Reaction equilibrium for lipase-catalyzed condensation in organic solvent systems

Lipase-catalyzed condensation in an organic solvent is useful for the syntheses of esters. To reasonably design and optimize the reaction conditions, knowledge of the reaction equilibrium is required. The interaction of water with other reactants and the quantitative predictions for adsorption of water by a desiccant are discussed. The solvent effects on the reaction equilibrium are also elucidated in mixtures of nitrile and tert-alcohol.     

Reaction equilibrium for lipase-catalyzed condensation in organic solvent systems

Lipase-catalyzed condensation in an organic solvent is useful for the syntheses of esters. To reasonably design and optimize the reaction conditions, knowledge of the reaction equilibrium is required. The interaction of water with other reactants and the quantitative predictions for adsorption of water by a desiccant are discussed. The solvent effects on the reaction equilibrium are also elucidated in mixtures of nitrile and tert-alcohol.     

Physical and reactive extraction equilibria of penicillin G in a hydrogen-bond acceptor solvent system

Physical and reactive extraction equilibria of penicillin G were investigated experimentally and theoretically in the existence of n-butyl acetate as a hydrogen-bond acceptor solvent. Physical extraction equilibrium experiments were carried out varying the pH of aqueous phase and overall penicillin concentration. We compared the experimental data with the calculated results from four physical extraction equilibrium models suggested here and obtained the most reasonable model. Also, penicillin G was reactively extracted using Amberlite LA-2 in n-butyl acetate. The experimental variables were pH of the aqueous phase, overall amine concentration, and overall penicillin concentration. A combined equilibrium model including our physical extraction equilibrium expression and the reactive extraction equilibrium expression suggested by Reschke and Schügerl was used so as to analyze the current reactive extraction equilibrium system. The calculated results from the reactive extraction equilibrium model were in good agreement with the experimental data.     

Rational design of a more stable penicillin G acylase against organic cosolvent

We have used a simple and efficient approach by combining the known functional and structural properties of penicillin G acylase (PGA) from E. coli, and tried to mutate PGA of Bacillus megaterium with the goal of increasing the stability of the enzyme in organic solvents or at acidic pH. The PGA mutants Kβ427A, Kβ430A and Kβ427A/Kβ430A obtained have higher stability in DMF than the wild-type PGA.     

Continuous penicillin G hydrolysis in an electro-membrane reactor with immobilized penicillin G acylase

Penicillin G (2%, w/v in phosphate buffer, pH 8) was hydrolysed in a flow-through, miniature electro-membrane reactor with the penicillin G acylase immobilized in 5% (w/v) polyacrylamide (diam. 10 mm, thickness 2.6 mm, enzyme activity 24 U ml^–1). The conversion of penicillin G increased from 0.15 to almost 0.5 when the electric current applied to the reactor was changed from –600 to +600 A/m² with a substrate residency of 1 h. Symbols and abbreviations c _j ^p & concentration of component j in product stream (M) c _j ^s & concentration of component j in substrate stream (M) c _s ^o & substrate concentration at reactor inlet (M) C _j ^p=c _j ^p/c _S ⁰ & scaled concentration of component j in product stream C _j ^s=c _j ^s/c _S ⁰ & scaled concentration of component j in substrate stream i & electric current density (A/m²) j & reaction component, j P, Q or S P & main reaction product (6-aminopenicillanic acid) PGA & penicillin G acylase Q & side reaction product (phenylacetic acid) S & substrate (penicillin G) Y _s=C _P ^s+C _P ^p & substrate conversion & mean residence time of substrate and product streams in reactor (h) =C _Q ^s+C _Q ^p+C _S ^s+C _S ^s & check-sum of scaled concentrations =C _P ^p/(C _P ^s+C _P ^p) & separation factor of 6-aminopenicillanic acid (0 1)     

Lipase-catalyzed transesterification in organic media: solvent effects on equilibrium and individual rate constants

The kinetics of the immobilized lipase B from Candida antarctica have been studied in organic solvents. This enzyme has been shown to be slightly affected by the water content of the organic media, and it does not seem to be subject to mass transfer limitations. On the other hand, some evidence indicates that the catalytic mechanism of reactions catalyzed by this lipase proceeds through the acyl-enzyme intermediate. Moreover, despite the fact that the immobilization support dramatically enhances the catalytic power of the enzyme, it does not interfere with the intrinsic solvent effect. Consequently, this enzyme preparation becomes optimum for studying the role played by the organic solvent in catalysis. To this end, we have measured the acylation and deacylation individual rate constants, and the binding equilibrium constant for the ester, in several organic environments. Data obtained show that the major effect of the organic solvent is on substrate binding, and that the catalytic steps are almost unaffected by the solvent, indicating the desolvation of the transition state. However, the strong decrease in binding for hydrophilic solvents such as THF and dioxane, compared to the rest of solvents, cannot be easily explained by means of thermodynamic arguments (desolvation of the ester substrate). For this reason, data have been considered as an indication of the existence of an unknown step in the catalytic pathway occurring prior to formation of the acyl-enzyme intermediate.     

Encapsulation of crosslinked penicillin G acylase aggregates in lentikats: evaluation of a novel biocatalyst in organic media

The encapsulation of crosslinked enzyme aggregates (CLEA) of penicillin G acylase into a very rigid polymeric matrix based on polyvinyl alcohol (LentiKats) has been used successfully to improve the inadequate mechanical properties of CLEA. This encapsulation decreased CLEA activity by only around 40%. As compensation, a significant improvement in the stability of the CLEA in the presence of organic solvents was detected. This could be related to the highly hydrophilic environment inside the LentiKats biocatalysts: Partition experiments showed that the concentration of dioxane inside LentiKats was lower than in the reaction medium. In fact, thermal stability was about the same as in the corresponding CLEA. This permitted great improvement in the reaction rate for thermodynamically controlled synthesis of a model antibiotic (using phenylacetic acid and 7-amino-deacetoxycefalosporanic acid). Even more importantly, yields could be improved by using LentiKats-encapsulated CLEA, very likely by a favorable product/substrate partition. Thus, this very simple technique not only provides an efficient technique for solving the mechanical stability problem associated with CLEA, but also greatly improves the behavior of CLEA in organic media.     

Recovery of penicillin G from fermentation broth with reactive extraction in a mixer-settler

Summary In a laboratory countercurrent mixer-settler, penicillin was recovered from its fermentation broth by extraction with Amberlite LA-2 in n-butylacetate at pH 5.0 and reextracted from the ion-pair complex containing a solvent phase with a buffer at 7.2–7.5 with an overall degree of extraction above 90 %.Symbols A amine - AHP complex - c concentration - C partition coefficent - E degree of extraction - HP penicillin acid - K_G equilibrium constant - P, P^– penicillin acid anion Indices aq aqueous phase - org organic phase - A amine - AHP complex - G overall - HP free acid - P penicillin     

Detecting penicillin G in milk with impedimetric label-free immunosensor

A label-free impedimetric flow injection immunosensor for the direct detection of penicillin G has been developed. Anti-penicillin G was immobilized on a gold working electrode modified with a self-assembled monolayer of thioctic acid. Real time monitoring of impedance was carried out at the optimum frequency of 160 Hz. Under optimum operating conditions the system provided a wide linear range between 1.0 x 10(-13) and 1.0 x 10(-8) M with a very low detection limit of 3.0 x 10(-15) M, much lower than the MRL of penicillin G in milk (1.2 x 10(-8) M). The immobilized anti-penicillin G on self-assembled thioctic acid monolayer gold electrode was very stable and provided good reproducible signal after regeneration up to 45 times with a relative standard deviation (R.S.D.) lower than 4%. Good recoveries and precisions were obtained when spiked raw milk samples were analyzed.     

Enantioselective synthesis ofN-acetyl-l-methionine with aminoacylase in organic solvent

We have developed an enzymatic procedure for the enantiospecific synthesis ofN-acetyl-l-methionine with aminoacylase in an organic solvent.N-Acetyl-l-methionine was most effectively synthesized with a yield of about 90% (on the basis of thel-methionine used) when the reaction mixture, composed of 100 mm sodium acetate, 20 MMdl-methionine and aminoacylase (1000 units) immobilized on celite in 1 ml ethyl acetate saturated with 32 l 140mm sodium phosphate buffer (pH 7.0) containing 0.1 mm CoCl₂, was incubated at 30°C for 24 h.N-Acetyl-l-methionine was isolated from the reaction mixture and the enantiomeric excess was 100%.d-Methionine was also isolated from the mixture with a yield of about 95% and 90% enantiomeric excess. The method is applicable to the synthesis of otherN-acetyl-l-amino acids.     

Reactive extraction of penicillin G in a pilot plant Karr-column

Summary Penicillin G was extracted from a model medium with a secondary amine (Amberlite LA-2) as carrier in n-butylacetate as solvent in a 7.6 m high pilot plant Karr-column at different stroke frequencies, throughput of the phases, concentrations of Penicillin G and carrier and ratios of the throughputs of the aqueous and organic phases. Up to penicillin concentrations of 30 gl^–1, throughputs of the aqueous phase of 100 lh^–1 and throughput ratios of the aqueous phase-to-organic phase of 3, very high degrees of extraction (99%) can be achieved with a penicillin loss below 1%.Symbols a specific interfacial area with regard to the volume of the continuous phase - C partition coefficient - cA, cA, i concentration of carrier (sec. amine) in the bulk at the interface - cAHP, cAHP, i concentration of complex in the bulk at the interface - cH proton concentration - cHP_a, cHP_a,i concentration of free acid in the bulk of the aqueous phase at the interface - cHP_o, cHP_{o, i} concentration of free acid in the bulk of the organic phase, at the interface - cP, cP, i concentration of acid anions in the bulk of the aqueous phase, at the interface - d₃₂ Sauter droplet diameter - E degree of extraction - f stroke frequency - KG reaction equilibrium constant - K_phys distribution coefficient - N number of stages in cascade - t mean residence time of the aqueous phase - _aq throughput of the aqueous phase - _o throughput of the organic phase - Z dimensionless longitudinal coordinate of the column with regard to its active length (4 m) - holdup of the organic phase     

Stabilizing effect of penicillin G sulfoxide, a competitive inhibitor of penicillin G acylase: its practical applications.

We have found that penicillin G sulfoxide (pen G SO) behaves as a general stabilizing agent of two bacterial penicillin G acylases (PGAs) from E. coli and from K. citrophila), and this role is related to a strong inhibitory effect on the enzymes. The stabilizing effect has been observed during two different inactivation processes: (i) thermal inactivation of soluble enzymes at alkaline pH, and (ii) inactivation of immobilized enzymes as a consequence of covalent multiinteraction with highly activated agarose aldehyde gels. At the same time, pen G SO behaves as a strong competitive inhibitor of these two enzymes. The inhibition constant is more than 10-fold lower than the one corresponding to another smaller competitive inhibitor, phenylacetic acid (PAA), the structure of which is exactly the acyl donor moiety corresponding to pen G SO. In turn, PAA hardly exerts any stabilizing effect on PGAs. The stabilizing effect of pen G SO allowed the preparation of derivatives of these PGAs preserving full catalytic activity in spite of being 1,400- and 650-fold more stable than the corresponding soluble or one-point attached immobilized enzymes.     

Novel photocatalytic NAD+ recycling system with a semiconductor in organic solvent

A novel, simple NAD⁺ recycling system in an organic solvent is described. Alcohol dehydrogenase and NAD⁺ adsorbed on a semiconductor, TIO₂, catalyzed dehydrogenation of cinnamyl alcohol through photocatalytic regeneration of NAD⁺. The merit of this system in an organic solvent is discussed.     

Assay of penicillin acylase in organic media

Summary The synthetic substrate 6-nitro-3-(phenylacetamido) benzoic acid (NIPAB) is an appropriate substrate for assaying penicillin acylase activity in reversed micellar systems of Aerosol - OT in isooctane. Accumulation of 6-nitro-3-aminobenzoic acid (NABA) produced by the enzymatic hydrolysis of NIPAB, followed by the increase in absorbance at 405 nm, was linear at 4 to 20 mM for up to 30 minutes and 15 °C to 40 °C.Abbreviations PA penicillin acylase (penicillin amidohydrolase EC 3.5.1.11) - AOT Aerosol OT (sodium bis- (2-ethylhexyl) sulfosuccinate) - NIPAB 6-nitro-3-(phenylacetamido)-benzoic acid - NABA 6-nitro-3-aminobenzoic acid - BSA bovine serum albumin     

Transesterification of phosphatidylcholine with eicosapentaenoic acid ethyl ester using phospholipase A2 in organic solvent

Phospholipase A₂-catalysed transesterification of phosphatidylcholine (PC, 99%) with eicosapentaenoic acid ethyl ester (EPAEE, 95%) was carried out in organic solvent. The maximum yield was 14.3% (w/w). The optimum reaction condition was 50°C, 48 h, initial water activity 0.25 and molar ratio of PC to EPAEE 1:10 in 5 ml toluene.     

Papain kinetics in the presence of a water-miscible organic solvent

The effects of various concentrations of a water-miscible organic solvent [a 7:3 (v/v) mixture of N, N dimethylformamide and dimethylsulfoxide] on the kinetics of papain have been investigated. The parameters k(cat) and K(m) for the amidase and esterase activity of papain using N-alpha-benzoyl-DL-arginine-p-nitroanilide (BAPNA) and N-alpha-benzoyl-L-arginine ethyl ester (BAEE) as substrates were determined. For both types of activity, k(cat) initially increased (up to about 15% solvent), and then decreased with increasing concentrations of organic solvent. In contrast, K(m) increased sharply with the organic solvent concentration. Active site titration at 0 and 50% solvent indicated no change in the amount of active enzyme. Fluorometric measurements of the emission spectrum of papain did not indicate any major conformational changes with increasing concentrations of organic solvent.     

Effect of organic cosolvent on kinetic resolution of tert-leucine by penicillin G acylase from Kluyvera citrophila

Penicillin G acylase (PGA) from Kluyvera citrophila immobilized on Amberzyml was used for enantioselective hydrolysis of N-phenylacetylated-dl-tert-leucine (N-Phac-dl-Tle) to produce l-tert-leucine (l-Tle). The effects of various organic cosolvents on hydrolysis of N-Phac-dl-Tle have been investigated in aqueous-cosolvent medium. It was founded that the rate of PGA-catalyzed reaction was significantly affected by the presence of 2% (v/v) organic cosolvent concentration. The initial rate fell with increasing logP of the cosolvent, but for logP values less than −0.24 the rate was faster than in purely aqueous medium. Additionally, the relative rate increases with the increase of dielectric constant (ε) of organic cosolvents. The yields of l-Tle in all aqueous-cosolvent systems were above 95% with the enantiomeric excess (ee) of >99%.     

Modeling hydration mechanisms of enzymes in nonpolar and polar organic solvents

A comprehensive study of the hydration mechanism of an enzyme in nonaqueous media was done using molecular dynamics simulations in five organic solvents with different polarities, namely, hexane, 3-pentanone, diisopropyl ether, ethanol, and acetonitrile. In these solvents, the serine protease cutinase from Fusarium solani pisi was increasingly hydrated with 12 different hydration levels ranging from 5% to 100% (w/w) (weight of water/weight of protein). The ability of organic solvents to 'strip off' water from the enzyme surface was clearly dependent on the nature of the organic solvent. The rmsd of the enzyme from the crystal structure was shown to be lower at specific hydration levels, depending on the organic solvent used. It was also shown that organic solvents determine the structure and dynamics of water at the enzyme surface. Nonpolar solvents enhance the formation of large clusters of water that are tightly bound to the enzyme, whereas water in polar organic solvents is fragmented in small clusters loosely bound to the enzyme surface. Ions seem to play an important role in the stabilization of exposed charged residues, mainly at low hydration levels. A common feature is found for the preferential localization of water molecules at particular regions of the enzyme surface in all organic solvents: water seems to be localized at equivalent regions of the enzyme surface independently of the organic solvent employed.