Extractive bioconversion in aqueous two-phase systems

Summary The transformation of hydrocortisone to prednisolone was studied in aqueous two-phase systems, as a model for the extractive bioconversion of fine chemicals. The bacterium, Arthrobacter simplex, was able to grow in the two-phase system and the cells could be revitalized after a period of use. Use of aqueous two-phase systems made it possible to operate the reaction at higher substrate concentrations than in pure buffer solution. An adsorptive method to remove the product from the top phase was tested and shown to be both efficient and compatible with the overall process. In order to reduce the costs of operation in aqueous two-phase systems, a cheaper starch-based polymer, Reppal-PES, was successfully used as a substitute for dextran.Dedicated to Professor Dr. Georg Manecke on the occasion of his 70th birthday     

Purification of recombinant protein A by aqueous two-phase extraction integrated with affinity precipitation

Aqueous two-phase extraction incorporated affinity precipitation was examined as a technique for protein purification. An enteric coating polymer, Eudragit S100, was employed as a ligand carrier. Eudragit was specifically partitioned to the top phase in the aqueous two-phase systems. For application of this method to purification of recombinant protein A using human IgG coupled to Eudragit in an aqueous two-phase system, 80% of protein A added was recovered with 81% purity. The purity was enhanced 26-fold by thid method. The IgG-Eudragit could be used repeatedly for the purification process. This seperation method should be applicable to industrial-scale purification as a new purification procedure combining the advantages and compensating for the disadvantages of the aqueous two-phase method and affinity precipitation method. (c) 1992 John Wiley & Sons, Inc.     

An aqueous hydroxypropylstarch-poly(ethylene glycol) two-phase system for extraction of alpha-lactalbumin and beta-lactoglobulin from bovine whey.

The partitioning of alpha-lactalbumin and beta-lactoglobulin from bovine whey has been studied in an aqueous poly(ethylene glycol) (PEG)-hydroxypropylstarch two-phase system. The influence of several parameters including concentrations of polymers, sodium phosphate buffer, KSCN, and of PEG palmitate, with and without the presence of Ca2+, on the partitioning of the proteins has been investigated. The separation of the two proteins was demonstrated by counter-current distribution. A purification procedure for both proteins has been developed by using PEG-hydroxypropylstarch two-phase system. This system is compared with the more costly standard system based on PEG and dextran. The possible use of the aqueous two-phase systems for batch extraction for large scale purification of these whey proteins is discussed.     

Changes in plasma membrane and microfilaments accompanying morphologic differentiation in Chinese hamster ovary (CHO) cells.

Studies on the application of the techniques of counter-current distribution (CCD) in aqueous two-phase systems and multiple sedimentation for the fractionation of metaphase chromosomes are presented. The two-phase systems were composed of aqueous solutions of Dextran 500 and poly(ethylene)glycol 6000 (PEG). It has been found that different groups of chromosomes differ in their distribution between the two phases and that the introduction of PEG with covalently attached positively or negatively charged groups provides a means of steering the distribution of chromosomes. A rough fractionation of chromosomes on the basis of size is possible by the technique of multiple sedimentation and this, in combination with CCD, yields 10 fractions of chromosomes. Partition and CCD in aqueous two-phase system separate chromosomes according to their surface properties and may prove useful for isolation of individual chromosomes in bulk.     

A rapid method for the isolation of L-cell surface membranes using an aqueous two-phase polymer system

Summary A dextran-polythylene glycol aqueous two-phase system has been used to separate cell surface membranes from other cellular organelles. The surface membranes have been identified on the basis of morphology, content of Na⁺, K⁺-ATPase, and presence of surface antigen as detected by a⁵¹Cr release method. Contamination of the surface membrane preparations by smooth endoplasmic reticulum, mitochondria, and nuclei has been found to be minimal. An average of 6.5% of the total protein was found in the membrane fraction. Less than two hours is required to isolate the membrane fraction after preparation of a Dounce homogenate. Fractionation by aqueous two-phase polymer systems appears to be a rapid and effective method for the isolation of surface membranes.     

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.     

Affinity-enhanced protein partitioning in decyl beta-D-glucopyranoside two-phase aqueous micellar systems

Liquid-liquid extraction in two-phase aqueous complex-fluid systems has been proposed as a scalable, versatile, and cost-effective purification method for the downstream processing of biotechnological products. In the case of two-phase aqueous micellar systems, careful choices of the phase-forming surfactants or surfactant mixtures allow these systems to separate biomolecules based on size, hydrophobicity, charge, or specific affinity. In this article, we investigate the affinity-enhanced partitioning of a model affinity-tagged protei--green fluorescent protein fused to a family 9 carbohydrate-binding module (CBM9-GFP)--in a two-phase aqueous micellar system generated from the nonionic surfactant n-decyl beta-D-glucopyranoside (C10G1), which acts simultaneously as the phase-former and the affinity ligand. In this simple system, CBM9-GFP was extracted preferentially into the micelle-rich phase, despite the opposing tendency of the steric, excluded-volume interactions operating between the protein and the micelles. We obtained more than a sixfold increase (from 0.47 to 3.1) in the protein partition coefficient (Kp), as compared to a control case where the affinity interactions were "turned off" by the addition of a competitive inhibitor (glucose). It was demonstrated conclusively that the observed increase in Kp can be attributed to the specific affinity between the CBM9 domain and the affinity surfactant C10G1, suggesting that the method can be generally applied to any CBM9-tagged protein. To rationalize the observed phenomenon of affinity-enhanced partitioning in two-phase aqueous micellar systems, we formulated a theoretical framework to model the protein partition coefficient. The modeling approach accounts for both the excluded-volume interactions and the affinity interactions between the protein and the surfactants, and considers the contributions from the monomeric and the micellar surfactants separately. The model was shown to be consistent with the experimental data, as well as with our current understanding of the CBM9 domain.     

Ethylene oxide and propylene oxide random copolymer/sodium chloride aqueous two-phase systems: wetting and adsorption on dodecyl-agarose and polystyrene

Liquid/liquid partition chromatography is a mild yet powerful separation method for a variety of biological materials. This work demonstrates that it should be feasible to immobilize an ethylene oxide-propylene oxide (EO/PO) random copolymer solution and to use a solution of NaCl equilibrated against the polymer solution as the mobile-phase (poly (EO-PO) [P(EO-PO)] and NaCl form two aqueous phases known as aqueous two-phase systems). Three random copolymers with different molecular weights and EO/PO ratios were used. Dodecyl-agarose and polystyrene were tested as possible supports. The wetting energies of the aqueous two-phase systems on these two kinds of surfaces were calculated as well as contact angles for each phase on the same surfaces. Finally, the thickness of P(EO-PO) adsorption layers on polystyrene lattices were measured by dynamic light scattering. Contact angle measurements indicate that indeed some EO/PO copolymers preferentially wet hydrophobic substrates, forming thin films.     

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.     

Substitutions of surface amino acid residues of cutinase probed by aqueous two-phase partitioning

The surface properties of a protein are often crucial for recognition and interaction with other molecules. Important functional residues can be identified by mutational analysis. There is a need for rapid methods to study protein surfaces and surface changes due to mutations. Partitioning in aqueous two-phase systems has the potential to be used in this respect since protein partitioning depends on the surface properties of the protein. The influence of surface-exposed amino acid residues in protein partitioning has been studied with cutinase variants, which differed in one or several amino acid residues as a result of site-directed mutagenesis. The solvent accessibility of the mutated residues was determined with a computer program, Graphical Representation and Analysis of Surface Properties. The aqueous two-phase system was composed of dextran and a random copolymer of ethylene oxide and propylene oxide. It was shown, for the first time, to what extent surface-exposed amino acid residues influence the partition coefficient in an aqueous two-phase system. The effect on partitioning could be described only taking into account solvent accessibility and type of residue substitution. The results demonstrate that the system can be used to detect conformational changes in mutant proteins since the expected effect on partitioning due to a mutation can be calculated. The aqueous two-phase system used here does indeed provide a rapid and convenient method to study protein surfaces and slight surface changes due to mutations.     

高速逆流色谱技术在生物大分子分离纯化中的应用

高速逆流色谱是一种连续液-液色谱技术,具有无固相载体、样品无需严格预处理等优点。近10年来,在设备结构和溶剂体系等方面进行了大量的研究开发,已推广应用于生物技术、医药、天然产物、环境监测、食品等领域。为适应生物大分子和活性细胞的分离,采用条件温和的双水相体系,研究开发相应的高速逆流色谱设备已成为热点。针对双水相体系的特点,已经开发出了多种具有较高固定相保留率的新型高速逆流色谱设备,通过优化实验条件,成功地进行了多种蛋白质的分离纯化。本对该领域的最新进展进行了综述与评价。     

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     

Analysis of the phase behavior of the aqueous poly(ethylene glycol)-Ficoll system

The PEG-Ficoll polymer phase system is one that has been overlooked in the past for biotechnology applications because of the stability of its emulsions. However, new applications, such as emulsion coating of cells, are appearing that rely on this very property. Ficoll is highly polydisperse and multimodal with three distinct Ficoll peaks in gel permeation chromatography. As a result, the transition between one-phase and two-phase systems is blurred and the binodials obtained through turbidometric titration and tie-line analysis differ significantly. Moreover, since the three Ficoll peaks partition differently, tie-line analysis cannot be described by a simple model of the aqueous two-phase system. A simple modification to the model allowed for excellent fit, and this modification may prove well-suited for the many practical cases where aqueous two-phase systems fail to display parallel tie-lines as implicitly assumed in the simpler model.     

Aqueous micellar two-phase system composed of hyamine-type hydrophobically modified ethylene oxide and application for cytochrome P450 BM-3 separation

The hydrophobically modified ethylene oxide polymer, HM-EO, was modified with an alkyl halide to prepare a hyamine-type HM-EO, named N-Me-HM-EO, which could be used for forming N-Me-HM-EO/buffer aqueous micellar two-phase system. The critical micelle concentration of N-Me-HM-EO solution and the phase diagrams of N-Me-HM-EO/buffer systems were determined. By using this novel aqueous micellar two-phase system, the separation of cytochrome P450 BM-3 from cell extract was explored. The partitioning behavior of P450 BM-3 in N-Me-HM-EO/buffer systems was measured. The influences of some factors such as total proteins concentration, pH, temperature and salt concentration, on the partitioning coefficients of P450 BM-3 were investigated. Since the micellar aggregates in the N-Me-HM-EO enriched phase were positively charged, it was possible to conduct the proteins with different charges to top or bottom phases by adjusting pH and salt concentration in the system. A separation scheme consisting of two consecutive aqueous two-phase extraction steps was proposed: the first extraction with N-Me-HM-EO/buffer system at pH 8.0, and the second extraction in the same system at pH 6.0. The recovery of P450 BM-3 was 73.3% with the purification factor of 2.5. The results indicated that the aqueous micellar two-phase system composed of hyamine modified polysoap has a promising application for selective separation of biomolecules depending on the enhanced electrostatic interactions between micelles and proteins.     

The potential of cloud point system as a novel two-phase partitioning system for biotransformation

Although the extractive biotransformation in two-phase partitioning systems have been studied extensively, such as the water–organic solvent two-phase system, the aqueous two-phase system, the reverse micelle system, and the room temperature ionic liquid, etc., this has not yet resulted in a widespread industrial application. Based on the discussion of the main obstacles, an exploitation of a cloud point system, which has already been applied in a separation field known as a cloud point extraction, as a novel two-phase partitioning system for biotransformation, is reviewed by analysis of some topical examples. At the end of the review, the process control and downstream processing in the application of the novel two-phase partitioning system for biotransformation are also briefly discussed.     

Distribution of free and antibody-bound peptide hormones in two-phase aqueous polymer systems

Peptide hormones labelled with radioactive iodine were partitioned into the aqueous two-phase polymer systems developed by Albertsson (1960) and the conditions required for separation of free from antibody-bound hormone have been worked out. Hormones studied included insulin, growth hormone, parathyroid hormone and [arginine]-vasopressin. Free and antibody-bound hormones show different distribution coefficients in a number of systems tested; two systems, the dextran-polyethylene glycol and dextran sulphate-polyethylene glycol system, give optimum separation. Free hormones distribute readily into the upper phase of these systems, whereas hormone-antibody complexes, as well as uncombined antibody, are found almost completely in the lower phase. Various factors including the polymer concentration, the ionic composition of the system, the nature of the hormone and the nature of added serum protein differentially affect the distribution coefficients for free and antibody-bound hormone. These factors can be adequately controlled so as to improve separation. The two-phase partition method has been successfully applied to measure binding of labelled hormone to antibody under standard radioimmunoassay conditions. It exhibits several advantages over the method of equilibration dialysis and can be applied to the study of non-immunological interactions.     

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.     

Optimization of bovine serum albumin sorption and recovery by hydrogels

Aqueous two-phase 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. Partitioning of proteins in such systems provides a powerful method for separating and purifying mixtures of biomolecules by extraction. If one of the phase forming polymers is a crosslinked gel, then the solution-controlled gel sorption may be considered as a modification of aqueous two-phase extraction. Since PEG/dextran systems are widely used in aqueous two-phase extraction and dextran gels (Sephadex) are common chromatographic media, we choose a PEG/dextran gel system as a model system in this study. The partitioning behavior of pure bovine serum albumin (BSA) in PEG/dextran gel systems is investigated to see the effects of variations in PEG and NaCl concentrations on the partition coefficient K. By making use of the Box-Wilson experimental design, K is shown to be maximized at 9.8 (%, w/w) PEG and 0.2 M NaCl concentrations, respectively, as 182.     

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.     

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.