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.     

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.     

Ionic liquids for two-phase systems and their application for purification,extraction and biocatalysis

The development of biotechnological processes using novel two-phase systems based on molten salts known as ionic liquids (ILs) got into the focus of interest. Many new approaches for the beneficial application of the interesting solvent have been published over the last years. ILs bring beneficial properties compared to organic solvents like nonflammability and nonvolatility. There are two possible ways to use the ILs: first, the hydrophobic ones as a substitute for organic solvents in pure two-phase systems with water and second, the hydrophilic ones in aqueous two-phase systems (ATPS). To effectively utilise IL-based two-phase systems or IL-based ATPS in biotechnology, extensive experimental work is required to gain the optimal system parameters to ensure selective extraction of the product of interest. This review will focus on the most actual findings dealing with the basic driving forces for the target extraction in IL-based ATPS as well as presenting some selected examples for the beneficial application of ILs as a substitute for organic solvents. Besides the research focusing on IL-based two-phase systems, the “green aspect” of ILs, due to their negligible vapour pressure, is widely discussed. We will present the newest results concerning ecotoxicity of ILs to get an overview of the state of the art concerning ILs and their utilisation in novel two-phase systems in biotechnology.     

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.     

An enzymatic method for radiolabeling vertebrate vitellogenin

Partition in aqueous two-phase systems should have great potentialities for studies of biological material. However, the general use of the method has probably been hindered by the difficulties in finding the composition of two-phase systems with desired qualities. Experimental design has proved to be of immense value for optimization in many different areas and should also be useful in selecting the best possible two-phase system. Therefore the simplex method has been applied to the search for the composition of an aqueous two-phase system in which the partition behavior of filamentous actin and human spectrin differ as much as possible.     

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.     

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.     

Novel polymer-polymer conjugates for recovery of lactic acid by aqueous two-phase extraction

A new family of polymer conjugates is proposed to overcome constraints in the applicability of aqueous two-phase systems for the recovery of lactic acid. Polyethylene glycol-polyethylenimine (PEI) conjugates and ethylene oxide propylene oxide-PEI (EOPO-PEI) conjugates were synthesized. Aqueous two-phase systems were generated when the conjugates were mixed with fractionated dextran or crude hydrolyzed starch. With 2% phosphate buffer in the systems, phase diagrams with critical points of 3.9% EOPO-PEI-3.8% dextran (DEX) and 3.5% EOPO-PEI-7.9% crude starch were obtained. The phase separation temperature of 10% EOPO-PEI solutions titrated with lactic acid to pH 6 was 35 degrees C at 5% phosphate, and increased linearly to 63 degrees C at 2% phosphate. Lactic acid partitioned to the top conjugate-rich phase of the new aqueous two-phase systems. In particular, the lactic acid partition coefficient was 2.1 in 10% EOPO-PEI-8% DEX systems containing 2% phosphate. In the same systems, the partitioning of the lactic acid bacterium, Lactococcus lactis subsp. lactis, was 0.45. The partitioning of propionic, succinic, and citric acids was also determined in the new aqueous two-phase systems.     

Two-phase systems: potential for in situ extraction of microalgal products

Algae are currently used for production of niche products and are becoming increasingly interesting for the production of bulk commodities, such as biodiesel. For the production of these goods to become economically feasible, production costs will have to be lowered by one order of magnitude. The application of two-phase systems could be used to lower production costs. These systems circumvent the costly step of cell harvesting, whilst the product is extracted and prepared for downstream processing. The mechanism of extraction is a fundamental aspect of the practical question whether two-phase systems can be applied for in situ extraction, viz, simultaneous growth, product formation and extraction, or as a separate downstream processing step. Three possible mechanisms are discussed; 1) product excretion 2) cell permeabilization, and 3) cell death. It was shown that in the case of product excretion, the application of two-phase systems for in situ extraction can be very valuable. With permeabilization and cell death, in situ extraction is not ideal, but the application of two-phase systems as downstream extraction steps can be part of a well-designed biorefinery process. In this way, processing costs can be decreased while the product is mildly and selectively extracted.Thus far none of the algal strains used in two-phase systems have been shown to excrete their product; the output has always been the result of cell death. Two-phase systems can be a good approach as a downstream processing step for these species. For future applications of two-phase in situ extraction in algal production processes, either new species that show product excretion should be discovered, or existing species should be modified to induce product excretion.     

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     

A new approach based on monitoring of phase formation kinetics for examination of biological particles and cells,using aqueous two phase polymer systems

An original technique of use of two-phase polymer systems as an analytical research method is described. The technique is based on the absorbance change of two-phase systems in visible spectrum during formation of the phases. Dynamics of this process was demonstrated as the kinetic curves. Addition of studied objects (macromolecules or cells) to the two-phase system modified the shape of the kinetic curve, depending on their individual surface properties. The technique has the following advantages as compared with traditional procedures of the particle surface analysis with the help of two-phase polymer systems: examination of particles with partition coefficients approaching zero; multiple analyses of the same samples; use of interphase as a matrix for study of spontaneous formation of studied particle complexes. The opportunities of the technique were demonstrated in a series of previous authors' works.     

A new approach based on monitoring of phase formation kinetics for examination of biological particles and cells,using aqueous two phase polymer systems

An original technique of use of two-phase polymer systems as an analytical research method is described. The technique is based on the absorbance change of two-phase systems in visible spectrum during formation of the phases. Dynamics of this process was demonstrated as the kinetic curves. Addition of studied objects (macromolecules or cells) to the two-phase system modified the shape of the kinetic curve, depending on their individual surface properties. The technique has the following advantages as compared with traditional procedures of the particle surface analysis with the help of two-phase polymer systems: examination of particles with partition coefficients approaching zero; multiple analyses of the same samples; use of interphase as a matrix for study of spontaneous formation of studied particle complexes. The opportunities of the technique were demonstrated in a series of previous authors' works.     

Separation of cephalosporin C and desacetyl cephalosporin C by high speed counter-current chromatography in aqueous two-phase systems

Summary In the recovery of cephalosporin C (CPC) from fermentation broth, the separation of desacetyl cephalosporin C (DAC) is a major concern. Multistage extraction in aqueous two-phase systems, mainly PEG/ammonium sulfate systems, proved to be promising. In preparative scale operation, high speed counter-current chromatography (HSCCC) with eccentric columns was used with aqueous two-phase systems to obtain baseline resolution of CPC and DAC. Solvents (e.g. 5% acetone) or neutral salts (e.g. 1.45% KSCN) added into aqueous two-phase systems enhanced the separation efficiency. Operation parameters of HSCCC such as rotational speed and mobile phase flow rate can affect the retention of the stationary phase and HETP.     

Preparation of benzoyl dextran and its use in aqueous two-phase systems.

The graft modification of dextran with benzoyl groups has been studied. The factors that affect the degree of substitution of benzoyl dextran were investigated. Phase diagrams for aqueous two-phase systems composed of polyethylene glycol/benzoyl dextran and dextran/benzoyl dextran have been determined. Phase separation was also obtained in aqueous solution of two benzoyl dextran polymers with different degrees of substitution. A four-phase system was obtained with a mixture of polyethylene glycol, dextran and two kinds of benzoyl dextrans. The partitioning of methylene blue and a Procion yellow HE-3G dextran derivative were studied in polyethylene glycol/benzoyl dextran and dextran/benzoyl dextran two-phase systems and in systems of two benzoyl dextrans differing in degree of substitution. The proteins bovine serum albumin and glucose-6-phosphate dehydrogenase were partitioned in polyethylene glycol/benzoyl dextran aqueous two-phase systems and the effect of the degree of substitution of benzoyl dextran was studied. Chlorella pyrenoidosa, thylakoid membrane vesicles, plasma membrane vesicles and chloroplasts were partitioned in polyethylene glycol/benzoyl dextran and dextran/benzoyl dextran two-phase systems, and in a polyethylene glycol/dextran/benzoyl dextran four-phase system.     

Aqueous polymer two-phase systems: effective tools for plasma membrane proteomics

Plasma membranes (PMs) are of particular importance for all living cells. They form a selectively permeable barrier to the environment. Many essential tasks of PMs are carried out by their proteinaceous components, including molecular transport, cell-cell interactions, and signal transduction. Due to the key role of these proteins for cellular function, they take center-stage in basic and applied research. A major problem towards in-depth identification and characterization of PM proteins by modern proteomic approaches is their low abundance and immense heterogeneity in different cells. Highly selective and efficient purification protocols are hence essential to any PM proteome analysis. An effective tool for preparative isolation of PMs is partitioning in aqueous polymer two-phase systems. In two-phase systems, membranes are separated according to differences in surface properties rather than size and density. Despite their rare application to the fractionation of animal tissues and cells, they represent an attractive alternative to conventional fractionation protocols. Here, we review the principles of partitioning using aqueous polymer two-phase systems and compare aqueous polymer two-phase systems with other methods currently used for the isolation of PMs.     

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.     

Protein separation using metal ion-bound particles in aqueous two-phase system

Metal ion affinity partitioning of protein in aqueous two-phase systems was studied using Sepharose as ligand carrier as an integrated adsorption partitioning. Cu(II)-bound Sepharose was mixed with protein solution and an aqueous two-phase system. The affinity sorbent was distributed quantitatively to the upper side or the interface. The binding studies of lysozyme to copper-bound gel in PEG/dextran two-phase systems demonstrate the feasibility of this bioseparation process. PEG/dextran system did not affect binding and elution of lysozyme to and from the Cu(II)-Sepharose particles.     

Metal affinity extraction of human hemoglobin in an aqueous polyethylene glycol-sodium sulfate two-phase system

Summary We have developed a protein extraction technique which uses metal affinity ligands in PEG/salt aqueous two-phase systems. Cu(II)IDA-PEG will partition proteins according to their surface histidine contents in two-phase systems formed from sodium sulfate and polyethylene glycol. The nearly complete separation of human hemoglobin and human serum albumin in a single stage is presented as a demonstration of the effectiveness of metal affinity extraction in PEG/salt systems.