Lipase kinetics in organic-water solvent with amphipathic substrate for chiral reaction

Lipase from Pseudomonas cepacia was used for asymmetric hydrolysis of the substrate (+/-)1-chloro-2-acetoxy-3-(1-naphthyloxy)-propane, which is a precursor for (S)-(-)-beta-blocker synthesis. Because this substrate is insoluble in water and partially soluble in hydrophobic solvents such as hexane and octane, a mixture of hydrophilic organic solvents and aqueous buffer was used to study the initial reaction rates. Because of the amphipathic nature of the substrate, it can remain in three different forms: (1) monomeric (solution); (2) micellar; and (3) emulsion, depending on the acetone and substrate concentrations in the medium. This behavior is presented in a phase diagram. The enzyme was found to be active with micelle as well as emulsion form of the substrate, whereas it showed negligible activity with the monomeric form. Michaelis-Menten constants were determined experimentally for the emulsion and micellar part of the substrate. The initial rate of hydrolysis (v(0)) goes through a maximum with respect to the acetone content of the mixture. It is due to the combined effect of various factors occurring simultaneously with the increase in acetone content in the solvent. These phenomena are discussed based on the interfacial activation of lipase, deactivation of the enzyme at very high acetone concentration, and increase in critical micelle concentration (CMC) and critical emulsion concentration (CEC) with the increase in acetone content in the solvent. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 399-407, 1997.     

Reaction rate with suspended lipase catalyst shows similar dependence on water activity in different organic solvents.

We have studied the effect of thermodynamic water activity (a W) on the initial rate of esterification catalysed by an immobilised lipase (Lipozyme) suspended in an organic reaction mixture. The catalyst and the organic phase were separately pre-equilibrated to the same aw value. The rate shows similar dependence on aw in reaction mixtures based on five different organic solvents ranging in polarity from pentan-3-one to hexane, and in a liquid reactant mixture. There is a maximum at aw about 0.5, with a decline to 30-70% at aw of either 0.9 or less than 0.01. When the rates are presented in terms of water concentration in the organic phase (or total water content of the system), the maxima for the various solvents come at very different positions, reflecting the widely varying solubilities of water in the organic phase.     

Enzymatic catalysis in cosolvent modified pressurized organic solvents.

An important advantage of carrying out enzymatic catalysis in organic media is the increased solubility of hydrophobic substrates. This study compares a model lipase catalyzed esterification of cholesterol using vinyl acetate (VA) in two such nontraditional media: high-pressure hexane and supercritical (SCF) ethane. The effect of using one of the reactants (VA) as a cosolvent to increase the solubility of the other reactant (cholesterol) in SCF ethane has been investigated. The thermodynamic activity of water (a(w)) in the reaction media was controlled by the direct addition of the salt hydrate pair Na(4)P(2)O(7)/Na(4)P(2)O(7).10H(2)O. The a(w) of the salt hydrate system is shown to be a function of pressure and its variation over the pressure range 104-173 bar has been estimated. The initial reaction rate in pressurized hexane was found to vary linearly with the cholesterol concentration. The reaction rate was also a function of pressure-the effect being more pronounced in ethane than in hexane. This is consistent with the large negative partial molar volumes observed in SCFs, although the sign of the resulting activation volume differs from previous investigations of lipase-catalyzed reactions in SCFs. When corrected for substrate concentration, the initial rate of catalysis in SCF ethane was determined to be greater than in pressurized hexane over the conditions investigated. This study shows that proper solvent choice can be used to regulate reaction rates in pressurized solvents.     

Enantioselective properties of Fusarium solani pisi cutinase on transesterification of acyclic diols: activity and stability evaluation

The regio and enantioselectivity of a recombinant cutinase from Fusarium solani pisi was tested on three racemic and one prochiral phenylalkanediols via irreversible transesterification with vinyl acetate. The optimization of the reaction conditions involved the screening of different organic solvents as well as the variation of the substrate concentrations. Thus, the enzymatic activity was checked by measuring initial reaction rates, overall yields, and enantiomeric excess of the reaction products. Only the smaller molecules were recognized by the enzyme, and a denaturing effect of the acyl donor was observed. Nevertheless, a stabilising effect on the enzyme caused by a pre-incubation with the diol was also noted.     

Synthesis of esters using a nylon-immobilized lipase in batch and continuous reactors.

Direct esterifications using a nylon-immobilized lipase from Candida cylindracea were carried out in batch and continuous-flow reactors. The immobilized enzyme was effective in catalyzing the synthesis of ethylpropionate, isoamylpropionate, and isoamylbutyrate. With ethanol dissolved in hexane as a substrate, the maximum initial esterification rate was 0.02 mole/(h x g of immobilized protein), but the enzyme was stable only when the substrate concentrations were lower than 0.2 M. With isoamyl alcohol in hexane as a substrate, esterification rates as high as 0.085 mole/(h x g of immobilized protein) were observed and the immobilized enzyme was stable over a much broader concentration range. However, in this case, the use of a solvent, such as hexane, was not necessary for esterification, and the enzyme could be employed in equimolar acid/alcohol mixtures. A packed-bed reactor was operated successfully for the continuous synthesis of esters. The reactor was stable for long periods of time, and the steady-state performance could be accurately predicted on the basis of batch reaction experiments.     

Lipase catalyzed esterification of glycidol in nonaqueous solvents: solvent effects on enzymatic activity

We studied the effect of organic solvents on the kinetics of porcine pancreatic lipase (pp) for the resolution of racemic glycidol through esterification with butyric acid. We quantified ppl hydration by measuring water sorption isotherms for the enzyme in the solvents/mixtures tested. The determination of initial rates as a function of enzyme hydration revealed that the enzyme exhibits maximum apparent activity in the solvents/mixtures at the same water content (9% to 11% w/w) within the associated experimental error. The maximum initial rates are different in all the media and correlate well with the logarithm of the molar solubility of water in the media, higher initial rates being observed in the solvents/mixtures with lower water solubilities. The data for the mixtures indicate that ppl apparent activity responds to bulk property of the solvent. Measurements of enzyme particle sizes in five of the solvents, as function of enzyme hydration, revealed that mean particle sizes increased with enzyme hydration in all the solvents, differences between solvents being more pronounced at enzyme hydration levels close to 10%. At this hydration level, solvents having a higher water content lead to lower reaction rates; these are the solvents where the mean enzyme particle sizes are greater. Calculation of the observable modulus indicates there are no internal diffusion limitations. The observed correlation between changes in initial rates and changes in external surface area of the enzyme particles suggests that interfacial activation of ppl is only effective at the external surface of the particles. Data obtained for the mixtures indicate that ppl enantioselectivity depends on specific solvent-enzyme interactions. We make reference to ppl hydration and activity in supercritical carbon dioxide. (c) 1994 John Wiley & Sons, Inc.     

Elucidation of the mechanism of lactic acid growth inhibition and production in batch cultures of Lactobacillus rhamnosus

Batch cultures of Lactobacillus rhamnosus were carried out at different pH values in order to study the limitation of growth and lactic acid production by the hydrogen ion, non-dissociated lactic acid and internal lactate concentrations. The effect of pH between 5 and 6.8 was studied at non-limiting concentrations of glucose; this is more significant for the lactic acid fermentation rate than for the maximum specific growth rate, as shown by the incomplete substrate consumption at lower values of medium pH and by the constant maximum cell mass obtained within the range of pH values studied. To check whether these results were a direct consequence of the different concentrations of the non-dissociated form of lactic acid at different external pH values, specific growth rates and lactic acid productions rates were calculated for each external pH value. The same specific growth rates were observed at the same non-dissociated lactic acid concentrations only at pH values of 5 and 5.5. For higher values of pH (pH > 6) the specific growth rate falls to zero as the non-dissociated lactic acid concentration decreases. This shows that generalisations made from studies performed within very narrow ranges of pH are not valid and that the non-dissociated form of lactic acid is not the only inhibiting species. The internal pH was measured experimentally for each external pH value in order to calculate the internal lactate ion concentration. This form is described to be the inhibitory one. The results obtained confirmed that the specific growth rate reached zero at approximately the same lactate concentration for all the pH values studied. Received: 31 January 1997 / Received revision: 15 May 1997 / Accepted: 19 May 1997     

Optimization of methyl propionate production catalysed by Mucor miehei lipase

Lipase from Mucor miehei was used to catalyse the esterification reaction between propionic acid and methyl alcohol in modified organic media. Small-scale model studies were performed in order to define the optimal conditions. The specific activity of immobilized lipase, adsorbed onto hydrophilic supports, compared to free lipase, showed that enzyme activity was altered by immobilisation. Non-polar solvents were shown to be less harmful for the biocatalyst than solvents with higher polarity. Diethyl ether was used as the cosolvent of hexane to improve the solubility of substrates in the organic phase thus increasing contact with enzyme. An optimal ratio of 90/10 (v/v) was determined for a hexane/diethyl ether mixture. The mass of enzyme preparation must be high enough to display optimal diffusion of the reagents and hydration of the catalytic sites. Increased substrate concentrations were stimulatory up to a point after which inhibition and enzyme destabilisation, in repeated runs, occurred. Water saturation of the organic medium greatly lowered the biosynthetic activity of the enzyme. It was possible to reach a 96% methyl propionate biosynthesis yield after 2.30 h reaction, underlining the free-enzyme operational capacity in a quasi-anhydrous modified organic medium.     

Thermodynamic and kinetic aspects on water vs. organic solvent as reaction media in the enzyme-catalysed reduction of ketones

The stereoselective reduction of ketones catalysed by alcohol dehydrogenase from Thermoanaerobium brockii was studied in different reaction media, hexane at controlled water activities, hexane with 2. 5% water (biphasic) and pure water. The reactions were studied in the temperature range from -1 to 50 degrees C. Increasing the water activity from 0.53 to 0.97 increased the reaction rate 16-fold. The rate was further enhanced in hexane when exceeding the water solubility and in pure water the rates were even higher. This was general for all ketones studied. At controlled water activity the entropy of activation (DeltaSdouble dagger) was the dominating factor. Large negative DeltaSdouble dagger values caused low reaction rates at low aw. When increasing the carbon chain length of the substrate, for reactions in hexane, the decrease of reaction rate was mainly due to a decrease in DeltaSdouble dagger. In the comparison between hexane and pure water, DeltaGdouble dagger values were higher in hexane due to higher DeltaHdouble dagger (activation enthalpy) values. The enantioselectivity (E value) increased from 2.6 at water activity 0. 53 to 4.6 at water activity 0.97. Changing media from hexane (2.5%, v/v water) to pure water was not affecting the enantioselectivity or the specificity for different ketones.     

Markedly improving Novozym 435-mediated regioselective acylation of 1-beta-D-arabinofuranosylcytosine by using co-solvent mixtures as the reaction media

A comparative study was made of Novozym 435-catalyzed regioselective acylation of 1-beta-D-arabinofuranosylcytosine with vinyl propionate for the preparation of the 5'-O-monoester in eleven co-solvent mixtures and three pure polar solvents. Novozym 435 displayed low or no acylation activity toward 1-beta-D-arabinofuranosylcytosine in pure polar solvents, although those solvents can dissolve the nucleosides well. When a hexane-pyridine co-solvent system was adopted, both the initial rate and the substrate conversion were enhanced markedly. The polarity of co-solvent mixtures had significant effect on the reaction. Among the solvent mixtures investigated, the higher the polarity of the solvent mixture, the lower the initial reaction rate and the substrate conversion. It was also found that the acylation was dependent on the hydrophobic solvent content, the water activity and the reaction temperature. The most suitable co-solvent, initial water activity, and reaction temperature were hexane-pyridine (28:72, v/v), 0.07, and 50 degrees C, respectively. Under these conditions, the initial rate, the substrate conversion and the regioselectivity were as high as 91.1 mM h(-1), >97% and >98%, respectively, after a reaction time of 6 h. Among the reaction mediums examined, the lowest apparent activation energy was achieved with hexane-pyridine (28:72, v/v), in which Novozym 435 also exhibited good thermal stability.     

Prediction of average biofilm density and performance of a spherical bioparticle under substrate inhibition

In this article, a model was proposed to predict the average performance and biofilm density of a spherical bioparticle under substrate inhibition in a fluidized bed system. The average biofilm density and substrate consumption rates were predicted for a definite biofilm thickness and limiting substrate concentrations. A diffusion and reaction model was developed over the bioparticle with biofilm-density dependent effective diffusion coefficients for maximum substrate consumption theory. This theory predicts the optimum density of a biofilm to yield a maximum substrate consumption rate within the biofilm, developed for the first time with this study and experimentally verified. A good correlation was observed between the model prediction and experimental results for biofilm density and substrate consumption rates. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 319-329, 1997.     

Biomass retention and performance of anaerobic fixed-film reactors treating acetic acid wastewater

An acetic-acid-based synthetic wastewater of different organic concentrations was successfully treated at 35 degrees C in anaerobic downflow fixed-film reactors operated at high organic loading rates and short hydraulic retention times (HRTs). Substrate removal and methane production rates close to theoretical values of complete volumetric chemical oxygen demand (COD) removal and maximum methane conversion were obtained. A high concentration of biofilm biomass was retained in the reactor. Steady-state biofilm concentration increased with increased organic loading rate and decreased HRTs, reaching a maximum of 8.3 kg VFS/m(3) at a loading rate of 17 kg COD/m(3) day. Biofilm substrate utilization rates of up to 1.6 kg COD/kg VFS day were achieved. Soluble COD utilization rates at various COD concentrations can be described by half-order reaction kinetics.     

Enzymatic production of enantiopure ketoprofen in a solvent-free two-phase system

Enzymatic hydrolysis conducted in a medium composed of solely substrate is considered to resolve racemic ketoprofen esters. In a system composed of two components, the pure liquid substrate (organic phase) and water (aqueous phase), hydrolysis products can be efficiently removed from the reaction mixtures. Accordingly, in this study we designed a solvent-free two-phase system for the enantioselective enzymatic hydrolysis of ketoprofen esters. In order to further optimize this system, the influences of various factors, such as the pH of the aqueous phase, temperature, enzyme content, and the alcohol chain length of esters, were examined on conversion and enantiomeric excess. 1N NaHCO₃ was identified as the most efficient aqueous phase for the extraction of ketoprofen. Changes in the amount of enzyme did not significantly affect the maximum conversion or the enantiomeric excess. On the other hand, ketoprofen esters with shorter alcohol chains displayed higher initial reaction rates and conversions in solventless media. In the case of ketoprofen propyl ester, for example, the productivity of the solvent-free two-phase system was about 10–100 times higher than that obtained to date for ketoprofen esterification with alcohols in organic solvents. The enantioselectivities obtained in solvent-free media were similar to those obtained for the enantioselective esterification of ketoprofen in organic solvents.     

Highly efficient enzymatic synthesis of an ascorbyl unstaturated fatty acid ester with ecofriendly biomass‐derived 2‐methyltetrahydrofuran as cosolvent

Enzymatic synthesis of ascorbyl undecylenate, an unsaturated fatty acid ester of ascorbic acid, was reported with biomass‐derived 2‐methyltetrahydrofuran (MeTHF) as the cosolvent. Of the immobilized lipases tested, Candida antarctica lipase B (CAL‐B) showed the highest activity for enzymatic synthesis of ascorbyl undecylenate. Effect of reaction media on the enzymatic reaction was studied. The cosolvent mixture, t‐butanol‐MeTHF (1:4, v/v) proved to be the optimal medium, in which not only ascorbic acid had moderate solubility, but also CAL‐B showed a high activity, thus addressing the major problem of the solvent conflict for dissolving substrate and keeping satisfactory enzyme activity. In addition, the enzyme was much more stable in MeTHF and t‐butanol‐MeTHF (1:4) than in previously widely used organic solvents, t‐butanol, 2‐methyl‐2‐butanol, and acetone. The much higher initial reaction rate in this cosolvent mixture may be rationalized by the much lower apparent activation energy of this enzymatic reaction (26.6 vs. 38.1–39.1 kJ/mol) and higher enzyme catalytic efficiency (V_max/K_m, 8.4 vs. 1.3–1.4 h^?1). Ascorbyl undecylenate was obtained with the yields of 84–89% and 6‐regioselectivity of >99% in t‐butanol‐MeTHF (1:4) at supersaturated substrate concentrations (60 and 100 mM) after 5–8 h. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1005–1011, 2014     

New patterns of mixed-substrate utilization during batch growth of Escherichia coli K12

Microbial growth on mixtures of substrates is of considerable engineering and biological interest. Most of the work until now has dealt with microbial growth on binary mixtures of sugars or polyols. In these cases, it is often found that no matter how the inoculum is precultured, only one of the two substrates is consumed in the first growth phase, leading to the diauxic growth pattern. The goal of the experiments reported here is to investigate growth on mixtures containing at least one organic acid. These experiments show that the substrate utilization patterns in such mixtures are qualitatively different from the diauxic growth pattern. For instance, during growth of Escherichia coli K12 on certain binary mixtures of organic acids, the two substrates are utilized simultaneously, and the mixed-substrate maximum specific growth rate exceeds the single-substrate maximum specific growth rate on either one of the two constituent substrates. Furthermore, the very same mixed-substrate maximum specific growth and substrate uptake rates are observed no matter how the inoculum is precultured. On the other hand, in a mixture of glucose and pyruvate, the maximum specific growth rate seems to depend on the preculturing conditions, thus suggesting the existence of multiple physiological quasi-steady states. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 747-757, 1997.     

Fatty acid esterification using nylon-immobilized lipase

The esterification of a long-chain fatty acid was conducted using a nylon-immobilized lipase from Candida cylindracea in a nearly anhydrous, nonpolar organic medium, hexane. Butyl laurate was produced from lauric acid and n-butanol at a maximum initial reaction rate of 37 mmol/h. g immobilized enzyme when the substrates were present in equimolar amounts at an initial concentration of 0.5 mol/L. Lower rates were obtained using nonstoichiometric amounts of the substrates. The rate of reaction increased with temperature, reaching a maximum between 35 and 45 degrees C and decreasing sharply at higher temperatures. (c) 1995 John Wiley & Sons, Inc.     

Pseudomonas cepacia lipase--mediated transesterification reactions of hydrocinnamates

Use of lipase from Pseudomonas cepacia in transesterifcation reactions of ethyl hydrocinnamate with different alcohols has been examined. Among the alcohols tested, viz., n-butanol, iso-amyl alcohol, benzyl alcohol, n-octanol and 1-phenylethanol, only n-butanol yielded the transesterified product. Among the solvents tested, viz., n-heptane, n-hexane, cyclohexane, toluene, diisopropylether and n-butanol, the initial rate of transesterification proceeded in the order cyclohexane > n-heptane > n-hexane > diisopropylether > n-butanol > toluene. Using hexane as the solvent and a substrate to enzyme ratio of 1:5, the substrate to alcohol ratio was varied to maximize the yield. n-Butyl hydrocinnamate was obtained in 92% yield in 48 hr by employing a 1:1 (wt/wt) ratio of ethyl hydrocinnamate to lipase and a 1:5 (vol/vol) ratio of ethyl hydrocinnamate to n-butanol in hexane.     

Kinetics of the extracellular cellulases of Clostridium thermocellum acting on pretreated mixed hardwood and Avicel

Initial hydrolysis rates were examined for mixed hardwood flour pretreated with 1% sulfuric acid for 9 s at 220 °C (PTW220) and Avicel. Linear rates were observed for fractional conversion relative to the theoretical up to 0.2 for PTW220 and 0.4 for Avicel. Initial rates were essentially unaffected by the presence of growth medium components over a range of pH values. Avicel-hydrolyzing activity was inhibited linearly by ethanol, with a 50% rate reduction at 8 wt.% ethanol. Rate saturation with either substrate or enzyme was observed in a manner qualitatively consistent with previously reported adsorption data. Although somewhat less reactive than Avicel at very low enzyme loadings, much higher reaction rates were observed for PTW220 at moderate and high enzyme loading because of its higher capacity to bind cellulase. At equal subtrate concentrations (as potential glucose) and fractional substrate coverage of 0.09, the initial rate of pretreated wood hydrolysis exceeded that of Avicel by 15-fold. For fractional substrate coverage values up to 0.09 (the maximum value achieved for PTW220), the initial rate was proportional to adsorbed enzyme for PTW220. However, the rate per adsorbed enzyme declined sharply with increasing fractional coverage for Avicel hydrolysis.     

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.     

Effects of Ni(II) on respirometric oxygen uptake

The effects of Ni(II), substrate and initial biomass concentrations on biochemical oxygen demand (BOD) were studied by using an electrolytic respirometer. The effects of Ni(II) (2.5, 5.0, 10.0, 25.0 mg/l) and substrate (325, 650, 1300 mg/l as chemical oxygen demand) in a synthetic wastewater with differing initial biomass concentrations (1, 10, 100 mg/l) were investigated. The biomass-to-metal ratio was found to be the most important parameter affecting the measured BOD values. The maximum specific growth rates were calculated and the results of batch respirometric experiments were analysed both by graphical and statistical methods. In statistical analyses, a factorial experimental design approach was followed and results were treated by multiple regression techniques. A mathematical model was developed to express the maximum oxygen uptake in terms of nickel, substrate and initial biomass concentrations and their magnitudes of their effects were compared. The biomass-to-metal ratio was found to be very significant so that another model that expresses oxygen uptake in relation to the biomass-to-metal ratio and also to substrate concentration was developed. Finally, the effect of Ni(II) was demonstrated to depend on both substrate and initial biomass concentrations. This effect was stimulatory at low concentrations of Ni(II), and complete inhibition was never observed even at the highest concentration of Ni(II) studied, which was 25.0 mg/l. Received: 4 January 1997 / Received revision: 10 June 1997 / Accepted: 29 June 1997