Aspects Of Biocatalyst Stability In Organic Solvents

The stability of biocatalysis in systems containing organic solvents is reviewed. Among the examples presented are homogeneous mixtures of water and water-miscible organic solvents, aqueous/organic two-phase systems, solid biocatalysts suspended in organic solvents, enzymes in reverse micelles and modified enzymes soluble in water immiscible solvents. The stability of biocatalysts in organic solvents depends very much on the conditions. The hydrophobicity or the polarity of the solvent is clearly of great importance. More hydrophobic solvents (higher log P values) are less harmful to enzymes than less hydrophobic solvents. The water content of the system is a very important parameter. Some water is essential for enzymatic activity; however, the stability of enzymes decreases with increasing water content. Mechanisms of enzyme inactivation are discussed.     

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.     

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.     

Biocatalysis in organic media

The potentials of using organic reaction media in biotechnological conversions have already been demonstrated in several experimental studies. Examples of possible advantages are: possibility of higher substrate and/or product concentrations, favorable shift of reaction equilibria, reduced substrate and/or product inhibition, and facilitated product recovery. Especially water/organic solvent two-phase systems seem to possess several of these advantages. The solvent type will highly affect kinetics and stability of the (immobilized) biocatalyst, solubility and partitioning of reactants/products, and product recovery. Therefore the solvent choice can have a large influence on the economics of the two-liquid-phase biocatalytic process. Immobilization of the biocatalyst may be useful to provide protection against denaturating solvent effects. The polarity of the employed support material will also be decisive for the partitioning of substrates and products among the various phases.

A classification of biphasic systems, which is based on the possible types of theoretical concentration profiles and aqueous phase configurations, is discussed. Reversed micelles and aqueous two-liquid-phase systems can be considered as special cases. The design of two-liquid-phase bioreactors is dependent on the state of the biocatalyst, free or immobilized, and on the necessity for emulsification of one of the two liquid phases in the other. Many mass-transfer resistances, e.g. across the liquid/liquid interface, in the aqueous phase, across the liquid/solid interface, and in the biocatalyst phase, can limit the overall reaction rate. The epoxidation of alkenes in water/solvent two-phase systems is discussed to give an example of the scope of biotechnological processes that is obtained by using organic media. Finally, a design calculation of a packed-bed organic-liquid-phasel immobilized-biocatalyst reactor for the epoxidation of propene is given to illustrate some of the above aspects.     

Micellar enzymology

Experimental approaches to modelling the enzymatic function of biological membranes are discussed. Emphasis is given to pseudohomogeneous systems such as proteolipid complexes and enzymes in organic solvents; the latter are solubilized with phospholipids or synthetic surfactants. Methods for producing and studying such micellar systems are considered. The key research problems of micellar enzymology are formulated and its relation to enzyme membranology is discussed. Finally, the new potentialities are noted of applied enzymology (biotechnology) offered by application of a colloidal solution of water in organic solvents as a microheterogeneous medium for enzymatic reactions.     

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.     

Strategies for enzymatic esterification in organic solvents: comparison of microaqueous, biphasic, and micellar systems.

The kinetics of butyl butyrate synthesis by a lipase from Mucor miehei in different types of organic media were investigated. The three systems studied were a microaqueous medium containing enzyme in suspension in hexane, a water-hexane two-phase system, and reverse micelles. The synthesis of butyl butyrate was possible in all cases because of a favorable partition of the ester into the organic solvent. A sufficient stirring rate was necessary to achieve good reaction rates in the case of the liquid-liquid biphasic medium. The effect of water content was different according to the type of system used. The dependence of reaction rate and of conversion yield on enzyme and substrate concentrations was also investigated. From an applied point of view, the best performances were obtained with either microaqueous or liquid-liquid two-phase systems. The use of reverse micelles can be advocated only in particular conditions, such as low enzyme concentration, compatible with the specific constraints it involves.     

Factor affecting enzyme characteristics of bilirubin oxidase suspensions in organic solvents

The activity of bilirubin oxidase toward bilirubin was studied in a liquid/solid two-phase low-water organic system using a simple spectrophotometric assay to follow the reaction. The enzyme was lyophilized from aqueous solution before being suspended in the organic solvent reaction medium. The activity was significantly influenced by the properties of the aqueous medium from which the enzyme was lyophilized, specifically its pH, and the quantity and nature of the buffering species. Analyses of these effect showed that the role of buffering species in such systems went beyond their effect in fixing the protonation state of the enzyme. The activity was also influenced by the quantity of water added to the organic solvent reaction medium. The reaction was shown to follow Michaelis-Menten Kinetics, and K(m) and k(cat) were determined. The liquid/solid two-phase system studied was extensively compared to a previously studied water-in-oil microemulsion system (c) 1993 Wiley & Sons, Inc.     

Recent Developments in NAD(P)H Regeneration for Enzymatic Reductions in One- and Two-Phase Systems

This review discusses recent achievements in the field of cofactor regeneration for the nicotinamide cofactors NADH and NADPH. The examples discussed include alcohol dehydrogenases, formate dehydrogenase, glucose dehydrogenase and a hydrogenase. For the reaction either one-phase systems or two-phase systems in combination with an organic solvent are discussed. For the enantioselective reduction of 2-octanone to (R)-2-octanol it could be shown that enzyme coupled NADPH regeneration with glucose dehydrogenase and glucose results in shorter reaction times and higher yields when compared to the substrate coupled regeneration with 2-propanol.     

两相系统在疏水性有机污染物高效降解菌富集培养中的应用研究进展

环境中疏水性有机污染物(Hydrophobic organic pollutants,HOPs)的浓度日益增加,获取HOPs高效降解功能微生物能有效提高HOPs污染治理效率。近年来,利用两相系统促进HOPs微生物降解转化的研究已取得一定进展。本文重点从两相系统的结构特点及其富集HOPs降解功能微生物的原理、主要影响因素和应用情况等方面进行综述,并在此基础上对两相系统在毒害性HOPs微生物加速降解脱毒中所存在的主要问题及其应用前景进行讨论和展望。     

Partition of synaptic membranes in aqueous two-phase systems at subzero temperatures by using anti-freeze solvent

The freezing point of aqueous two-phase (liquid-liquid) systems containing water, dextran and poly(ethylene glycol) has been lowered by including glycerol. Biological membranes, obtained by fragmentation of a crude synaptosomal preparation from calf brain cortex, have been included in the two-phase systems. The effects of temperature and the concentration of glycerol on the partition of the membranes within the systems have been investigated. Considerable stabilisation of the membranes was noticed when they were partitioned at -10 degrees C compared with 0 degrees C. The influences of glycerol, ethylene glycol, N,N-dimethylformamide and tetrahydrofuran on the phase-forming properties of the systems and on enzyme activities are also presented. Possible use of the above systems for studies and separation of biological membranes are discussed.     

Bioremediation of phenol by a novel partitioning bioreactor using cow dung microbial consortia

A bioreactor has been designed and developed for partitioning of aqueous and organic phases with a provision for aeration and stirring, a cooling system and a sampling port. The potential of a cow dung microbial consortium has been assessed for bioremediation of phenol in a single-phase bioreactor and a two-phase partitioning bioreactor. The advantages of the two-phase partitioning bioreactor are discussed. The Pseudomonas putida IFO 14671 has been isolated, cultured and identified from the cow dung microbial consortium as a high-potential phenol degrader. The methods developed in this study present an advance in bioremediation techniques for the biodegradation of organic compounds such as phenol using a bioreactor. We have also demonstrated the potential of microorganisms from cow dung as a source of biomass.     

Whole cell biocatalysis in nonconventional media

Summary In this paper biocatalytic reactions carried out by whole cells in nonconventional media are reviewed. Similar relationships are observed between solvent hydrophobicity and catalytic activity in reactions carried out by isolated enzymes and whole cells. In addition to the effect of organic solvent on biocatalyst stability, microbial cells are susceptible to damaging effects caused by the organic phase. In general, more hydrophobic solvents manifest lower toxicity towards the cells. Whole cell biocatalysts require more water than isolated enzymes and two-phase systems have been most widely used to study whole cell biocatalysis. Immobilization makes cell biocatalysts more resistant to organic solvents and helps achieve homogeneous biocatalyst dispersion. Cell entrapment methods have been widely used with organic solvent systems and mixtures of natural and/or synthetic polymers allow adjustment of the hydrophobicity-hydrophilicity balance of the support matrix. Some examples of stereoselective catalysis using microbial cells in organic solvent media are presented.     

Two-phase partitioning bioreactors in fermentation technology

The two-phase partitioning bioreactor concept appears to have a great potential in enhancing the productivity of many bioprocesses. The proper selection of an organic solvent is the key to successful application of this approach in industrial practice. The integration of fermentation and a primary product separation step has a positive impact on the productivity of many fermentation processes. The controlled substrate delivery from the organic to the aqueous phase opens a new area of application of this strategy to biodegradation of xenobiotics. In this review, the most recent advances in the application of two-liquid phase partitioning bioreactors for product or substrate partitioning are discussed. Modeling and performance optimization studies related to those bioreactor systems are also reviewed.     

The water-dependence of the catalytic activity of bilirubin oxidase suspensions in low-water systems.

We investigated the enzymic activity of bilirubin oxidase when it is suspended as a lyophilized powder in a low-water system. The enzyme required buffer salts and a source of water to show activity. This study investigated the complete range of water thermodynamic activity (a(w)) by combining the use of salt hydrates and two-phase systems with concentrated solutes in the aqueous phase. When free water was added, activity reached a maximum at a defined water content, but this maximum increased with buffer content, suggesting that there was competition for water with the buffer salts from which the enzyme was lyophilized. Alternatively, a range of salt hydrates was used, each able to fix the water activity (a(w)) at a different value. By providing water to the organic solvent phase in this way, the dependency of enzyme activity upon a(w) was investigated and shown to be independent of buffer concentration. However, the optimum a(w) was uncertain because the available a(w) range for salt hydrates is < or = 0.90. Investigation of the remaining water activity range was made possible by using an a(w) depressor (sorbitol) to lower the a(w) of a two-phase system. The optimum a(w) for the bilirubin oxidase activity in this two-phase system was a(w) = 0.936, independent of buffer concentration. The study therefore confirmed the need to control the water 'available' to low-water systems and the dependence of enzyme activity on water thermodynamic activity (a(w)) not water content.     

Investigation and characterization of liquid two-phase systems for the separation of crystal mixtures by interfacial partitioning

The interfacial partitioning behavior of ampicillin and phenylglycine crystals in different two-phase systems has been investigated. The two-phase systems employed are water/dodecane, water/1-butanol, and water/pentane/methanol. By means of partition experiments and microscopic imaging, it has been shown that the mechanism of separation strongly depends on the choice of the two-phase system. While water/dodecane features a mechanism of sheer competitive adsorption at the interface, separation in water/1-butanol is mainly due to partitioning into both liquid phases, leading to a higher degree of separation. Experiments with water/pentane/methanol have illustrated the large potential of three-component systems, as slight variations in the composition can have large effects on the separation.     

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.     

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。