall mucilages render conventional procedures of extraction and purification much more difficult. In this respect, aqueous polymer two-phase systems are presented as a powerful technique in extraction of vanadate-dependent bromoperoxidases from the brown macroalga Laminaria digitata, a seaweed extremely rich in mucilages. Little bromoperoxidase activity was obtained when fresh thallus material was extracted in Tris buffer. Extraction from freeze-dried and powdered material was more efficient but only satisfactory when partitioning in an aqueous polymer two-phase system was employed. Among several two-phase systems tested, one composed of poly(ethylene glycol) (PEG 1550) and potassium carbonate proved most successful (phase system-1). A rapid and efficient extraction procedure was developed with special regard for suitability in large scale processes. Staining for catalytic activity after PAGE revealed a pattern of several bromoperoxidase isoforms. Bromoperoxidases extracted in phase system-1 were fractionated into two groups of isoforms by partitioning in a second system (phase system-2) indicating that isoforms from both groups differ significantly in surface properties. Subsequently, one purification step by hydrophobic interaction chromatography was sufficient to remove residual non-peroxidase proteins as well as remaining polysaccharides from bromoperoxidases of both groups. Thus, consideration of aqueous two-phase systems as a technique for extraction and purification of plant proteins can be recommended, whenever inconveniant amounts of phenolic compounds, mucilages or pigments are present.     

Synthesis of Alkyl Glycosides Catalyzed by β-Glycosidases in a System of Reverse Micelles

A basic possibility of enzymic synthesis of alkyl glycosides in a system of the Aerosol-OT (AOT) reverse micelles was studied. Octyl -D-galactopyranoside and octyl -D-glucopyranoside were synthesized from the corresponding sugars (lactose or glucose) and octyl alcohol under catalysis with glycolytic enzymes, -galactosidase and -glucosidase, respectively. The transglycosylation/hydrolysis ratio was shifted toward transglycosylation by using octyl alcohol, one of the substrates, as an organic solvent. The alkyl glycosides were thus obtained in one step from a hydrophilic mono- or disaccharide and a hydrophobic aliphatic alcohol. The direction of the reaction was shown to depend on the pH of aqueous solution solubilized in reverse micelles. The maximum yields were 45% and 40% for octyl galactoside and octyl glucoside, respectively; they markedly exceeded the yields of enzymic syntheses in a two-phase system reported previously.     

Development of a novel bioreactor system for treatment of gaseous benzene

A novel, continuous bioreactor system combining a bubble column (absorption section) and a two-phase bioreactor (degradation section) has been designed to treat a gas stream containing benzene. The bubble column contained hexadecane as an absorbent for benzene, and was systemically chosen considering physical, biological, environmental, operational, and economic factors. This solvent has infinite solubility for benzene and very low volatility. After absorbing benzene in the bubble column, the hexadecane served as the organic phase of the two-phase partitioning bioreactor, transferring benzene into the aqueous phase where it was degraded by Alcaligenes xylosoxidans Y234. The hexadecane was then continuously recirculated back to the absorber section for the removal of additional benzene. All mass transfer and biodegradation characteristics in this system were investigated prior to operation of the integrated unit, and these included: the mass transfer rate of benzene in the absorption column; the mass transfer rate of benzene from the organic phase into the aqueous phase in the two-phase bioreactor; the stripping rate of benzene out of the two-phase bioreactor, etc. All of these parameters were incorporated into model equations, which were used to investigate the effects of operating conditions on the performance of the system. Finally, two experiments were conducted to show the feasibility of this system. Based on an aqueous bioreactor volume of 1 L, when the inlet gas flow and gaseous benzene concentration were 120 L/h and 4.2 mg/L, respectively, the benzene removal efficiency was 75% at steady state. This process is believed to be very practical for the treatment of high concentrations of gaseous pollutants, and represents an alternative to the use of biofilters.     

Characterization of aqueous two-phase systems based on polydisperse phase forming polymers: Enzymatic hydrolysis of starch in a PEG-starch aqueous two-phase system

A new method for determination of the binodial of an aqueous two-phase system, using spectrophotometric measurements of the turbidity, is described in this article. The method is especially designed to characterize phase systems composed of polydisperse phase components. It gives information about the area representing the transition from homogeneous solution to a two-phase system. The two-phase systems studied were first a conventional Dextran T40-polyethylene glycol 20M (PEG 20M) system, then a less-well-defined phase system based on PEG 20M and partially hydrolyzed starch. The PEG 20M-starch system could be changed with respect to the volume ratio between the phases with time using hydrolytic enzymes, and the possibility of using the glucose released from the starch polymer is pointed out. Then the system is transformed to an extractive biconversion where the bottom phase polymer also served as the substrate.     

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.     

Control of autolysis of Bacillus subtilis for selective production of the intracellular enzyme glucose-6-phosphate dehydrogenase in aqueous two-phase systems

A method for the release of intracellular enzyme by autolysis of Bacillus subtilis cells is presented. Both the growth and lysis processes were further applied to aqueous two-phase systems (ATPS). Lysis induced by the addition of Triton X-100 and by low-temperature treatment facilitated the release of cytoplasmic enzyme glucose-6-phosphate dehydrogenase (G6PDH) in ATPS. The release selectivity increased when lysis was regulated by the addition of 50 μM or 100 μM Triton X-100. Cardiolipin efficiently inhibited the autolytic process. Control of the autolytic system promoted the selective release of G6PDH. B. subtilis cells could be grown and lysed in aqueous two-phase systems in a similar fashion to the conventional single-phase medium solutions. The released enzymes were partitioned according to their surface properties. G6PDH were extracted to the top phase in a PEG1540/Dex100K-200K sytem. Cells were partitioned to the bottom phase or the interface, and could be recycled into the fermentor. The selectivity of enzyme production was also increased in two-phase systems by the addition of cardiolipin.     

Bioconversions in an aqueous two-phase system using enzymes immobilized on ultrafine silica particles

Bioconversions of corn starch and bovine hemoglobin in an aqueous two-phase system using α-amylase and papain immobilized on ultrafine silica particles (average diameter 15 nm) were studied. Both α-amylase and papain were immobilized onto the ultrafine silica particles with high efficiency by covalent cross-linking with glutaraldehyde, and both enzymes showed high activities. Since these immobilized enzymes were totally partitioned to the polyethylene glycol (PEG)-rich top phase in PEG/dextran aqueous two phase systems, the products were recovered from the bottom phase. These reaction systems were found to be effective for extractive bioconversions.     

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.     

Growth and Secondary Metabolite Production by Hairy Roots of Tagetes Patula in Aqueous Two-Phase Systems

Hairy roots of Tagetes patula have been grown in aqueous two-phase systems. After selecting suitable polymers from single-phase experiments (in which salt phases were unable to support growth in the desired concentrations) several two-phase systems were tested for their influence on cell growth and thiophene production. Cell growth occurred in all aqueous two-phase systems, but the highest growth rate was achieved in normal medium. There was no difference in thiophene production between medium and aqueous two-phase systems. The partition of thiophenes favoured slightly the more hydrophobic top phase in most cases, while the cells were confined to the bottom phase. One aqueous two-phase system (15% polyethyleneglycol 10,000 and 15% Reppal PES 200) was tested in a stirred tank reactor with normal medium as a control. The growth rate in medium was higher than in the aqueous two-phase system, while the thiophene production per unit cell weight was in the same range for both systems. The excretion of thiophenes in the reactor with the aqueous two-phase system was about ten times as high as in the control reactor. The amount excreted was however still not more than 3% of the total production.     

Aqueous two-phase: the system of choice for extractive fermentation

Extractive fermentation in aqueous two-phase systems is a meaningful approach to overcome low product yield in a conventional fermentation process, and by proper design of the two-phase system it is possible to obtain the product in a cell-free stream. The characteristics of an aqueous two-phase system, various polymers used for forming an aqueous two-phase system, the physicochemical parameters of the aqueous two-phase system, partitioning of biomolecules and cell mass and the effect of individual phase forming polymers on cell growth and product formation are reviewed in this article. The various extractive fermentation processes are also summarised here. At the end, the economic viability and scope of aqueous two-phase fermentation are briefly discussed in relation to the wider application of this topic. Received: 16 June 1999 / Received revision: 29 December 1999 / Accepted: 4 January 2000     

Growth and Secondary Metabolite Production by Hairy Roots of Tagetes Patula in Aqueous Two-Phase Systems

Hairy roots of Tagetes patula have been grown in aqueous two-phase systems. After selecting suitable polymers from single-phase experiments (in which salt phases were unable to support growth in the desired concentrations) several two-phase systems were tested for their influence on cell growth and thiophene production. Cell growth occurred in all aqueous two-phase systems, but the highest growth rate was achieved in normal medium. There was no difference in thiophene production between medium and aqueous two-phase systems. The partition of thiophenes favoured slightly the more hydrophobic top phase in most cases, while the cells were confined to the bottom phase. One aqueous two-phase system (15% polyethyleneglycol 10,000 and 15% Reppal PES 200) was tested in a stirred tank reactor with normal medium as a control. The growth rate in medium was higher than in the aqueous two-phase system, while the thiophene production per unit cell weight was in the same range for both systems. The excretion of thiophenes in the reactor with the aqueous two-phase system was about ten times as high as in the control reactor. The amount excreted was however still not more than 3% of the total production.     

Casein hydrolysis in PEG-salt two phase system by Eudragit-chymotrypsin bioconjugate

A bioconjugate of -chymotrypsin and Eudragit S-100 was used in an aqueous two-phase system (polyethylene glycol/phosphate) for casein hydrolysis. More product was obtained by replacing the lower salt phase with a fresh one during the reaction. The bioconjugate could be reused six times for casein hydrolysis.     

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.     

Bioconversions in aqueous two-phase systems.

Bioconversions involving enzymes and/or microbial cells in aqueous two-phase systems are reviewed. The partitioning of biocatalysts, substrates, and products is discussed in relation to their size. The efficiency of retaining biocatalysts in aqueous two-phase systems is summarized in relation to other methods of recirculating. The influence of phase components on the activity and the stability of enzymatic biocatalysts is exemplified with penicillin acylase and the cellulolytic enzyme system, and the effect of phase components on biocatalytic living cells is exemplified with the production of alpha-amylase with Bacillus sp. Process design costs in bioconversions in aqueous two-phase systems are briefly summarized.