High-affinity binding of water by proteins is similar in air and in organic solvents

Published data for water adsorption by proteins suspended in organic solvents (of interest as enzyme reaction mixtures) have been converted to a basis of thermodynamic water activity (aw). The resulting adsorption isotherms have been compared with those known for proteins equilibrated with water from a gas phase. This comparison can show any effects of the solvent on the interaction between the protein and water at the molecular level. At lower water contents (aw less than about 0.4), similar adsorption isotherms are found in each solvent and in the gas phase; differences are probably less than the likely errors. Hence, it may be concluded that the presence of an organic solvent has little effect on the interaction between proteins and tightly bound water; on a molecular scale there is probably little penetration of the primary hydration layer by solvent molecules, even fairly polar ones such as EtOH. At higher aw values, there are differences between the isotherms which probably are significant. Nonpolar solvents increase the amount of water bound by the enzyme (at fixed aw), while polar solvents (mainly EtOH) may reduce the amount of water bound by the enzyme, presumably by occupying part of the secondary hydration layers in place of water.     

Effect of thermodynamic water activity on amino-acid ester synthesis catalyzed by agarose-chymotrypsin in 3-pentanone.

Chymotrypsin linked to agarose beads by multi-point covalent attachment catalyzes synthesis of Ac-Trp-OEt in 3-pentanone even when the thermodynamic water activity (aw) of the system is reduced to as low as 0.4. If fully hydrated catalyst is added to the reaction mixture before removal of water, product is formed linearly once aw has stabilized. The initial rate is reduced from that if aw is kept close to 1 (0.47 mmol s-1 (kg enzyme)-1), to 50% (aw 0.9), 25% (aw 0.4) and < 1% (aw 0.25). The large drop between aw of 1 and 0.9 probably reflects the effects of water removal on the agarose gel structure. Catalyst partly dried (even only to aw 0.86) before adding to the organic phase is inactive. At reduced aw, the equilibrium (when reached) is shifted in favor of the ester, as expected.     

Effect of water activity on the lipase catalyzed esterification of geraniol in ionic liquid [bmim]PF6

Enzymatic reactions in non-aqueous media have been shown to be effective in carrying out chemical transformation where the reactants are insoluble in water or water is a byproduct limiting conversion. Ionic liquids, liquid organic salts with infinitesimal vapor pressure, are potentially useful alternatives to organic solvents. It is known that the thermodynamic water activity is an important variable affecting the activity of enzymes in non-aqueous solvents. This study investigated the influence of water activity on the esterification of geraniol with acetic acid in ionic liquid [bmim]PF6 catalyzed by immobilized Candida antarctica lipase B. The conversion of geraniol in [bmim]PF6 was significant although the reaction rate was slower than in organic solvents. The profile of initial reaction rate-water activity was determined experimentally, and differed from the data reported for other non-aqueous solvents. A maximum in the initial reaction rate was found at aw = 0.6. The pseudo reaction equilibrium constant, Kx, was measured experimentally for the reaction. The average value of Kx in [bmim]PF6 was 12, 20-fold lower than the value reported for the same system in hexane.     

Optimization of Pseudomonas cepacia lipase preparations for catalysis in organic solvents

The activity of different lipase (from Pseudomonas cepacia) forms, such as crude powder (crude PC), purified and lyophilized with PEG (PEG + PC), covalently linked to PEG (PEG-PC), cross-linked enzyme crystals (CLEC-PC), and immobilized in Sol-Gel-AK (Sol-Gel-AK-PC) was determined, at various water activities (aw), in carbon tetrachloride, benzene and 1,4-dioxane. The reaction of vinyl butyrate with 1-octanol was employed as a model and both transesterification (formation of 1-octyl butyrate) and hydrolysis (formation of butyric acid from vinyl butyrate) rates were determined. Both rates depended on the lipase form, solvent employed, and aw value. Hydrolysis rates always increased as a function of aw, while the optimum of aw for transesterification depended on the enzyme form and nature of the solvent. At proper aw, some lipase forms such as PEG + PC, PEG-PC, and Sol-Gel-AK-PC had a total activity in organic solvents (transesterification plus hydrolysis) which was close to (39 and 48%) or even higher than (130%) that displayed by the same amount of lipase protein in the hydrolysis of tributyrin-one of the substrates most commonly used as standard for the assay of lipase activity-in aqueous buffer. Instead, CLEC-PC and crude PC were much less active in organic solvents (2 and 12%) than in buffer. The results suggest that enzyme dispersion and/or proper enzyme conformation (favored by interaction with PEG or the hydrophobic Sol-Gel-AK matrix) are essential for the expression of high lipase activity in organic media.     

Enzymatic ester synthesis with continuous measurement of water activity

Ester synthesis from aliphatic monoalcohols and organic acids was investigated by using a microbial lipase. The reaction medium only contained the substrates and the enzyme without addition of water or organic solvent. During the reaction, water was produced and the water activity (aw) increased. Batch reactors and continuous-flow reactors were used. In batch, the aw was 0.13 at the beginning of the reaction and increased to reach a plateau at 0.77, after which ester synthesis continued without modification of the aw. Different alcohols and acids were tried in solid-liquid reactors, and all cases synthesis occurred, leading to a significant increase in the water activity. For continuous-flow reactors, the use of silica beads retaining water inside the reactor where the enzymatic reaction took place resulted in some control of the enzymatic reaction by changing the aw.     

Enantioselective synthesis of (S)‐naproxen using immobilized lipase on chitosan beads

S‐naproxen by enantioselective hydrolysis of racemic naproxen methyl ester was produced using immobilized lipase. The lipase enzyme was immobilized on chitosan beads, activated chitosan beads by glutaraldehyde, and Amberlite XAD7. In order to find an appropriate support for the hydrolysis reaction of racemic naproxen methyl ester, the conversion and enantioselectivity for all carriers were compared. In addition, effects of the volumetric ratio of two phases in different organic solvents, addition of cosolvent and surfactant, optimum pH and temperature, reusability, and inhibitory effect of methanol were investigated. The optimum volumetric ratio of two phases was defined as 3:2 of aqueous phase to organic phase. Various water miscible and water immiscible solvents were examined. Finally, isooctane was chosen as an organic solvent, while 2‐ethoxyethanol was added as a cosolvent in the organic phase of the reaction mixture. The optimum reaction conditions were determined to be 35 °C, pH 7, and 24 h. Addition of Tween‐80 in the organic phase increased the accessibility of immobilized enzyme to the reactant. The optimum organic phase compositions using a volumetric ratio of 2‐ethoxyethanol, isooctane and Tween‐80 were 3:7 and 0.1% (v /v/v), respectively. The best conversion and enantioselectivity of immobilized enzyme using chitosan beads activated by glutaraldehyde were 0.45 and 185, respectively.     

Modification of the Microenvironment of Enzymes in Organic Solvents. Substitution of Water by Polar Solvents

Enzyme catalysis in water-immiscible organic solvents is strongly influenced by the amount of water present in the reaction mixture. Effects of substitution of part of the water by other polar solvents were studied. In an alcoholysis reaction catalyzed by chymotrypsin deposited on celite, it was possible to exchange half of the water by formamide, ethylene glycol or dimethyl sulfoxide with often increased initial reaction rate. Furthermore, these substitutions caused the suppression of the competing hydrolysis reaction. However, formamide caused enzyme inactivation, and ethylene glycol participated as a reactant in the alcoholysis to some extent, hence dimethyl sulfoxide was considered the best water substitute among the solvents tested. These effects were noted for chymotrypsin catalyzed alcoholysis in several water immiscible solvents and also for interesterification reactions catalyzed by Candida cylindracea lipase on celite. In the latter case a change in the stereoselectivity was observed. At a low water content a high stereoselectivity was observed; when the amount of polar solvent was increased, either by doubling the water content or adding an equal amount of DMSO, the stereoselectivity decreased.     

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.     

Effect of water activity on thermolysin-catalyzed peptide synthesis in organic solvents

Summary The effect of water activity on the rate of thermolysin-catalyzed synthesis of an aspartame precursor has been investigated in water-miscible and water-immiscible solvents. In both cases, the enzyme reaction rate at a given water activity was found to be significantly different depending on the nature of the solvent. The reaction rates in water-immiscible solvents, where the water activities were close to 1.0, were found to be significantly dependent on the volume ratio of water to organic media and the hydrophobicity of the solvent. These data suggest that the enzyme reaction in the solvent is influenced appreciably by other factors in addition to the water activity.     

Enzymatic Reactions in Non-Conventional Media: Prediction of Solvent Water Content for Optimum Water Activity

Most enzymes provide their optimum performance at a given water activity (aw), which is generally solvent independent. For a given organic liquid solvent at a specific temperature or for a supercritical solvent at a specific temperature and pressure this corresponds to a water concentration in which water has the desired activity. We present here a methodology for predicting this water concentration thus reducing substantially the amount of experimental work needed to find the optimum solvent with respect to equilibrium conversion.

If the enzyme optimum water activity is known, the methodology predicts the required water content in the solvent to achieve this aw value. If, in addition, the enzyme water activity curve is available, this methodology provides the total water that must be added to the system (enzyme plus solvent) so that a specific water activity can be obtained.

The same methodology can also be applied to predict the effect of the total water content of the system (initial or initial plus produced) on the water activity values. It is shown that: (a) for esterification reactions taking place in hydrophobic organic solvents, the produced water can lead to a substantial change in water activity, but not for less hydrophobic solvents; (b) introduction of dry CO₂ into a system, pre-equilibrated to a certain water activity at atmospheric pressure, can lead to a substantial decrease in the water activity especially at temperatures just above the critical one of the solvent and pressures larger than that.     

Interfacial versus homogeneous enzymatic cleavage of mandelonitrile by hydroxynitrile lyase in a biphasic system

The question of an interfacial versus a homogeneous reaction is carefully addressed for the enzymatic biphasic cleavage of mandelonitrile to benzaldehyde by Prunus amygdalus hydroxynitrile lyase (pa-Hnl) (Hickel et al. [1999] Biotechnol Bioeng 36:425-436). Experimental evidence, including 1) the reaction ceases when the interface is populated by previously adsorbed denatured pa-Hnl, 2) the reaction continues even after washout of the bulk enzyme from the aqueous phase, 3) highly nonpolar organic solvents initially promote fast reaction kinetics that relatively quickly decay to zero product production, and 4) the reaction rate is nonlinear in the bulk enzyme concentration, provide robust grounds for an interfacial reaction. We also model enzymatic mandelonitrile cleavage assuming a homogeneous aqueous-phase reaction. The homogeneous reaction scheme does not simultaneously account for the experimental observations of a linear dependence of the reaction rate on organic/water interfacial area, no dependence on the aqueous-phase volume, and a nonlinear dependence on pa-Hnl aqueous concentration. Further, simple calculations demonstrate that the homogeneous reaction rate is at least three orders of magnitude slower than those observed by Hickel et al. (1999). We again conclude that enzyme adsorbed at the organic solvent/water interface primarily catalyzes the biphasic mandelonitrile cleavage reaction.     

Solid-phase peptide synthesis by ion-paired alpha-chymotrypsin in nonaqueous media

Solid-phase synthesis of dipeptides in low-water media was achieved using AOT ion-paired alpha-chymotrypsin solubilized in organic solvents. Multiple solvents and systematic variation of water activity, a(w), were used to examine the rate of coupling between N-alpha-benzyloxycarbonyl-L-phenylalanine methyl ester (Z-Phe-OMe) and leucine as a function of the reaction medium for both solid-phase and solution-phase reactions. In solution, the observed maximum reaction rate in a given solvent generally correlated with measures of hydrophobicity such as the log of the 1-octanol/water partitioning coefficient (log P) and the Hildebrand solubility parameter. The maximum rate for solution-phase synthesis (13 mmol/h g-enzyme) was obtained in a 90/10 (v/v) isooctane/tetrahydrofuran solvent mixture at an a(w) of 0.30. For the synthesis of dipeptides from solid-phase leucine residues, the highest synthetic rates (0.14-1.3 mmol/h g-enzyme) were confined to solvent environments that fell inside abruptly defined regions of solvent parameter space (e.g., log P > 2.3 and normalized electron acceptance index <0.13). The maximum rate for solid-phase synthesis was obtained in a 90/10 (v/v) isooctane/tetrahydrofuran solvent mixture at an a(w) of 0.14. In 90/10 and 70/30 (v/v) isooctane/tetrahydrofuran environments with a(w) set to 0.14, seven different N-protected dipeptides were synthesized on commercially available Tentagel support with yields of 74-98% in 24 h.     

Effect of water activity on enzyme hydration and enzyme reaction rate in organic solvents

The effects of water on enzyme (protein) hydration and catalytic efficiency of enzyme molecules in organic solvents have been analyzed in terms of the thermodynamic activity of water, which has been estimated by the NRTL or UNIFAC equations. When the amount of water bound to the enzyme was plotted as a function of water activity, the water adsorption isotherms obtained from the water-solvent liquid mixtures were similar to the reported water-vapor adsorption isotherms of proteins. The water adsorption of proteins from the organic media was not significantly dependent on the properties of the solvents or the nature of the proteins. It is also shown that there is a linear relationship between the logarithm of the enzyme reaction rate and water activity. However, the dependence of the enzyme reaction rate on water activity was found to be different depending on the properties of the solvent. The relationship between water activity and other solvent parameters such as solvent hydrophobicity and the solubility of water in the solvent is also discussed.     

One-pot synthesis in aqueous system for water-soluble chitosan-graft-poly(ethylene glycol) methyl ether

Chitosan is functionalized with poly(ethylene glycol) methyl ether (mPEG) at the amino and hydroxyl groups via a single step reaction in a homogeneous aqueous system. A chitosan aqueous solution obtained from the mixture of chitosan and hydroxybenzotriazole (HOBt) in water is a key factor in providing mild conditions to conjugate mPEG by using a carbodiimide conjugating agent. The reaction at ambient temperature for 24 h gives chitosan-g-mPEG with water solubility with mPEG content as high as 42%. This work demonstrates that a water-soluble chitosan-HOBt complex is an effective system for the preparation of chitosan derivatives via the aqueous system without the use of acids or organic solvents.     

水-有机溶剂两相体系中甲基单孢菌Z201细胞催化丙烯环氧化的初步研究

Laabe于1987年提出了生物催化剂工程(Biocatalyst engineering)和介质工程(Medium engineering)的概念^[1]。有机相生物催化中溶剂的选择也是介质工程的内容之一。纯酶在有机相中的催化作用已有大量报道^[2],但对完整细胞研究甚步。本文以甲基单胞菌(Methylomonas Z201)完整细胞为生物催化剂．丙烯环氧化为指标反应．研究有机溶剂对活性的影响并对催化活性——溶剂疏水性进行了相关性分析。研究了水一十六烷两相体系中十六烷含量和搅拌速度对丙烯环氧化速度的影响和细胞的操作稳定性。     

Destruction of cyanogen bromide and inorganic cyanides

Cyanogen bromide in water and seven organic solvents and sodium cyanide in water may safely and efficiently (greater than 99.7%) be destroyed using sodium hydroxide (1 M) solution and commercially available sodium or calcium hypochlorite. Details are given of an analytical procedure which can be used to check the final reaction mixture for the presence of residual cyanogen bromide or cyanide.     

Structural change and catalytic activity of horseradish peroxidase in oxidative polymerization of phenol

The effects of solvent and reaction conditions on the catalytic activity of horseradish peroxidase (HRP) were investigated for oxidative polymerization of phenol in water/organic mixtures using hydrogen peroxide as an oxidant. Also, the structural changes of HRP were investigated by CD and absorption spectroscopy in these solvents. The results suggest that the yield of phenol polymer (the conversion of phenol to polymer) is strongly affected by the reaction conditions due to the structural changes of HRP, that is, the changes in higher structure of the apo-protein and dissociation or decomposition of the prosthetic heme. Optimum solvent compositions for phenol polymerization depend on the nature of the organic solvents owing to different effects of the solvents on HRP structure. In addition to initial rapid changes, slower changes of HRP structure occur in water/organic solvents especially at high concentrations of organic solvents. In parallel with these structural changes, catalytic activity of HRP decreases with time in these solvents. At higher reaction temperatures, the yield of the polymer decreases, which is also ascribed to modification of HRP structure. It is known that hydrogen peroxide is an inhibitor of HRP, and the yield of phenol polymer is strongly dependent on the manner of addition of hydrogen peroxide to the reaction solutions. The polymer yield decreases significantly when hydrogen peroxide was added to the reaction solution in a large amount at once. This is probably due to inactivation of HRP by excess hydrogen peroxide. From the CD and absorption spectra, it is suggested that excess hydrogen peroxide causes not only decomposition of the prosthetic heme but also modification of the higher structure of HRP.     

Structural Change and Catalytic Activity of Horseradish Peroxidase in Oxidative Polymerization of Phenol

The effects of solvent and reaction conditions on the catalytic activity of horseradish peroxidase (HRP) were investigated for oxidative polymerization of phenol in water/organic mixtures using hydrogen peroxide as an oxidant. Also, the structural changes of HRP were investigated by CD and absorption spectroscopy in these solvents. The results suggest that the yield of phenol polymer (the conversion of phenol to polymer) is strongly affected by the reaction conditions due to the structural changes of HRP, that is, the changes in higher structure of the apo-protein and dissociation or decomposition of the prosthetic heme. Optimum solvent compositions for phenol polymerization depend on the nature of the organic solvents owing to different effects of the solvents on HRP structure. In addition to initial rapid changes, slower changes of HRP structure occur in water/organic solvents especially at high concentrations of organic solvents. In parallel with these structural changes, catalytic activity of HRP decreases with time in these solvents. At higher reaction temperatures, the yield of the polymer decreases, which is also ascribed to modification of HRP structure. It is known that hydrogen peroxide is an inhibitor of HRP, and the yield of phenol polymer is strongly dependent on the manner of addition of hydrogen peroxide to the reaction solutions. The polymer yield decreases significantly when hydrogen peroxide was added to the reaction solution in a large amount at once. This is probably due to inactivation of HRP by excess hydrogen peroxide. From the CD and absorption spectra, it is suggested that excess hydrogen peroxide causes not only decomposition of the prosthetic heme but also modification of the higher structure of HRP.     

Solvent effect on enzyme-catalyzed synthesis of β-d-glucosides using the reverse hydrolysis method: Application to the preparative-scale synthesis of 2-hydroxybenzyl and octyl β-d-glucopyranosides

Almond β-d-glucosidase was used to catalyze alkyl-β-d-glucoside synthesis by reacting glucose and the alcohol in organic media. The influence of five different solvents and the thermodynamic water activity on the reaction have been studied. The best yields were obtained in 80 or 90% (v/v) tert-butanol, acetone, or acetonitrile where the enzyme is very stable. In this enzymatic synthesis under thermodynamic control, the yield increases as the water activity of the reaction medium decreases. Enzymatic preparative-scale syntheses were performed in a tert-butanol-water mixture which was found to be the most appropriate medium. 2-Hydroxybenzyl β-d-glucopyranoside was obtained in 17% yield using a 90:10 (v/v) tert-butanol-water mixture. Octyl-β-glucopyranoside was obtained in 8% yield using a 60:30:10 (v/v) tert-butanol-octanol-water mixture.     

水-有机溶剂两相体系中甲基单胞菌Z201催化丙烯环氧化的初步研究

Lanne于1987年提出了生物催化剂工程（Biocatalyst engimeering）和介质工程（Medium enineering）的概念^[1].有机相生物催化中溶剂的选择也是介质工程的内容之一。纯酶在有机相中的催化作用已有大量报道^[2],但对完整细胞研究甚少。本文以甲基单胞菌（Methylomonos）Z201完整细胞为生物催化剂,丙烯环氧化为指标反应,研究有机溶剂对活性的影响并对催化活性-溶剂疏水性进行了相关性分析。研究了水-十六烷两相体系中十六烷含量和搅拦速度对丙烯环氧化速度的影响和细胞的操作稳定性。