Lipase catalyzed polytransesterification in an organic solvent

Summary Lipase-catalyzed polytransesterification ofbis(2,2,2-trifluoroethyl) dodecanedioate with aliphatic diols (from 1,2-ethanediol to 1,6-hexanediol) was studied with 4 enzymes and a number of solvents. The effects of experimental parameters were investigated with the purpose of obtaining a polyester of as high as possible average molar mass. The highest mass average molar mass (M _w) of 34,750 g mol^-1 (DP = 122) was obtained under vacuum with 1,4-butanediol,Mucor miehei lipase, and diphenyl ether as solvent.     

Steady state kinetics of an enzyme reaction with one substrate and one modifier

This study examines the steady state kinetics of a reaction involving an enzyme, a substrate and a modifier when the reaction follows Michaelis-Menten kinetics. Conditions for Michaelis-Menten kinetics are deduced, and it is shown that an analogue of detailed balance determines the complexity of the rate equations in these cases. A scheme to distinguish many cases of Michaelis-Menten kinetics is presented. It is shown that steady state kinetics are, in general, insufficient to specify the mechanism of a reaction, since different effects of a modifier can give identical steady state kinetic data.     

The solvent effects on the kinetics of bacterial formate dehydrogenase reaction

The increase in concentration of organic cosolvents results in a 2-2.5-fold increase of the maximal reaction rate and a decrease of Michaelis constant for formate of NAD(+)-dependent formate dehydrogenase from methylotrophic bacteria Pseudomonas sp. 101. These parameters, however, are not affected with the increase of ionic strength. For the logarithm of both Vmax and Km a linear function of the reciprocal of solvent dielectric permittivity was found. The decrease of Km is possibly due to the dielectric screening effect on the substrate binding energy. The increase in Vmax is explained by a model based on a solvent-dependent electrostatic image force, acting on the charges moved in the course of the catalytic step of the enzyme reaction.     

Reactivation kinetics of guanidine hydrochloride-denatured creatine kinase measured using the substrate reaction

Guanidine hydrochloride-denatured creatine kinase (CK) can very quickly form a dimer with reactivity when the denaturant is diluted into the reaction system in the presence of DTT or EDTA. Tsou's method and its applied equation [Tsou (1988), Adv. Enzymol. Rel. Areas Mol. Biol. 61, 381–436; Yang and Zhou (1998), Biochim. Biophys. Acta 1388, 190–198] were used to measure the kinetic reactivation rate constants and the reactivation degree for reassociated CK dimers. Partial reactivation (about 50% at best) occurred following a monophasic course during the substrate reaction when compared with previous time interval measurements. The reactivation degree increased with increasing DTT (0.1–5 mM) and EDTA (0.1–1 mM) concentrations. The apparent forward rate constants do not change with DTT concentration, showing that the reactivation is a reversible first-order reaction, but not of complex formation type. However, the apparent forward rate constants do change with EDTA concentration, showing that the reactivation with EDTA is a reversible first-order reaction as well as of complex formation type. Excess DTT concentrations have an inhibitory effect, indicating that the excessive EDTA acts as a metal chealate not only for free Mg²⁺, but also for MgATP during the enzyme catalysis. This study shows that additional information about the reactivation of CK can be obtained from examining the substrate reaction. The possible refolding pathway of CK is discussed.     

Optimal substrate feeding policy for a fed batch fermentation with substrate and product inhibition kinetics

The optimal substrate feeding policy for the fed batch fermentation which is governed by product and substrate inhibited kinetics is presented. The conjunction point between nonsingular and singular arcs and the feeding policy along the singular arc are derived analytically in terms of the concentrations of substrate and product and the liquid volume. Thus, it is possible to determine the feeding rate by monitoring the state variables (i.e., closed loop control). As a specific example, an optimization study of the fed batch fermentation for ethanol production by Saccharomyces cerevisiae is presented. It is shown that the optimal feeding patterns are heavily dependent upon the initial conditions. The point selectivity provides the guideline for predicting the optimal feeding patterns and explaining the results of rigorous mathematical analysis.     

Reactions of anthranilate hydroxylase with salicylate, a nonhydroxylated substrate analogue. Steady state and rapid reaction kinetics

Steady state and rapid reaction kinetics of the flavoprotein anthranilate hydroxylase (EC 1.14.12.2) have been examined with the nonhydroxylated substrate analogue, salicylate. Since the reaction with salicylate does not involve events in which aromatic substrate is oxygenated, it provides a simpler model for studying the hysteresis exhibited by this enzyme. It is shown that the first turnover of the enzyme is slower than subsequent turnovers owing in part to slow initial binding reactions of salicylate with the enzyme. The reductive half-reaction of the first turnover is also slow since rapid reduction of the enzyme flavin requires bound aromatic substrate. The oxidative half-reaction involves reaction of the reduced enzyme-salicylate complex with oxygen to form a flavin C4a-hydroperoxide, which then decays to oxidized flavoenzyme and H2O2. Several lines of evidence indicate that salicylate remains bound to the enzyme at the end of the catalytic cycle so that in turnovers subsequent to the first, the slow steps involving salicylate binding are avoided.     

Analytic solution to steady-state radial diffusion of a substrate with first-order reaction kinetics in the tissue of a Krogh's cylinder

It is often useful to calculate the concentration profile for a substrate undergoing reaction in the tissue surrounding a capillary. In this paper, we consider a model geometry consisting of a long straight cylinder of tissue surrounding a capillary. Substrate diffuses radially out of the capillary through the tissue, with consumption of substrate in the tissue directly proportional to substrate concentration (i.e., first-order reaction kinetics). The model is extended to include the case where a cylinder of necrotic tissue surrounds a metabolically active inner tissue cylinder. A simple analytic solution is derived, and concentration profiles are generated for various combinations of parameters. Compared to the case where substrate consumption is independent of concentration, this model predicts much more rapid depletion of substrate near the capillary interface. This can have significant implications for the calculation of the hypoxic fraction (e.g., tissue with pO(2)<0.5-5 mmHg) when tumor oxygenation is modeled. The model also permits calculation of the limiting substrate concentration for cell viability when the reaction rate constant is known and vice versa.     

Generalization of monod kinetics for analysis of growth data with substrate inhibition

The inhibitory effect of butanol on yeast growth has been studied for the strain Candida utilis ATCC 8205 growing aerobically on butanol under batch conditions. A mathematical expression was then proposed to fit the kinetic pattern of butanol inhibition on the specific growth rate: \documentclass{article}\pagestyle{empty}\begin{document}$$ \mu = \frac{{\mu _m S}}{{K_s + S}}\left[{1 - \frac{S}{{S_m }}} \right];n $$\end{document}The maximum allowable butanol concentration above which cells do not grow was predicted to be 9.16g/L. The proposed model appears to accurately represent the experimental data obtained in this study and the literature data developed for a variety of batch culture systems at widely ranging substrate concentrations.     

Helical screw sense bias in chiral polyfluorene stimulated by solvent

Conjugated homopolymer poly(9,9‐bis(3‐((S )‐2‐methylbutylpropanoate))fluorene) (PSF) with chiral pendants was synthesized and characterized. Dissolution experiments show that PSF is well dissolved in racemic limonene at high temperature and begins aggregating upon sequential cooling treatment. The corresponding assemblies were transferred to quartz plate by the spin‐coating method. Comparably, film casting from chloroform solution was also prepared. Upon annealing thermal treatments, these PSF films exhibited perfect mirror circular dichroism (CD) Cotton effects and dissymmetry ratios. Optical absorption spectroscopy (UV‐vis), CD, and fluorescence spectroscopy results reveal that chiral side chains successfully induced M ‐ and P ‐helical structures in aggregates and films, and this significant difference was ascribed to their differential supramolecular conformations.     

Lipase activity of resting cells of Aspergillus flavus after solvent washing; memory effects from endogenous substrate arising from the original growth medium

Aspergillus flavusresting cells were washed with solvents of different polarity for 2, 6, and 24 h and then suspended in isooctane containing either oleic acid and 1-propanol or 1-propanol alone. Propyl oleate and propyl linoleate were produced in all experiments after 24 h due to the presence of residual fatty acids originating from the sunflower oil used for growing the mycelium. After 24 h washing, most solvents produced a 70 to 90% decrease in lipase activity and a 0 to 99% decrease in the amount of residual acids. 0.7 M 1-propanol in hexane was the best washing solvent among all those assayed (93% remaining activity, 0.3% residual oleic acid).     

Improving lipase enantioselectivity in organic solvents by forming substrate salts with chiral agents

We recently demonstrated (J Am Chem Soc 121:3334-3340, 1999) that enzymatic enantioselectivity in organic solvents can be markedly enhanced by temporarily enlarging the substrate via salt formation. In the present study, this approach was expanded by finding that, in addition to its size, the stereochemistry of the counterion can greatly affect the enantioselectivity enhancement. For example, the enantioselectivity [E = (k(cat)/K(M))(S)/(k(cat)/K(M))(R)] of crystalline Pseudomonas cepacia lipase in the propanolysis of phenylalanine methyl ester (PheOMe) in anhydrous acetonitrile was found to be 5.8 +/- 0.6; the E value doubled when PheOMe's salt with S mandelic acid was used as a substrate instead of the free ester, and rose sevenfold with R mandelic acid as a Bronsted-Lowry acid. Similar effects were observed with other bulky, but not petite, counterions. The greatest enantioselectivity enhancement was afforded by 10-camphorsulfonic acid: the E value increased to 18 +/- 2 for a salt with its R enantiomer and jumped to 53 +/- 4 for the S. These effects, also observed in other organic solvents, were explained by means of structure-based molecular modeling of the lipase-bound transition states of the substrate enantiomers and their diastereomeric salts.     

Lipase catalyzed preparation of biodiesel from Jatropha oil in a solvent free system

The monoethyl esters of the long chain fatty acids (biodiesel) were prepared by alcoholysis of Jatropha oil, a non-edible oil, by a lipase. The process optimization consisted of (a) screening of various commercial lipase preparations, (b) pH tuning, (c) immobilization, (d) varying water content in the reaction media, (e) varying amount of enzyme used, and (f) varying temperature of the reaction. The best yield 98% (w/w) was obtained by using Pseudomonas cepacia lipase immobilized on celite at 50 °C in the presence of 4–5% (w/w) water in 8 h. It was found that yields were not affected if analytical grade alcohol was replaced by commercial grade alcohol. This biocatalyst could be used four times without loss of any activity.     

Structural basis for chiral substrate recognition by two 2,3-butanediol dehydrogenases

2,3-Butanediol dehydrogenase (BDH) catalyzes the NAD-dependent redox reaction between acetoin and 2,3-butanediol. There are three types of homologous BDH, each stereospecific for both substrate and product. To establish how these homologous enzymes possess differential stereospecificities, we determined the crystal structure of l-BDH with a bound inhibitor at 2.0 Å. Comparison with the inhibitor binding mode of meso-BDH highlights the role of a hydrogen-bond from a conserved Trp residue¹⁹². Site-directed mutagenesis of three active site residues of meso-BDH, including Trp¹⁹⁰, which corresponds to Trp¹⁹² of l-BDH, converted its stereospecificity to that of l-BDH. This result confirms the importance of conserved residues in modifying the stereospecificity of homologous enzymes.     

Helix nucleation kinetics from molecular simulations in explicit solvent

We study the reversible folding/unfolding of short Ala and Gly-based peptides by molecular dynamics simulations of all-atom models in explicit water solvent. A kinetic analysis shows that the formation of a first alpha-helical turn occurs within 0.1-1 ns, in agreement with the analyses of laser temperature jump experiments. The unfolding times exhibit Arrhenius temperature dependence. For a rapidly nucleating all-Ala peptide, the helix nucleation time depends only weakly on temperature. For a peptide with enthalpically competing turn-like structures, helix nucleation exhibits an Arrhenius temperature dependence, corresponding to the unfolding of enthalpic traps in the coil ensemble. An analysis of structures in a "transition-state ensemble" shows that helix-to-coil transitions occur predominantly through breaking of hydrogen bonds at the helix ends, particularly at the C-terminus. The temperature dependence of the transition-state ensemble and the corresponding folding/unfolding pathways illustrate that folding mechanisms can change with temperature, possibly complicating the interpretation of high-temperature unfolding simulations. The timescale of helix formation is an essential factor in molecular models of protein folding. The rapid helix nucleation observed here suggests that transient helices form early in the folding event.     

Ordered mesoporous materials containing Mucor Miehei Lipase as biocatalyst for transesterification reaction

Herein, we report the design of a biocatalyst by the immobilization of Mucor Miehei Lipase (Mm-L) onto mesoporous silica materials. Supports with different pore diameters have been considered. Infrared spectroscopy was used to determine the adsorption isotherms in different pH conditions.Then, the biocatalyst was tested for the methanolysis of colza oil. The production of methyl esters was monitored over time by gas chromatography coupled to a mass spectrometer. The results show that to reach maximum performance of the biocatalyst, a certain amount of water is required (5 wt.%). By using ratio lower than the stoichiometry (1:1), the methanol conversion is completed and high transesterification yields could be obtained even in the absence of non polar solvents (i.e. hexane). Herein, the lipase uses the fatty substrate as lipophilic interface required for the opening of the active site of the enzyme.     

Models for mineralization kinetics with the variables of substrate concentration and population density.

The rates of mineralization of [14C]benzoate by an induced population of Pseudomonas sp. were measured at initial substrate concentrations ranging from 10 ng/ml to 100 micrograms/ml. Plots of the radioactivity remaining in the culture were fit by nonlinear regression to six kinetic models derived from the Monod equation. These models incorporate only the variables of substrate concentration and cell density. Plots of the mineralization kinetics in cultures containing low, intermediate, and high initial substrate concentrations were well fit by first-order, integrated Monod, and logarithmic kinetics, respectively. Parameters such as maximum specific growth rate, half-saturation constant, and initial population density divided by yield agreed between cultures to within a factor of 3.4. Benzoate mineralization by microorganisms in acclimated sewage was shown to fit logistic (sigmoidal), Monod, and logarithmic kinetics when the compound was added at initial concentrations of 0.1, 1.0, and 10 micrograms/ml, respectively. The mineralization of 10 micrograms of benzoate per ml in sewage also followed logarithmic kinetics in the absence of protozoa. It is concluded that much of the diversity in shapes of mineralization curves is a result of the interactions of substrate concentration and population density. Nonlinear regression with models incorporating these variables is a valuable means for analysis of microbial mineralization kinetics.     

Variable elimination in post-translational modification reaction networks with mass-action kinetics

We define a subclass of chemical reaction networks called post-translational modification systems. Important biological examples of such systems include MAPK cascades and two-component systems which are well-studied experimentally as well as theoretically. The steady states of such a system are solutions to a system of polynomial equations. Even for small systems the task of finding the solutions is daunting. We develop a mathematical framework based on the notion of a cut (a particular subset of species in the system), which provides a linear elimination procedure to reduce the number of variables in the system to a set of core variables. The steady states are parameterized algebraically by the core variables, and graphical conditions for when steady states with positive core variables imply positivity of all variables are given. Further, minimal cuts are the connected components of the species graph and provide conservation laws. A criterion for when a (maximal) set of independent conservation laws can be derived from cuts is given.