The use of gas-phase substrates to study enzyme catalysis at low hydration

Although there are varying estimates as to the degree of enzyme hydration required for activity, a threshold value of ca. 0.2 g of water per gram of protein has been widely accepted. The evidence upon which this is based is reviewed here. In particular, results from the use of gas-phase substrates are discussed. Results using solid-phase enzyme-substrate mixtures are not altogether in accord with those obtained using gas-phase substrates. The use of gaseous substrates and products provides an experimental system in which the hydration of the enzyme can be easily controlled, but which is not limited by diffusion. All the results show that increasing hydration enhances activity. The results using gas-phase substrates do not support the existence of a critical hydration value below which enzymatic activity is absent, and suggest that enzyme activity is possible at much lower hydrations than previously thought; they do not support the notion that significant hydration of the surface polar groups is required for activity. However, the marked improvement of activity as hydration is increased suggests that water does play a role, perhaps in optimizing the structure or facilitating the flexibility required for maximal activity.     

Esterase catalysis of substrate vapour: enzyme activity occurs at very low hydration

It has been generally accepted that enzyme activity requires a minimal hydration of about 0.2 g H2O g(-1) protein. This fits well with evidence that hydration above this level is associated with the onset of intramolecular motions. The influence of enzyme hydration on the hydrolysis of substrate by Candida rugosa Lipase B and pig liver esterase was investigated. Each enzyme was studied as a powder at various hydration levels, using vapour phase ethyl butyrate as substrate. This procedure allows the separation of those effects that are due to hydration from those arising from diffusional constraints. We found hydrolytic activity in both enzymes at all hydration levels above zero (between 0.054-0.47 and 0.029-0.60 g H2O g(-1) protein, respectively) that were investigated. The lowest hydration level investigated, <0.03 g H2O g(-1) enzyme, corresponded to a water/enzyme mole ratio of 100 and a coverage of about 10% of the enzyme surface by water molecules. The hydrolytic activity of both enzymes was dependent on protein hydration. However, since the hydrolysis of ethyl butyrate requires water as a second substrate, the absence of activity at zero hydration does not rule out the possibility of enzyme activity in the absence of water. These results suggest that the properties conferred on proteins by water, at least above 10% surface coverage (in this case corresponding to a hydration level of 0.03 g H2O g(-1) protein), are not a requirement for enzyme catalysis.     

Solvent effects on the catalytic activity of subtilisin suspended in organic solvents

We studied a model transesterification reaction catalyzed by subtilisin Carlsberg suspended in toluene, n-hexane, diisopropyl ether, and mixtures of these solvents. To account for solvent effects due to differences in water partitioning between the enzyme and the bulk solvents, we measured water sorption isotherms for the enzyme in each solvent. We measured catalytic activity as a function of enzyme hydration and obtained bell-shaped curves with maxima at the same enzyme hydration in all the solvents. However, the activity maxima were different in all the media, being the lowest in toluene. Differences in the partitioning of substrates and product between the bulk solvent phase and the enzyme active site were accounted for but could not explain the lower catalytic activity observed in toluene. The fact that toluene is very similar to one of the substrates suggested the possibility of competitive inhibition by this solvent. We derived a model allowing for differences in solvation of the substrates, by using thermodynamic activities instead of concentrations, as well as for competitive inhibition by toluene. The model fit the experimental data well, confirming that toluene had a direct adverse effect on the catalytic activity of the enzyme. (c) 1996 John Wiley & Sons, Inc.     

Effect of gallic acid polydisulfide on activity and stability of catalase in various media

The effect of the active bioantioxidant polydisulfide of gallic acid (PDSG) on the catalytic activity and operational and thermal stability of catalase was studied in three media: distilled water (pH approximately 5.6), phosphate buffer, pH 7.4, and reversed micelles of Aerosol OT (AOT) in heptane of varied hydration degree w0. PDSG inhibited the catalase-induced decomposition of H2O2 by the mixed or noncompetitive mechanism: in various media the inactivation constant Ki varied in the range of (0.63-2.32).10-5 M. PDSG nearly twofold decreased the rate constant of interaction of the complex I of catalase with H2O2 (k2, M-1.sec-1) in water and reversed micelles of AOT and 3-5 times increased the effective rate constant of catalase thermal inactivation, k*in, sec-1, depending on the reaction medium. PDSG significantly decreased the rate constant of catalase inactivation during the enzymatic reaction, kin, sec-1, and thus increased the enzyme operational stability in water and reversed AOT micelles in heptane. The interaction of PDSG with catalase in water and in phosphate buffer was accompanied by significant changes in CD spectra in the far UV-region that indicated disturbances in the secondary structure of catalase subunits induced by the bioantioxidant; the latter was suggested to initiate the reaction of thiol--disulfide exchange with the enzyme. The problem of the compatibility of catalase with disulfide bioantioxidants is discussed.     

What can we learn by studying enzymes in non-aqueous media?

What is the role of water in enzyme structure and function? One approach to answers should come from studies in which the amount of water present is a variable. In the absence of bulk liquid water, effective monitoring of enzyme action requires an alternative fluid medium through which substrates and products may be transported. The past 20 years have seen quite extensive study of enzyme behaviour when reactants are transferred via a bulk phase that is an organic liquid, a supercritical fluid or a gas. Some lipases, at least, remain highly active with only a few, if any, residual water molecules. Many enzymes seem to require larger amounts of water, but still not a liquid water phase. There are hysteresis effects on both the amount of bound water and the observed catalytic activity. Increasing hydration promotes mobility of the enzyme molecule, as revealed by various techniques, and there are correlations with catalytic activity. There are other plausible roles for hydration, such as opening up proton conduction pathways.     

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.     

Working at controlled water activity in a continuous process: the gas/solid system as a solution

Fusarium solani cutinase and Candida cylindracea lipase were used to catalyze a transesterification reaction in a continuous gas/solid bioreactor. In this system, a solid phase composed of a packed enzymatic preparation was continuously percolated with carrier gas which fed substrate and removed reaction products simultaneously. Different conditions of immobilization were used and compared to the results obtained with a nonsupported enzyme. The enzymatic activity was found to be highly dependent of a key parameter: water activity (a(w)). Biocatalyst stability was greatly influenced by water activity and the choice of immobilization technique for the enzymatic material. For free and adsorbed enzymes, water requirements exhibited optima which corresponded to the complete hydration coverage of the protein. These optima presented a good correlation with the isotherm sorption curves obtained for the different preparations. In this work are reported the results concerning the possibility of using a continuous system able to operate at controlled water activity in a heterogeneous medium. Lipolytic enzyme in such a system appears to be a new process for the biotransformation of volatile esters. (c) 1995 John Wiley & Sons, Inc.     

Regulation of the supramolecular structure and the catalytic activity of gamma-glutamyltransferase in the reversed micelle system

Regulation mechanisms of the supramolecular structure and the catalytic activity of a heterodimeric enzyme, gamma-glutamyltransferase, in the system of Aerosol OT (AOT) reversed micelles in octane have been studied. gamma-(3-carboxy-4-nitro)-glutamic acid anilide (L- and D-isomers) and glycylglycine were used as substrates to explore the enzyme-catalyzed hydrolase, autotransferase, and transferase reactions. For all types of reactions, the catalytic activity of gamma-glutamyltransferase as a function of the hydration degree has a shape of curves with three optima. The optima of the catalytic activity were detected at hydration degrees [( H2O]/[AOT] = 11, 17, and 26) when radii of the micelle's inner cavity are commensurate with the light and heavy subunits (Mr 21,000 and 54,000, respectively) of gamma-glutamyltransferase as well as with the dimer (Mr 75,000). As ultracentrifugation the change in hydration degree caused a reversible dissociation of the enzyme to the light and heavy subunits. Both subunits catalyze the hydrolase and transferase reactions, whereas the autotransferase activity was detected only for the heavy subunit. Dependencies of catalytic activities of the subunits on the hydration degree have one optimum each (at [H2O]/[AOT] = 11 and 17 for the light and heavy subunits, respectively). When mixing micellar solutions containing both subunits, a third optimum was detected corresponding to the dimer [( H2O]/[AOT] = 26).     

Effect of yeast cell disruption on ADH activity for redox reactions with in situ cofactor regeneration in a continuous solid/gas bioreactor

It has recently been demonstrated that dried cells of Saccharomyces cerevisiae were able to produce alcohols and aldehydes in a solid/gas reactor with in situ cofactor regeneration. Since diffusion of gaseous substrates may be limited by the membrane and cell wall, cell disruption by sonication was used to improve oxidoreduction with ethanol and butyraldehyde as substrates. Results showed that partial cell disruption enhances the maximum conversion yield with the best results obtained after 2 min of sonication. Beyond this time, the ADH activity decreased. Better stability was observed in the pellet obtained after centrifugation indicating the importance of cell environment for enzyme stability. Tests on purified mitochondria showed that the ADH activity in cells was mainly cytoplasmic. The addition of oxidized cofactor did not change either the activity or the stability of the catalyst in a gaseous medium. The effect of water activity was studied on material obtained after 2 min of disruption and a reduction of critical water activity needed for revealing enzymatic activity was observed. With increasing a_w, the enzyme was active at a_w=0.3 while a water activity of 0.4 was required before disruption. Nevertheless, the best compromise between activity and stability was obtained in both cases for a water activity of 0.57.     

Activity and stability of cross-linked tyrosinase aggregates in aqueous and nonaqueous media

Cross-linked tyrosinase aggregates were prepared by precipitating the enzyme with ammonium sulfate and subsequent cross-linking with glutaraldehyde. Both activity and stability of these cross-linked enzyme aggregates (CLEAs) in aqueous solution, organic solvents, and ionic liquids have been investigated. Immobilization effectively improved the stability of the enzyme in aqueous solution against various deactivating conditions such as pH, temperature, denaturants, inhibitors, and organic solvents. The stability of the CLEAs in various organic solvents such as tert-butanol (t(1/2)=326.7h at 40°C) was significantly enhanced relative to that in aqueous solution (t(1/2)=5.5h). The effect of thermodynamic water activity (a(w)) on the CLEA activity in organic media was examined, demonstrating that the enzyme incorporated into CLEAs required an extensive hydration (with an a(w) approaching 1.0) for optimizing its activity. The impact of ionic liquids on the CLEA activity in aqueous solution was also assessed.     

Effect of yeast cell disruption on ADH activity for redox reactions with in situ cofactor regeneration in a continuous solid/gas bioreactor

It has recently been demonstrated that dried cells of Saccharomyces cerevisiae were able to produce alcohols and aldehydes in a solid/gas reactor with in situ cofactor regeneration. Since diffusion of gaseous substrates may be limited by the membrane and cell wall, cell disruption by sonication was used to improve oxidoreduction with ethanol and butyraldehyde as substrates. Results showed that partial cell disruption enhances the maximum conversion yield with the best results obtained after 2 min of sonication. Beyond this time, the ADH activity decreased. Better stability was observed in the pellet obtained after centrifugation indicating the importance of cell environment for enzyme stability. Tests on purified mitochondria showed that the ADH activity in cells was mainly cytoplasmic. The addition of oxidized cofactor did not change either the activity or the stability of the catalyst in a gaseous medium. The effect of water activity was studied on material obtained after 2 min of disruption and a reduction of critical water activity needed for revealing enzymatic activity was observed. With increasing a_w, the enzyme was active at a_w=0.3 while a water activity of 0.4 was required before disruption. Nevertheless, the best compromise between activity and stability was obtained in both cases for a water activity of 0.57.     

Gas phase biotransformation reaction catalyzed by baker's yeast

The gas phase continuous production of acetaldehyde from ethanol and hexanol from hexanal using dried baker's yeast was studied as an alternative approach to conventional processes. The effects of water activity, activity of substrates, and amount of yeast on the performance of the continuous bioreactor were investigated. The extent of yeast hydration and ethanol activity are the most important factors affecting yeast activity and stability.     

Stability and activity of alcohol dehydrogenases in W/O-microemulsions: enantioselective reduction including cofactor regeneration

Microemulsions provide an interesting alternative to classical methods for the conversion of less water-soluble substrates by alcohol dehydrogenase, but until now stability and activity were too low for economically useful processes. The activity and stability of the enzymes are dependent on the microemulsion composition, mostly the water and the surfactant concentration. Therefore, it is necessary to know the exact phase behavior of a given microemulsion reaction system and the corresponding enzyme behavior therein. Because of their economic and ecologic suitability polyethoxylated fatty alcohols were investigated concerning their phase behavior and their compatibility with enzymes in ternary mixtures. The phase behavior of Marlipal O13-60 (C13EO6 in industrial quality)/cyclohexane/water and its effect on the activity and stability of alcohol dehydrogenase from Yeast (YADH) and horse liver (HLADH) and the carbonyl reductase from Candida parapsilosis (CPCR) is presented in this study. Beside the macroscopic phase behavior of the reaction system, the viscosity of the system indicates structural changes of aggregates in the microemulsion. The changes of the enzyme activities with the composition are discussed on the basis of transitions from reverse micelles to swollen reverse micelles and finally, the transition to the phase separation. The formate dehydrogenase from Candida boidinii was used for the NADH-regeneration during reduction reactions. While the formate dehydrogenase did not show any kinetic effect on the microemulsion composition, the other enzymes show significant changes of activity and stability varying the water or surfactant concentration of the microemulsion. Under certain conditions, stability could be maintained with HLADH for several weeks. Successful experiments with semi-batch processes including cofactor regeneration and product separation were performed.     

Kinetic studies of fusarium solani pisi cutinase used in a gas/solid system: transesterification and hydrolysis reactions

Fusarium solani cutinase supported onto Chromosorb P was used to catalyze transesterification (alcoholysis) and hydrolysis on short volatile alcohols and esters in a continuous gas/solid bioreactor. In this system, a solid phase composed of a packed enzymatic preparation was continuously percolated with carrier gas which fed substrates and removed reaction products simultaneously. A kinetic study was performed under differential operating conditions in order to get initial reaction rates. The effect of the hydration state of the biocatalyst on the kinetics was studied for 3 conditions of hydration (a(w) = 0.2, a(w) = 0.4 and a(w) = 0.6), the alcoholysis of propionic acid methyl ester with n-propanol, and for 5 hydration levels (from a(w) = 0.2 to a(w) = 0.6) for the hydrolysis of propionic acid methyl, ethyl or propyl esters. F. solani cutinase was found to have an unusual kinetic behavior. A sigmoid relationship between the rate of transesterification and the activity of methyl propionate was observed, suggesting some form of cooperative activation of the enzyme by one of its substrate. For the hydrolysis of short volatile propionic acid alkyl esters, threshold effects on the reaction rate, highly depending on the water activity and the substrate polarity, are reported. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 1-8, 1997.     

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.     

Enzymatic oxidation of ethanol in the gaseous phase

The enzymatic conversion of gaseous substrates represents a novel concept in bioprocessing. A critical parameter in such systems is the water activity, A(w) The present article reports the effect of A(w) on the catalytic performance of alcohol oxidase acting on ethanol vapors. Enzyme activity in the gas-phase reaction increases several orders of magnitude, whereas the thermostability decreases drastically when A(w) is increased from 0.11 to 0.97. The enzyme is active on gaseous substrates even at hydration levels below the monolayer coverage. Enhanced thermostability at lower hydrations results in an increase in the optimum temperature of the gas-phase reaction catalyzed by alcohol oxidase. The apparent activation energy decreases as A(w) increases, approaching the value obtained for the enzyme in aqueous solution. The formation of a pread-sorbed ethanol phase on the surface of the support is not a prerequisite for the reaction, suggesting that the reaction occurs by direct interaction of the gaseous substrate with the enzyme. The gas-phase reaction follows Michaelis-Menten kinetics, with a K(m) value almost 100 times lower than that in aqueous solution. Based on vapor-liquid equilibrium data and observed K(m) values, it is postulated that during the gas-phase reaction the ethanol on the enzyme establishes an equilibrium with the ethanol vapor similar to that between ethanol in water and ethanol in the gas phase.     

An automated method for measuring the operational stability of biocatalysts with carbonic anhydrase activity

The operational stability of an enzyme can be quantified by its half-life, or the length of time after which 50% of its original activity has degraded. Ideally, continuous methods for measuring half-lives are preferred but they can be expensive and relatively low throughput. Batch methods, while simple, cannot be used for all enzymes. For example, batch reactions can be difficult when there is a gas phase reactant or when there is significant product or substrate inhibition. Here we describe a repeated-batch method for measuring the half-life of carbonic anhydrase (CA)-based biocatalysts by automated periodic switching between a forward and reverse reaction. This method is inexpensive and can be multiplexed for high-throughput analysis of enzyme variants. Several purified CA enzymes as well as whole-cell biocatalysts with engineered CA activity were evaluated with this method. The results indicate a significant increase in operational stability is achieved upon immobilization of CA in the cellular periplasm of Escherichia coli.     

Factors influencing the operational stability of NADPH-dependent alcohol dehydrogenase and an NADH-dependent variant thereof in gas/solid reactors

The continuous enzymatic gas/solid bio-reactor serves both for the production of volatile fine chemicals and flavors on an industrial scale and for thermodynamically controlled investigation of substrate and water effects on enzyme preparations for research purposes. Here, we comparatively investigated the molecular effects on the operational stability of NADPH-dependent Lactobacillus brevis alcohol dehydrogenase and an NADH-dependent variant thereof, LbADH G37D, in the gas/solid bioreactor. The reference reaction is the reduction of acetophenone to (R)-1-phenylethanol with concomitant oxidation of 2-propanol to acetone for the purpose of regeneration of the redox cofactor.It could be clearly shown that not the thermostability of the cofactor, but the thermostability of the proteins in the solid dry state govern the order of magnitude of the operational stability of both purified enzymes in the gas/solid reactor at low thermodynamic activity of water and substrate. However, at higher thermodynamic activity the operational stability in the gas/solid reactor is overlaid by stabilizing and destabilizing effects of the substrates that require further investigation. We demonstrated first evidence that the substrate affinity of the two variants in the gas/solid reactor is similar to the affinity in aqueous medium. We could also show that partial unfolding of the proteins with subsequent aggregation are the factors governing protein thermo-in-stability both in the dissolved and in the dry state. Thus, stability investigations of enzymes in the dry state are suggested to predict their basal level of operational stability in gas/solid reactions.     

Anomalous behaviour of cathepsin B: dependence of activity and stability on salt concentration

Effect of salt concentration on the activity and stability of cathepsin B from buffalo spleen has been investigated. Catheptic activity was maximal at a buffer concentration of 5.5 x 10(-3) M. The enzyme was, however, highly unstable at a salt concentration lower than 1.5 x 10(-2) M. The use of 0.02 M sodium phosphate buffer has been suggested for the assay of cathepsin B activity. For storage of the enzyme, however, a 0.1 M sodium phosphate or other buffer of equivalent ionic strength has been recommended.     

The control of lipase-catalysed transesterification and esterification reaction rates. Effects of substrate polarity, water activity and water molecules on enzyme activity

The reaction rate of two lipase-catalysed reactions, esterification and transesterification, were studied in a liquid/solid two-phase system in order to investigate the effect of water partition between the enzyme preparation and the liquid phase composed of only the reactants, i.e. without the conventional solvents. Lipase from Candida cylindracea was used for these studies. The enzyme was inactive in dehydrated systems. In the case of monoester synthesis, the reaction rate increased with increasing water activity. The reaction rates of the non-specific C. cylindracea lipase-catalysed reactions were very sensitive to the nature of the substrates in this unusual system. For instance, the transesterification reaction rate of ethyl propionate was 48 times higher with nonanol than heptanol in the case of dehydrated substrates, but only 2.2 times higher in the case of water-saturated substrates. The results presented here demonstrate the absolute necessity to consider the polarity of every substrate, because of its ability to modify the water partition between the solid phase (enzyme preparation) and the liquid phase (substrate and product), which results in drastic changes in enzyme activity. Contrary to esterification, which is known to be activated by the water produced, the rate of transesterification remained constant at the beginning of the reaction. However, when transesterification and esterification were carried out in the same liquid phase, the transesterification reaction rate was controlled by the water produced by the concomitant esterification. Activation effects of the water molecules produced during the enzymatic reaction were of exactly the same order of magnitude for both reactions.