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The influence of the addition of an extra component in a gaseous reaction medium, on the kinetics of alcoholysis of methyl propionate and n-propanol catalyzed by immobilized lipase B from Candida antarctica was studied in a continuous solid/gas reactor. In this reactor, the solid phase is composed of a packed enzymatic sample, which is percolated by gaseous nitrogen, simultaneously carrying gaseous substrates and additional components to the enzyme while removing reaction products. The system permits to set thermodynamic activity of all gaseous components (substrates or not) independently at the desired values. This allows in particular to study the influence of an extra added component at a constant thermodynamic activity value, contrary to classical solid/liquid system, which involves large variations of thermodynamic activity of added solvent, when performing full kinetic studies. Alcohol inhibition constant (K(I)) and methyl propionate and propanol dissociation constants (K(MP) and K(P)) have been determined in the solid/gas reactor in the presence of 2-methyl-2-butanol, and compared with values previously obtained in the absence of added component and in the presence of water. Complementary experiments were carried out in the presence of an apolar compound (hexane) and led to the conclusion that the effect of added organic component on lipase-catalyzed alcoholysis is related to their competitive inhibitory character towards first substrate methyl propionate. The comparison of data obtained in liquid or with gaseous 2-methyl-2-butanol shows that lower K(MP) and K(I) are found in gaseous medium, which would correspond on the one hand to a lower acylation rate k(2), and on the other hand to a higher binding rate k(1) between substrate and free enzyme in gaseous medium.

The influence of water on the kinetics of alcoholysis of methyl propionate and n-propanol catalyzed by immobilized lipase B from Candida antarctica was studied in a continuous solid/gas reactor. In this reactor, the solid phase is composed of a packed enzymatic sample which is percolated by gaseous nitrogen, simultaneously carrying gaseous substrates to the enzyme while removing reaction products. In this system, interactions between the enzyme and nonreacting molecules are avoided, since no solvent is present, and it is thus more easy to assess the role of water. To this end, alcohol inhibition constant, substrates dissociation constants as well as acylation rate constant and ratio of acylation to deacylation rate constants have been determined as a function of water activity (a(w)). Data obtained highlight that n-propanol inhibition constant and dissociation constant of methyl propionate are a lot affected by a(w) variations whereas water has no significant effect on the catalytic acylation step nor on the ratio of acylation to deacylation rate constants. These results suggest the water-independent character of the transition step.

The effect of water on the alcoholysis of methyl propionate and n-propanol catalyzed by immobilized Candida antarctica lipase B (CALB) has been compared in a continuous solid-gas reactor and in an organic liquid medium. The enthalpic and entropic contributions of water to the Gibbs free energy of activation in the gas phase were different from the ones in the organic phase, the inverse trends being observed for the variation of both DeltaH* and DeltaS* with water activity. Different phenomena were identified for their influence on the thermodynamic parameters. When increasing a(w), the enhanced flexibility of the enzyme was predominant in the gas phase whereas substrate-solvent interactions due to an increased polarity of the solvent affected mainly the thermodynamic parameters in the organic phase. The observed variations of DeltaG* with water activity were in accordance with kinetics results previously obtained in both reaction media.

The kinetics of alcoholysis of methyl propionate and n-propanol catalyzed by Candida antarctica lipase B supported onto silanized Chromosorb P was studied in a continuous solid/gas reactor. In this system the solid phase is composed of a packed enzymatic sample and is percolated by nitrogen as carrier gas, which simultaneously carries substrates to the enzyme while removing reaction products. In this reactor the thermodynamic activity of substrates and effectors can be perfectly adjusted allowing kinetic studies to be performed under different operating conditions. The kinetics obtained for alcoholysis were suggested to fit a Ping Pong Bi Bi mechanism with dead-end inhibition by the alcohol. The values of all apparent kinetic parameters were calculated and the apparent dissociation constant of enzyme for gaseous ester was found very low compared with the one obtained for liquid ester in organic medium, certainly due to the more efficient diffusion in the gaseous phase. The effect of water thermodynamic activity was also investigated. Water was found to act as a competitive inhibitor, with a higher inhibition constant than n-propanol. Thus alcoholysis of gaseous methyl propionate and n-propanol catalyzed by C. antarctica lipase B was found to obey the same kinetic mechanism as in other non-conventional media such as organic liquid media and supercritical carbon dioxide, but with much higher affinity for the substrates.

Analysis of the kinetic behaviour of a two-enzyme-system carrying out two consecutive reactions was investigated in macroheterogeneous biphasic media (octane/buffer pH 9.6, v/v = 1:1). The lipase-catalysed hydrolysis of trilinolein and the subsequent lipoxygenation of the liberated linoleic acid, were coupled in a modified Lewis cell with a well-defined liquid/liquid interfacial area. Trilinolein was dissolved in the organic phase and hydrolysed in the presence of Mucor javanicus lipase at the organic/aqueous interface. Linoleic acid, liberated after hydrolysis was transferred to the aqueous phase and reacted with lipoxygenase. This reaction consumed linoleic acid and produced hydroperoxides, which favoured the transfer of residual linoleic acid, since they possess surface active properties. Catalysis and transfer influenced each other reciprocally. At low substrate concentrations, cooperativity phenomena were observed in the experimental and also the modelled two-enzyme systems. When the initial substrate concentration was high, the kinetic behaviour of the two-enzyme system in a compartmentalised medium, seemed to be independent of the substrate concentration, unlike that observed in homogeneous monophasic enzymology. The numerical integration program used to model the two-enzyme system was based on results obtained in separate studies of the following three phenomena: (1) trilinolein hydrolysis in biphasic medium. (2) linoleic acid transfer across a liquid/liquid interface and (3) lipoxygenation in an aqueous media. Results obtained by modelling were similar to the results observed experimentally.

A comparative study of temperature and pressure effects were carried out by using two homologous enzymes exhibiting different thermostability and oligomery: almond beta-glucosidase and Sulfolobus solfataricus beta-glucosidase. Both the activity and stability were studied using an in-house built bioreactor allowing injection, stirring, sampling and on-line spectrophometric monitoring with retention of pressure up to 2.5 kbar and temperature control possible up to 150 degrees C. Almond beta-glucosidase, the most pressure sensitive enzyme of the two was continuously affected by pressure up to 1.5 kbar. Activation volume changes revealed that the inactivation of almond beta-glucosidase was due to both catalytic step inactivation and enzyme-substrate binding inactivation. Structural modifications generated by pressure, related to a loss of activity did not affect the global conformation of almond beta-glucosidase, after depressurization. In contrast, Sulfolobus solfataricus beta-glucosidase was a highly barostable enzyme. It maintained a half-life of 91 h at 60 degrees C and 2.5 kbar. Moreover, this enzyme appeared to be activated by pressure between atmospheric pressure and 2.5 kbar with a maximal activity at 1.25 kbar. However, this enzyme still displayed the best catalytic efficiency at atmospheric pressure because of a Km value drastically increased by pressure. Activation volume changes indicated that the hydrolysis reaction catalysed by Sulfolobus solfataricus beta-glucosidase, was alternatively favoured and disfavoured by pressure due to the catalytic step activation or inactivation associated with the enzyme-substrate binding step being continuously inactivated by pressure.

A comparison between the pressure effects on the catalysis of Thermoanaerobium brockii alcohol dehydrogenase (TBADH: a thermostable tetrameric enzyme) and yeast alcohol dehydrogenase (YADH: a mesostable tetrameric enzyme) revealed a different behaviour. YADH activity is continuously inhibited by an increase of pressure, whereas YADH affinity seems less sensitive to pressure. TBADH activity is enhanced by pressure up to 100 MPa. TBADH affinity for alcoholic substrates increases if pressure increases, was TBADH affinity for NADP decreases when pressure increases. Hypothesis has been raised concerning the dissociation of oligomeric enzymes under high hydrostatic pressure ( < 200 MPa) [1]. But in the case of these two enzymes, unless the oligomers reassociate very quickly (< 1 min), the activity inhibition of YADH at all pressures and TBADH for pressures above 100 MPa is not correlated to subunit dissociation. Hence we suggest that enzymes under pressure encounter a molecular rearrangement which can either have a positive or a negative effect on activity. Finally, we have observed that the catalytic behaviour of alcohol dehydrogenases under pressure is connected to their thermostability.

A novel method for modulation of lipase hydrolysis and synthesis lipase was investigated by using carbohydrates in the microenvironment of the Candida rugosa enzyme. The influence of the addition of different sugars to the previously dialysed enzyme was tested on the two reactions. Rates of hydrolysis were lowered by using dialysed enzyme but were increased after sugar addition, regardless of the identity of the added sugar. In contrast, synthesis reaction rates depended on the nature of the carbohydrate. Rates were increased by adding lactose, which is not a water activity depressor, but were lowered by adding fructose, glucose, sucrose or sorbitol, which are all water activity depressors.

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.