Enzyme glycation influences product yields during oligosaccharide synthesis by reverse hydrolysis

Possible evidence is presented for Maillard glycation of enzymes during oligosaccharide synthesis by reverse hydrolysis. In 70% (w/v) mannose solutions, 1,2-α-mannosidase from Penicillium citrinum lost 40% and α-mannosidase from almonds lost 60% activity at 55 °C over 2 weeks. Oligosaccharide yields were 15 and 45% respectively. Higher molecular weight glycation adducts were formed in a time-dependent manner as seen by MALDI-TOF. Inhibitors of the Maillard reaction were able to partially alleviate these effects resulting in reduced loss of enzyme activity and oligosaccharide yield increases of 27–53% relative to the control.     

Optimization of Operating Temperature for Continuous Immobilized Glucose Isomerase Reactor with Pseudo Linear Kinetics

In this work, the optimal operating temperature for the enzymatic isomerization of glucose to fructose using a continuous immobilized glucose isomerase packed bed reactor is studied. This optimization problem describing the performance of such reactor is based on reversible pseudo linear kinetics and is expressed in terms of a recycle ratio. The thermal deactivation of the enzyme as well as the substrate protection during the reactor operation is considered. The formulation of the problem is expressed in terms of maximization of the productivity of fructose. This constrained nonlinear optimization problem is solved using the disjoint policy of the calculus of variations. Accordingly, this method of solution transforms the nonlinear optimization problem into a system of two coupled nonlinear ordinary differential equations (ODEs) of the initial value type, one equation for the operating temperature profile and the other one for the enzyme activity. The ODE for the operating temperature profile is dependent on the recycle ratio, operating time period, and the reactor residence time as well as the kinetics of the reaction and enzyme deactivation. The optimal initial operating temperature is selected by solving the ODEs system by maximizing the fructose productivity. This results into an unconstrained one‐dimensional optimization problem with simple bounds on the operating temperature. Depending on the limits of the recycle ratio, which represents either a plug flow or a mixed flow reactor, it is found that the optimal temperature of operation is characterized by an increasing temperature profile. For higher residence time and low operating periods the residual enzyme activity in the mixed flow reactor is higher than that for the plug flow reactor, which in turn allows the mixed flow reactor to operate at lower temperature than that of the plug flow reactor. At long operating times and short residence time, the operating temperature profiles are almost the same for both reactors. This could be attributed to the effect of substrate protection on the enzyme stability, which is almost the same for both reactors. Improvement in the fructose productivity for both types of reactors is achieved when compared to the constant optimum temperature of operation. The improvement in the fructose productivity for the plug flow reactor is significant in comparison with the mixed flow reactor.     

Entrapping of Tyrosinase in a System of Reverse Micelles

The enzymatic activity of tyrosinase was studied both in aqueous and organic media. In the latter case tyrosinase was entrapped in a system of reverse micelles of Aerosol OT in octane. At hydration degree 25, when the inner cavity of the reverse micelles was comparable with the size of a tetrameric tyrosinase form known for aqueous solutions, an optimum level of catalytic activity was observed. Another peak of catalytic activity of tyrosinase was observed at hydration degree 12, when the size of the inner cavity of the reverse micelles was consistent with a monomeric form of tyrosinase. Thus, the system of reverse micelles can be exploited as a medium for the investigation of the monomeric form of tyrosinase, which is unstable in aqueous solution.     

Neuroglobin: enzymatic reduction and oxygen affinity

Neuroglobin (Ngb) is a hexacoordinate globin expressed in the nervous system of vertebrates, involved in neuroprotection. O₂ equilibrium measurements on mouse Ngb yielded significantly different P₅₀ values, ranging from ∼2 torr to ∼10 torr. By a kinetic approach minimizing the effects of protein autoxidation, we measured P₅₀ = 2.2 torr at 20 °C. As predicted from the structure, O₂ binds to the Y44D Ngb mutant more quickly (k = 2.2 s⁻¹ vs 0.15 s⁻¹) and with slightly higher affinity (P₅₀ = 1.3 torr) than wild-type. In addition, we introduced a novel reduction protocol for metNgb based on NADH:flavorubredoxin oxidoreductase (FlRd-red) from Escherichia coli, a candidate for the Ngb reducing activity recently identified in E. coli extracts. Interestingly, E. coli FlRd-red shares sequence similarity with the FAD-binding domain of the human apoptosis-inducing factor, a finding which may have unexpected significance with reference to the mechanism of neuroprotection by Ngb.     

Preparation and characterization of immobilized lipase on magnetic hydrophobic microspheres

A novel magnetic poly(vinyl acetate (VAc)–divinyl benzene (DVB)) material (8–34 μm) was synthesized by copolymerization of vinyl acetate and divinyl benzene using oleic acid-stabilized magnetic colloids as magnetic cores. The magnetic colloids and the copolymer microspheres were characterized with transmission and scanning electron microscopes, respectively. Magnetization of the microspheres could be described by the Langevin function. All the observations indicated that the microspheres were superparamagnetic. Magnetic sedimentation of the microspheres was achieved within 3 min, over 300 times faster than the gravitational sedimentation. Candida cylindracea lipase (CCL) was immobilized to the porous carrier at up to 6750 IU/g carrier, remarkably higher than the previous studies. The pH and temperature dependencies of the immobilized CCL were investigated and the optimum temperature and pH for the immobilized CCL were determined. Activity amelioration of the immobilized CCL for the hydrolysis of olive oil was observed, indicating an interfacial activation of the enzyme after immobilization. Moreover, the immobilized CCL showed enhanced thermal stability and good durability in the repeated use after recovered by magnetic separations.     

Enzymatic production of γ-L-glutamyltaurine through the transpeptidation reaction of γ-glutamyltranspeptidase from Escherichia coli K-12

γ-L-Glutamyltaurine is a naturally occurring peptide and known to have several physiological functions in mammals. This paper describes a new method for the enzymatic production of γ-L-glutamyltaurine from L-glutamine and taurine through the transpeptidation reaction of γ-glutamyltranspeptidase (EC 2.3.2.2) of Escherichia coli K-12. The optimum conditions for the production of γ-L-glutamyltaurine were 200 mM L-glutamine, 200 mM taurine and 0.2 U/ml γ-glutamyltranspeptidase, pH 10, and 1-h incubation at 37°C. Forty-five mM γ-L-glutamyltaurine was obtained, the yield being 22.5%. γ-L-Glutamyltaurine was purified on Dowex 1 × 8 and C₁₈ columns, and identified by means of NMR and a polarimeter.     

Enzymatic synthesis of 2-ethylhexyl esters of fatty acids by immobilized lipase from Candida sp. 99–125

The 2-ethylhexyl esters of fatty acids were synthesized by immobilized lipase from Candida sp. 99–125. The reuse stability of immobilized lipase was at least four batches. The conditions of enzymatic synthesis of 2-ethylhexyl palmitate were optimized. In the system of petroleum ether, 10% (w/w) immobilized lipase was used in the esterfication of 2-ethyl hexanol (7.8 mmol) and palmitic acid (7.8 mmol) at 40 °C with silica gel as the water absorbent. The esterification degree was 91% under these conditions. The purity of 2-ethylhexyl palmitate was 98% after purification consisting washing by water and evaporation to remove the organic solvent.     

Stabilization of a tetrameric enzyme (α-amino acid ester hydrolase from Acetobacter turbidans) enables a very improved performance of ampicillin synthesis

The stabilized derivative of the enzyme α-amino acid ester hydrolase from Acetobacter turbidans has been found to be very adequate as biocatalyst of the synthesis of the very relevant antibiotic ampicillin. This enzyme resulted much more adequate than the Penicillin G Acylase (PGA) from Escherichia coli (the most used enzyme). The stabilization of the enzyme was required because under optimal conditions (absence of phosphate and 40% of MeOH), no-stabilized derivatives or soluble enzyme from A. turbidans become very rapidly inactivated. Under these conditions, this new stabilized derivative exhibited a very high selectivity for the transferase activity compared to the esterase one, as well as a very low hydrolytic activity towards the antibiotic. Moreover, this new biocatalyst did not recognize -phenylglycine as substrate in the synthetic process. By using the racemic mixture of / phenylglycine methyl ester, 85% of the -ester could be transformed to ampicillin. In contrast, the enzyme from E. coli exhibited a high hydrolytic activity for the ampicillin yielding low synthetic yields. This enzyme also resulted much less enantioselective producing both isomers of the antibiotic.     

Continuous enzymatic regeneration of redox mediators used in biotransformation reactions employing flavoproteins

Oxidoreductases are a group of enzymes that have been regarded uneconomical for industrial processes due to their dependence on cofactors or prosthetic groups for activity and the difficulties of regenerating these. Especially, flavoproteins have long been neglected for biocatalytical applications. The prosthetic group of some of these enzymes, but not all, can be regenerated by oxygen, resulting in hydrogen peroxide formation, which is detrimental to enzyme stability. As a contribution to alleviating this problem, a novel concept for the regeneration of electron acceptors (redox mediators) for flavoenzymes is described. Flavin-containing enzymes such as cellobiose dehydrogenase (CDH) or pyranose oxidase (P2O) are used in conjunction with laccases and a redox mediator. The flavin of the synthetic enzyme is reduced while the oxidized product of interest is formed, in turn, the flavin is reoxidized with the help of an electron acceptor, which then is regenerated using a laccase. Laccases are copper containing phenol oxidases that can transfer four electrons to oxygen, producing two molecules of water. Preliminary screening experiments with different redox mediators, and a coupled enzyme system of CDH and laccase, showed that a wide variety of different substances can efficiently shuttle electrons between these two enzymes. Among them are substituted and unsubstituted ortho- and para-quinones, benzoquinone imines, cation radicals such as 2,2′-azinobis(3-ethylbenzthiazoline-6-sulfonic acid) (ABTS), redox dyes such as phenothiazines or phenoxazines, as well as iron complexes.

Experiments in which CDH completely oxidizes lactose to lactobionic acid and P2O entirely converts glucose to 2-keto-glucose are presented. Catalytic amounts of redox mediators are used and continuously regenerated by a laccase. Specific productivities of up to 19.3 g·(h·kU)⁻¹ and 72 g·(h·kU)⁻¹ for CDH and P2O, respectively, were found. The total turnover numbers (TTNs) for the two enzymes used were in the range of 10⁵–10⁶. Oxygen supply for the laccase is a crucial factor in avoiding rate limitation. Undeniably, this system facilitates the efficient use of a hitherto underexploited group of enzymes for preparative purposes.     

Biosaccharification of cellulosic biomass in immiscible solvent–water mixtures

The enzymatic hydrolysis of wheat straw was carried out in bi-phasic media prepared with acetate esters and Na-acetate buffer. The volume percentage of the organic chemicals was 75%. The biomass was pretreated in a steam explosion plant at 217°C and for 3 min. A cellulase complex from commercial source was utilised and the experiments were run at 45°C and at constant enzyme to biomass weight ratio (0.06). Biomass loadings ranged from 6.25 to 100 g per litre of reactor. The amount of glucose formed per litre of reactor and hour and the glucose yield (grams of product per gram of biomass) were close to the values attained in pure buffer. The glucose concentration in the aqueous phase was in bi-phasic media much higher than in pure buffer and reached the value of 146 g l_H2O⁻¹ during 72 h of saccharification. The results were poorly dependent on the physical–chemical properties of the solvents. Nevertheless, butyl acetate could be slightly preferred to propyl and i-amyl acetate. The use of bi-phasic media did not require stirring rate higher than in pure buffer. The presence of acetate ester traces did not alter markedly the production of ethanol in the fermentation stage, but determined the extension of the lag phase.