Effects of organic solvents and substrate binding on trypsin in acetonitrile and hexane media

In this work, we used molecular dynamic (MD) simulation to study trypsin with and without a six-amino-acid peptide bound in three different solvents (water, acetonitrile and hexane) in order to provide molecular information for well understanding the structure and function of enzymes in non-aqueous media. The results show that the enzyme is more compact and less native-like in hexane than in the other two polar solvents. The substrate could stabilize the native protein structure in the two polar media, but not in the non-polar hexane. There are no significant differences in the conformation of the S1 pocket upon the substrate binding in water and acetonitrile media while a reverse behavior is observed in hexane media, implying a possible induced fit binding mechanism in the non-polar media. The substrate binding enhances the stability of catalytic H-bond network since it could expel the solvent molecules from the active site. The enzyme and the substrate appear to be more appropriate to the reactive conformation in the organic solvents compared with aqueous solution. There is much greater substrate binding strength in hexane media than the water and acetonitrile ones since the polar solvent significantly weakens electrostatic interactions, which are observed to be the main driving force to the binding. In addition, some residues of the S1 pocket could remain favorable contribution to the binding despite the solvent change, but with differences in the contribution extent, the number and the type of residues between the three media.

To keep or not to keep? the question of crystallographic waters for enzyme simulations in organic solvent

The use of enzymes in non-aqueous solvents expands the use of biocatalysts to hydrophobic substrates, with the ability to tune selectivity of reactions through solvent selection. Non-aqueous enzymology also allows for fundamental studies on the role of water and other solvents in enzyme structure, dynamics, and function. Molecular dynamics simulations serve as a powerful tool in this area, providing detailed atomic information about the effect of solvents on enzyme properties. However, a common protocol for non-aqueous enzyme simulations does not exist. If you want to simulate enzymes in non-aqueous solutions, how many and which crystallographic waters do you keep? In the present work, this question is addressed by determining which crystallographic water molecules lead most quickly to an equilibrated protein structure. Five different methods of selecting and keeping crystallographic waters are used in order to discover which crystallographic waters lead the protein structure to reach an equilibrated structure more rapidly in organic solutions. It is found that buried waters contribute most to rapid equilibration in organic solvent, with slow-diffusing waters giving similar results.     

Phospholipid synthesis by extracellular phospholipase A2 in organic solvents

The catalytic activity of extracellular phospholipase A2 was studied in low polarity solvents where hydrolytic enzymes have been demonstrated to catalyze synthesis reactions. It was demonstrated that extracellular phospholipase A2 can catalyze the esterification of lysophosphatidylcholine with oleic acid. Up to 6.5% of lysophosphatidylcholine can be esterified into phosphatidylcholine. This activity requires a preincubation of the enzyme in a pH 9 aqueous solution containing calcium, before the incubation in the non-aqueous solvent. No transfer of fatty acid between a phospholipid and a lysophospholipid or between two phospholipids was observed. These results may be useful in understanding the function of the membrane phospholipase A2 which may catalyze acylation or deacylation depending on the local physico-chemical environment.     

Biocatalysis in multi-phase reaction mixtures containing organic liquids

A wide range of enzymes and whole microbial cells will act as catalysts in reaction mixtures that contain 2 or more phases, one of which is an organic liquid (either a reactant or including water-immiscible organic solvents). These "biphasic" systems have a variety of structures, knowledge of which aids predictions about biocatalyst activity and stability. There is often a dilute aqueous solution phase (containing the biocatalyst), which may be emulsified with the organic phase, or "trapped" within catalyst particles; sometimes however there may only be traces of water adsorbed to the enzyme or cells. These reaction systems offer several advantages for industrial applications, notably the higher solubilities of many reactants of interest, and the ability of readily available hydrolytic enzymes to catalyse syntheses. The most non-polar organic liquids are least likely to inactivate biocatalysts, though many do remain active with relatively polar solvents. Modification of the biocatalyst may stabilise against inactivation, especially where this is due to direct contact with the phase interface. The mass transfer processes required in these systems remain poorly understood, particularly because the interfacial area is often unknown. Attractive continuous reactors may be operated using a packed bed of catalyst with a trapped aqueous phase.     

Activation of immobilized lipase in non-aqueous systems by hydrophobic poly-DL-tryptophan tethers

Many industrially important reactions use immobilized enzymes in non-aqueous, organic systems, particularly for the production of chiral compounds such as pharmaceutical precursors. The addition of a spacer molecule ("tether") between a supporting surface and enzyme often substantially improves the activity and stability of enzymes in aqueous solution. Most "long" linkers (e.g., polyethylene oxide derivatives) are relatively hydrophilic, improving the solubility of the linker-enzyme conjugate in polar environments, but this provides little benefit in non-polar environments such as organic solvents. We present a novel method for the covalent immobilization of enzymes on solid surfaces using a long, hydrophobic polytryptophan tether. Candida antarctica lipase B (CALB) was covalently immobilized on non-porous, functionalized 1-microm silica microspheres, with and without an intervening hydrophobic poly-DL-tryptophan tether (n approximately 78). The polytryptophan-tethered enzyme exhibited 35 times greater esterification of n-propanol with lauric acid in the organic phase and five times the hydrolytic activity against p-nitrophenol palmitate, compared to the activity of the same enzyme immobilized without tethers. In addition, the hydrophobic tethers caused the silica microspheres to disperse more readily in the organic phase, while the surface-immobilized control treatment was less lipophilic and quickly settled out of the organic phase when the suspensions were not vigorously mixed.     

Dramatic enhancement of enzymatic activity in organic solvents by lyoprotectants

When seven different hydrolytic enzymes (four proteases and three lipases) were lyophilized from aqueous solution containing a ligand, N-Ac-L-Phe-NH(2), their catalytic activity in anhydrous solvents was far greater (one to two orders of magnitude) than that of the enzymes lyophilized without the ligand. This ligand-induced activation was expressed regardless of whether the substrate employed in organic solvents structurally resembled the ligand. Furthermore, nonligand lyoprotectants [sorbitol, other sugars, and poly(ethylene glycol)] also dramaticaliy enhanced enzymatic activity in anhydrous solvents when present in enzyme aqueous solution prior to lyophilization. The effects of the ligand and of the lyoprotectants were nonadditive, suggesting the same mechanism of action. Excipient activated and nonactivated enzymes exhibited identical activities in water. Also, addition of the excipients directly to suspensions of nonactivated enzymes in organic solvents had no appreciable effect on catalytic activity. These observations indicate that the mechanism of the excipient-induced activation is based on the ability of the excipients to alleviate reversible denaturation of enzymes upon lyophilization. Activity enhancement induced by the excipients is displayed even after their removal by washing enzymes with anhydrous solvents. Subtilisin Carlsberg, lyophilized with sorbitol, was found to be a much more efficient practical catalyst than its "regular" counterpart. (c) 1993 John Wiley & Sons, Inc.     

Effect of organic solvents on stability and activity of two related alcohol dehydrogenases: a comparative study.

A comparative study was performed regarding the catalytic activity and stability of two related enzymes (thermophilic alcohol dehydrogenase from Thermoanaerobacter brockii and its mesophilic counterpart from yeast) in the presence of a number of miscible and immiscible organic solvents. The study was performed in view of the practical usefulness of organic solvents for alcohol dehydrogenases which have been shown to catalyse a variety of industrially-important dehydrogenation reactions. A number of organic solvents of different physicochemical characteristics were used and substantial stabilization was achieved. The non-polar solvents utilized showed the ability to enhance thermal stability of both proteins. Protection against thermal denaturation was especially pronounced by n-dodecane, the solvent with the highest logP used in the present study. Dimethylformamide and dioxane, employed as two miscible organic solvents, showed the ability to cause substrate inhibition and changes in protein conformation as indicated by kinetic and fluorescence studies. A higher resistance of the thermophilic protein to the deleterious effect of pyridine and thermostabilization of the mesophilic enzyme by non-polar solvents are especially emphasized. Combined differences in protein structure and nature of organic solvents are suggested to explain the differences in stability and catalytic activity observed in the present investigation.     

Hydrogen ions in microaqueous phase during lipase catalysed esterification in non-aqueous media

Lipase catalysed stearoyl lactic acid preparation in non-aqueous media was treated as a model system to study the microaqueous phase containing hydrogen ions arising from dissociation of water soluble lactic acid in it. The thermodynamic factors operating at the microaqueous enzyme-water-solvent phase on the lipase in non-polar solvents were investigated in terms of the water of reaction which constitutes the microaqueous phase, partitioning of acid between water of the microaqueous phase and the organic solvent, dissolution and dissociation of the acid and the resultant number of H+ present in the microaqueous phase and the extent of esterification for a given amount of enzyme at various substrate concentrations. Using mass transfer equations, the theoretical number of H+ at the microaqueous phase were calculated and expressed as hydrogen ion numbers to generate plots which indicated various thermodynamic processes operating at the microaqueous phase to maintain this concentration to a safe minimum.     

Hydrolytic reactions in two-phase systems. Effect of water-immiscible organic solvents on stability and activity of acid phosphatase, beta-glucosidase, and beta-fructofuranosidase.

The stability and activity of three hydrolytic enzymes, acid phosphatase (EC 3.1.3.2), beta-fructofuranosidase (EC 3.2.1.26), and beta-glucosidase (EC 3.2.1.4), were studied at 30 degrees C in two-phase systems. They were prepared with equal quantities of buffered water and a water-immiscible organic solvent. Low-molecular-weight acetates and paraffins were tested in this investigation. The kinetic constant of storage inactivation was correlated with the logarithm of solvent polarity. Enzyme stability in the presence of organic phases, whose log P value was included in 1.2-2.2, was greater than the one measured in pure buffered aqueous media. On the other hand, a dramatic enzyme denaturation took place making use of solvents at higher log P-value. Experiments carried out during the 24-h operation clarified that the reaction yield does not depend solely on solvent polarity. Acid phosphatase and beta-glucosidase, which are less resistant than beta-fructofuranosidase to temperature and shear in buffered solutions, showed especially significant enhancement of catalytic activity when hydrolysis was performed with the addition of acetates (50% v/v).     

Enzymes in Low Water Systems

Water is fundamental for enzyme action and for formation of the three-dimensional structure of proteins. Hence, it may be assumed that studies on the interplay between water and enzymes can yield insight into enzyme function and formation. This has proven correct, because the numerous studies that have been made on the behavior of water-soluble and membrane enzymes in systems with a low water content (reverse micelles or enzymes suspended in nonpolar organic solvents) have revealed properties of enzymes that are not easily appreciated in aqueous solutions. In the low water systems, it has been possible to probe the relation between solvent and enzyme kinetics, as well as some of the factors that affect enzyme thermostability and catalysis. Furthermore, the studies show that low water environments can be used to stabilize conformers that exhibit unsuspected catalytic properties, as well as intermediates of enzyme function and formation that in aqueous media have relatively short life-times. The structure of enzymes in these unnatural conditions is actively being explored.     

Lipase-catalyzed cellulose acetylation in aqueous and organic media

Screening for lipases capable of catalyzing acetylation of cellulosic substrates was conducted in aqueous buffer solution using water-soluble carboxymethyl cellulose (CMC) as substrate. Lipase A12 from Aspergillus niger (A. niger) showed the most promising acetylation activity among 11 tested commercial microbial lipases and was further applied to catalyzing acetylation of solid cellulose in aqueous solution. This reaction was shown to be feasible with an acetylation extent of 0.16 wt % achieved compared with no detectable acetylation in the absence of enzyme. Pretreatments on cellulose substrate by ultrasonic irradiation and surfactant solution only slightly improved the acetylation extent by 44 and 27%, respectively. Alternatively, this lipase-catalyzed acetylation was remarkably improved with solubilized cellulose as substrate in the dimethyl sulfoxide/paraformaldehyde solvent system, with an acetylation extent (7.87 wt %) nearly 50 times higher than that achieved in aqueous solution. This improvement was attributed to (1) the absence of bulk water and the increase in substrate solubility by the transition of reaction media from aqueous solution to organic solvents and (2) the ability of lipase A12 to remain catalytically active in highly polar DMSO. This discovery that the A. niger lipase was capable of surviving its contact with polar solvents was further confirmed by its considerably preserved catalytic activity on CMC acetylation in aqueous media after enzyme pretreatments with organic solvents of various polarities and in mixture media with the aqueous phase partially replaced by organic solvents.     

Effects of non-aqueous solvents on CO2 absorption in monoethanolamine: Ab initio calculations

Monoethanolamine (MEA) is the most typical alkanolamine and its aqueous solutions are widely used for CO₂ absorption with mature technology, but the regeneration process is energy consuming. To reduce the energy demand, non-aqueous solvents, such as methanol and ethanol are proposed to substitute water in amine solutions. To understand the influence of the aqueous and non-aqueous solvents on CO₂ capture process, the chemical reactions of MEA absorbing CO₂ were conducted via ab initio calculations. The non-aqueous solvents discussed in this paper are methanol, ethanol, 1-propanol and 2-propanol. The reaction patterns were investigated and energy barriers were observed. The results show that zwitterion formation and the followed intermolecular hydrogen transfer are proven to be the most possible reaction pattern in both aqueous and non-aqueous solvents. The energy analysis shows that the forward reaction energy barriers increase while the backward barriers decrease as the solvent changes from water to methanol, ethanol, 1-propanol and 2-propanol in turn. The decreases of the energy barriers for backward processes are much higher than the corresponding increases for forward processes. These results indicate that lower energies are required in non-aqueous solvents than in water during the desorption reactions and the non-aqueous solvents are very promising to reduce the regeneration energy consumption in MEA capturing CO₂ process. Moreover, the reaction energy gaps between different solvation effects were found to have linear relationship with the logarithm of the dielectric constant difference, which could provide an easy way to theoretically predict the reaction energies of monoethanolamine absorbing CO₂ in other solvation effect and can be used to screen appropriate CO₂ capture solvent.     

Engineering enzymes for non-aqueous solvents.

Enzymes may be redesigned to permit catalysis in non-aqueous solvents by engineering their amino acid sequences, thereby altering their physical and chemical properties to suit the new solvent environment. The interactions that contribute to protein stability in non-aqueous solvents are discussed in the context of attempting to identify possible approaches to constructing enzymes which exhibit enhanced stability in non-aqueous media. These approaches are illustrated by several examples where protein engineering has resulted in enzymes that are better suited for catalysis in organic solvents.     

Catalytic activity and denaturation of enzymes in water/organic cosolvent mixtures. Alpha-chymotrypsin and laccase in mixed water/alcohol, water/glycol and water/formamide solvents

The dependence of the catalytic activities of alpha-chymotrypsin and laccase on the concentration of organic cosolvents (alcohols, glycols and formamides) in mixed aqueous media has a pronounced threshold character: it does not change up to a critical concentration of the non-aqueous cosolvents added, yet further increase of the latter (by only a small percentage, by vol.) leads to an abrupt decrease in enzyme activity. Fluorescence studies indicate that the inactivation results from reversible conformational changes (denaturation) of the enzymes. There is a linear correlation between the critical concentration of residual water (at which the enzyme inactivation occurs in a threshold manner) and the hydrophobicity of the organic cosolvents added. A quantitative criterion is suggested for the selection of organic cosolvents to be used for enzymatic reactions in homogeneous water/organic solvent media.     

Predicting enzyme behavior in nonconventional media: correlating nitrilase function with solvent properties

The insolubility of nitrile substrates in aqueous reaction mixture decreases the enzymatic reaction rate. We studied the interaction of fourteen water miscible organic solvents with immobilized nitrile hydrolyzing biocatalyst. Correlation of nitrilase function with physico-chemical properties of the solvents has allowed us to predict the enzyme behavior in such non-conventional media. Addition of organic solvent up to a critical concentration leads to an enhancement in reaction rate, however, any further increase beyond the critical concentration in the latter leads to the decrease in catalytic efficiency of the enzyme, probably due to protein denaturation. The solvent dielectric constant (epsilon) showed a linear correlation with the critical concentration of the solvent used and the extent of nitrile hydrolysis. Unlike alcohols, the reaction rate in case of aprotic solvents could be linearly correlated to solvent log P. Further, kinetic analysis confirmed that the affinity of the enzyme for its substrate (K (m)) was highly dependent upon the aprotic solvent used. Finally, the prospect of solvent engineering also permitted the control of enzyme enantioselectivity by regulating enantiomer traffic at the active site.     

Reverse micelles as a versatile medium for the study of lactate dehydrogenase in vitro

Rabbit muscle lactate dehydrogenase has been solubilized in cationic reverse micelles of cetyltrimethyl ammonium bromide (CTAB) and isooctane-chloroform (1:1, V/V). The activity of the enzyme was notably affected by the change in water pool, pH, and concentration of the surfactant. Lactate dehydrogenase showed its full activity in this reverse micellar system in non-aqueous solvent under specific conditions at a Wo value of 30.55, pH 7.0, and 100 mM CTAB in comparison to the activity measured in aqueous system under optimum conditions. These results indicate that even the large and complex enzymes (M.W. hundred thousand and four subunits) can be solubilized in apolar solvents where they may retain their conformational integrity and oligomericity, i.e., optimum subunit-subunit interaction with maintenance of full activity.     

微生物嗜盐酶的研究进展

嗜盐酶一般来自于嗜盐菌,它的主要特点是严格依赖体系中一定的盐离子浓度,可以在高盐环境中维持其结构稳定,并且能够抵抗高温、p H和有机溶剂存在下的变性,因此在高盐、水/有机和非水介质环境的催化中具有重要的应用价值。本综述从盐对嗜盐酶活性和稳定性的影响、金属离子和有机溶剂对嗜盐酶的影响几个方面介绍了嗜盐酶的特点。在总结蛋白质数据库(PDB)中已有嗜盐酶的结构和特点的基础上,对嗜盐酶的嗜盐机制进行了分析,认为嗜盐酶不同于非嗜盐酶的特点在于盐桥和氢键明显增多,含有一些特殊的盐离子结合位点并且常以低聚体的形式存在,表面酸性氨基酸含量明显增多。最后对嗜盐酶的分子改造和应用进行了简要的介绍。     

Role of organic solvents on Pa-hydroxynitrile lyase interfacial activity and stability

Catalytic activity and adsorption of Pa-hydroxynitrile lyase (Pa-Hnl) was investigated at various organic solvent/water interfaces. We focused on the role of solvent polarity in promoting activity and stability in two-phase systems, specifically for the solvents heptane, dibutyl ether (DBE), diisopropyl ether (DIPE), butylmethyl ether (BME), and methyl tert-butyl ether (MTBE). Enzyme activity towards mandelonitrile cleavage was determined in a recycle reactor with a well-defined interfacial area as described by Hickel, et al. 1999. Here the recycle reactor was modified to permit exchange of the aqueous phase. With this modification, irreversibility of enzyme adsorption was determined as a function of the adsorption time at the interface. Irreversibility of enzyme adsorption was also investigated by measuring the surface pressure of a sessile-drop upon washout. We find that Pa-Hnl exhibits the highest stability but the lowest initial catalytic activity at the aqueous/organic solvent interface with the most polar organic solvents. Thus, DIPE and MTBE display no loss in enzyme activity over a period of several hours. However, the more apolar the solvent is the higher the initial Pa-Hnl activity, but the faster the loss of activity. Dynamic tensiometry reveals that Pa-Hnl adsorbs more strongly at the interface of the more apolar solvents. Surprisingly, Pa-Hnl develops some irreversible adsorption after 30 min at the DIPE/water interface, but does not lose catalytic activity.     

Enhancement of hydrolytic activity of sphingolipid ceramide N-deacylase in the aqueous-organic biphasic system

Lysoglycosphingolipids were produced from glycosphingolipids by using sphingolipid ceramide N-deacylase, which cleaves the N-acyl linkage between fatty acids and sphingosine bases in various glycosphingolipids. The enzyme reaction was done in a biphasic media prepared with water;-immiscible organic solvent and aqueous buffer solution containing the enzyme. We investigated the effects of organic solvents and detergents on lysoglycosphingolipid production in the biphasic system. Among the organic solvents tested, n-butylbenzene, cumene, cyclodecane, cyclohexane, n-decane, diisopropylether, n-heptadecane, and methylcyclohexane promoted hydrolysis of GM1, whereas benzene, chloroform, ethyl acetate, and toluene inhibited GM1 hydrolysis. Hydrolysis of asialo GM1, GD1a, GalCer, and sulfatide was also enhanced by the addition of n-decane. The hydrolytic activity of the enzyme was enhanced by the addition of 0.8% sodium taurodeoxycholate or sodium cholate to the aqueous phase. The most effective hydrolysis of various glycosphingolipids by the enzyme was thus obtained in the aqueous-n-decane biphasic system containing 0.8% sodium taurodeoxycholate. Under this condition, the fatty acids released from GM1 by the action of the enzyme were trapped and diffused into the organic phase, while lysoGM1 remained in the aqueous phase.Thus the almost complete hydrolysis of GM1 was achieved using the biphasic system, while at most 70% of hydrolysis was obtained using normal aqueous media possibly due to the inhibition of hydrolysis reaction by accumulation of fatty acids in the reaction mixture.