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Synthesis of nucleopeptides by employing an enzyme-labile urethane protecting group.

Nucleoproteins are naturally occurring biopolymers in which the hydroxy group of a serine, a threonine, or a tyrosine moiety is linked through a phosphodiester group to the 3'- or 5'-end of a nucleic acid. For the study of the biological phenomena in which nucleoproteins are involved, for example, viral replication, nucleopeptides embodying the characteristic linkage between the peptide chain and the oligonucleotide may serve as powerful tools. However, as a result of the multifunctionality and the pronounced acid and base lability of nucleopeptides, their synthesis requires the application of a variety of orthogonally stable blocking groups, which can be removed under the mildest conditions. We have developed a new mild enzymatic deprotection method, that is, the penicillin G acylase-catalyzed hydrolysis of the N-phenylacetoxybenzyloxycarbony (PhAcOZ) group, for the synthesis of nucleopeptides. We demonstrate the wide applicability of this method by coupling the N-terminally deprotected nucleopeptides 31 a-c with PhAcOZ-protected amino acids and subsequent removal of the N-PhAcOZ group from fully protected nucleotetrapeptides 32 a,b with penicillin G acylase. The reaction conditions are very mild (pH 6.8) so that no undesired side reaction such as cleavage of the nucleotide bond or beta-elimination of the nucleotide was observed.

Amino Acids↗

Impact of deglycosylation methods on two-dimensional gel electrophoresis and matrix assisted laser desorption/ionization-time of flight-mass spectrometry for proteomic analysis.

Glycosylation is a common post-translational modification that can add complexity to the proteome of many cell types. We used enzymatic and chemical methods of deglycosylation to treat a heavily glycosylated exoproteome sample from the filamentous fungus Trichoderma reesei. Deglycosylated samples were resolved on one-dimensional (1-D) and two-dimensional (2-D) gels in order to determine the effect of deglycosylation on the electrophoresis patterns and on the ability to identify proteins by peptide mass matching using matrix assisted laser desorption/ionization-time of flight-mass spectrometry (MALDI-TOF-MS) analysis of in-gel tryptic digests. We found that deglycosylation of the protein sample resulted in different protein patterns on 1-D and 2-D gels, reduced the complexity of gel patterns, and enhanced the protein identification of some proteins via MALDI-TOF-MS. Deglycosylation with trifluoromethanesulfonic acid (TFMS) was found to be more effective than enzymatic treatments. These deglycosylation techniques may be employed in whole proteome analysis to locate glycosylated proteins and assist in their identification by MS.

Amidohydrolases↗

A high-performance liquid chromatography based strategy for rapid, sensitive sequencing of N-linked oligosaccharide modifications to proteins in sodium dodecyl sulphate polyacrylamide electrophoresis gel bands.

The majority of biologically active proteins are glycosylated, therefore any approach to proteomics which fails to address the analysis of oligosaccharides is necessarily incomplete. To appreciate the structure of a glycoprotein fully, to understand the roles for the attached oligosaccharides and to monitor disease associated changes it is necessary to visualise the sugars as well as the protein. To achieve this aim when biological samples are available at the low microgram level or less has involved increasing the sensitivity of the technology for glycan analysis. Since one protein may have many different oligosaccharides attached to it (glycoforms) this is a major technical challenge. CD59, for example, has over 100 different sugars at one N-linked glycosylation site. Applications of recently developed technology suggest that it is now becoming realistic to extend the proteomics analysis of glycoproteins to include details of glycosylation. This is achieved by releasing the N-glycans from the protein in a gel by optimised peptide-N-glycosidase F digestion. The released glycans are then tagged with the fluorophore, 2-amino benzamide. The labelled glycan pools (containing 50-100 femtomoles of glycans) are resolved by predictive normal phase high performance liquid chromatography (HPLC) on an amide based column or by reverse phase HPLC on a C18 column. Preliminary structural assignments are confirmed by exoglycosidase array digestions of the entire glycan pool. Complementary matrix-assisted laser desorption/ionization-mass spectrometry, which requires 10-20 times as much sugar for a single run, can be used where there is sufficient material. This provides a composition analysis but not linkage information.

Amidohydrolases↗

Identification of protein-bound carbohydrates by mass spectrometry.

This review outlines the use of modern methods of mass spectrometry, mainly based on electrospray ionization and matrix-assisted lased desorption/ionization, for the identification of protein-bound carbohydrates. The techniques are briefly described together with methods for glycan release and purification prior to mass spectrometry. Fragmentation of glycans, produced under various conditions, is described in the context of obtaining structural information at the sensitivity required for proteomic work.

Amidohydrolases↗

Structure-guided consensus approach to create a more thermostable penicillin G acylase.

The thermostabilization of penicillin G acylase (PGA) is a difficult problem due to the large size of the protein and its complex maturation process. We developed a data-driven protein design method that requires fewer homologous sequences than the traditional consensus approach and utilizes structural information to limit the number of variants created. Approximately 50% of our 21 single-point mutants were found experimentally to be more thermostable than the wild-type PGA, two had almost threefold longer half-life at 50 degrees C, with very little effect on activity. An analysis of four programs that predict the thermostability conferred by point mutations shows little agreement between the programs and with the experimental data, emphasizing that the chosen stabilizing mutations are very difficult to predict, but that our data-driven design method should prove useful.

Bacteria↗

Fluorogenic substrates for lipases, esterases, and acylases using a TIM-mechanism for signal release.

3-Acyloxyl-2-oxopropyl ethers of umbelliferone were investigated as new fluorogenic substrates for lipases and esterases. The aliphatic primary alcohol-leaving group released the fluorescent product umbelliferone by an enolization/beta-elimination reaction similar to the triose phosphate isomerase (TIM) reaction. A similarly designed phenylacetamide provided a fluorescent probe for penicillin G acylase, whereby the enolization/beta-elimination sequence from the intermediate aminoketone was very fast and spontaneous even under acidic conditions. The corresponding epoxyketone was not fluorogenic with epoxide hydrolases (EH). These substrates represent periodate-free Clips-otrade mark substrates.

Acetamides↗

Metabolic control of recombinant monoclonal antibody N-glycosylation in GS-NS0 cells.

Variable N-glycosylation at Asn(297) in the Fc region of recombinant therapeutic immunoglobulin G (IgG) molecules, specifically terminal galactosylation and sialylation, may affect both pharmacokinetic behavior and effector functions of recombinant therapeutic antibodies. We investigated the hypothesis that IgG Fc glycosylation can be controlled by manipulation of cellular nucleotide-sugar metabolism. In control cultures, N-glycans associated with the Fc domain of a recombinant humanized IgG1 produced by GS-NS0 cells in culture were predominantly biantennary, variably beta-galactosylated (average 0.3 mol galactose complex N-glycan(-1)) structures with no bisecting N-acetylglucosamine residues, sialylation, or alpha1,3-linked galactosylation evident. However, a variable proportion (5% to 15%) of high-mannose (Man5 to Man9) oligosaccharides were present. To manipulate the cellular content of the nucleotide sugar precursor required for galactosylation, UDP-Gal, we included either 10 mM glucosamine or 10 mM galactose in the culture medium. In the case of the former, a 17-fold increase in cellular UDP-N-acetylhexosamine content was observed, with a concomitant reduction (33%) in total UDP-hexose, although the ratio of UDP-Glc:UDP-Gal (4:1) was unchanged. Associated with these alterations in cellular UDP-sugar content was a significant reduction (57%) in the galactosylation of Fc-derived oligosaccharides. The proportion of high-mannose-type N-glycans (specifically Man5, the substrate for N-acetylglucosaminyltransferase I) at Asn(297) was unaffected. In contrast, inclusion of 10 mM galactose in culture specifically stimulated UDP-Gal content almost five-fold. However, this resulted in only a minimal, insignificant increase (6%) in beta1,4-galactosylation of Fc N-glycans. Sialylation was not improved upon the addition of the CMP-sialic acid (CMP-SA) precursor N-acetylmannosamine (20 mM), even with an associated 44-fold increase in cellular CMP-SA content. Analysis of recombinant IgG1 Fc glycosylation during batch culture showed that beta1,4-linked galactosylation declined slightly during culture, although, in the latter stages of culture, the release of proteases and glycosidases by lysed cells were likely to have contributed to the more dramatic drop in galactosylation. These data demonstrate: (i) the effect of steric hindrance on Fc N-glycan processing; (ii) the extent to which alterations in cellular nucleotide-sugar content may affect Fc N-glycan processing; and (iii) the potential for direct metabolic control of Fc N-glycosylation.

Amidohydrolases↗

Significance of location of enzymes on their release during microbial cell disruption.

The release kinetics of the enzyme invertase and alcohol dehydrogenase from yeast and penicillin acylase from E. coli during disruption using various techniques has been investigated. The disruption techniques used were sonication, high-pressure homogenization, and hydrodynamic cavitation. The first-order-release kinetics was applied for the determination of release rate of these enzymes and total soluble proteins. Location factor (LF) values were calculated using these release rates. The location of the enzymes as given by the values of location factor coincided well with those reported in the literature. Varying values of location factor for the same enzyme by different disruption techniques gave some indications about the selectivity of release of a target enzyme by different disruption techniques. Varying values of location factor for the same enzyme with the use of a particular equipment or disruption technique at different conditions reveals the degree to which the cell is disrupted. Few plausible applications of this location factor concept have been predicted and these speculations have been examined. This location factor concept has been used for monitoring the heat-induced translocation of ADH and location of penicillin acylase during the growth period of E. coli cells.

Alcohol Dehydrogenase↗

A novel enzyme reactor using gluten membrane entrapping cell-associated enzyme.

A membrane enzyme reactor consisting of variable pieces of replaceable cell-immobilized membranes was proposed for the continuous production of bioproducts. To demonstrate the characteristics of the reactor, cell-immobilized membranes were prepared by the entrapment of permeabilized recombinant Escherichia coli cells containing penicillin G acylase within the gluten matrices. A stainless-steel net that was created with a mesh frame was used to support each gluten membrane so that the membranes could be filled into the rectangular-shaped reactor. The reactor equipped with either six or 12 pieces of cell-immobilized gluten membranes containing a biomass concentration of 5%, w/w was effective in catalyzing the production of 6-aminopenicillanic acid from penicillin G. In comparison with intact cells, the cell-immobilized preparation was more stable and the half-life time of the immobilized cell-associate enzyme in gluten membrane was estimated to be 36 days by a long-term operation. As the substrate solution was forced to flow through the reactor equipped with six membranes and in the direction perpendicular to the membranes, the pressure drop was determined to be less than 50 cm H(2)O with a flow-rate up to 50 mL/min. This low pressure due to the porous structure of gluten membrane would lead to a lower operational cost. Increasing either the number of membranes or the area of each cell-immobilized membrane can easily do scaling-up of this membrane reactor.

Anti-Bacterial Agents↗

Evaluation of the performance of immobilized penicillin G acylase using active-site titration.

Penicillin G acylase from Escherichia coli was immobilized on Eupergit C with different enzyme loading. The activity of the immobilized preparations was assayed in the hydrolysis of penicillin G and was found to be much lower than would be expected on the basis of the residual enzyme activity in the immobilization supernatant. Active-site titration demonstrated that the immobilized enzyme molecules on average had turnover rates much lower than that of the dissolved enzyme. This was attributed to diffusion limitations of substrate and product inhibition. Indeed, when the immobilized preparations were crushed, the activity increased from 587 U g-1 to up to 974 U g-1. The immobilized preparations exhibited up to 15% lower turnover rates than the dissolved enzyme in cephalexin synthesis from 7-ADCA and D-(-)-phenylglycine amide. The synthesis over hydrolysis ratios of the immobilized preparations were also much lower than that of the dissolved enzyme. This was partly due to diffusion limitations but also to an intrinsic property of the immobilized enzyme because the synthesis over hydrolysis ratio of the crushed preparations was much lower than that of the dissolved enzyme.

Antigens, Neoplasm↗

Penicillin acylase-catalyzed ampicillin synthesis using a pH gradient: a new approach to optimization.

The penicillin acylase-catalyzed synthesis of ampicillin by acyl transfer from D-(-)-phenylglycine amide (D-PGA) to 6-aminopenicillanic acid (6-APA) becomes more effective when a judiciously chosen pH gradient is applied in the course of the process. This reaction concept is based on two experimental observations: 1) The ratio of the initial synthesis and hydrolysis rates (V(S)/V(H)) is pH-dependent and exhibits a maximum at pH 6.5-7.0 for a saturated solution of 6-APA; 2) at a fixed 6-APA concentration below saturation, V(S)/V(H) increases with decreasing pH. Optimum synthetic efficiency could, therefore, be achieved by starting with a concentrated 6-APA solution at pH 7 and gradually decreasing the pH to 6.3 in the course of 6-APA consumption. A conversion of 96% of 6-APA and 71% of D-PGA into ampicillin was accomplished in an optimized procedure, which significantly exceeds the efficiency of enzymatic synthesis performed at a constant pH of either 7.0 or 6.3.

Ampicillin↗

Equilibrium modeling of extractive enzymatic hydrolysis of penicillin G with concomitant 6-aminopenicillanic acid crystallization.

In the present downstream processing of penicillin G, penicillin G is extracted from the fermentation broth with an organic solvent and purified as a potassium salt via a number of back-extraction and crystallization steps. After purification, penicillin G is hydrolyzed to 6-aminopenicillanic acid, a precursor for many semisynthetic beta-lactam antibiotics. We are studying a reduction in the number of pH shifts involved and hence a large reduction in the waste salt production. To this end, the organic penicillin G extract is directly to be added to an aqueous immobilized enzyme suspension reactor and hydrolyzed by extractive catalysis. We found that this conversion can exceed 90% because crystallization of 6-aminopenicillanic acid shifts the equilibrium to the product side. A model was developed for predicting the equilibrium conversion in batch systems containing both a water and a butyl acetate phase, with either potassium or D-p-hydroxyphenylglycine methyl ester as counter-ion of penicillin G. The model incorporates the partitioning equilibrium of the reactants, the enzymatic reaction equilibrium, and the crystallization equilibrium of 6-aminopenicillanic acid. The model predicted the equilibrium conversion of Pen G quite reasonably for different values of pH, initial penicillin G concentration and phase volume ratio. The model can be used as a tool for optimizing the enzymatic hydrolysis.

Acetates↗

A two-step, one-pot enzymatic synthesis of cephalexin from D-phenylglycine nitrile.

A cascade of two enzymatic transformations is employed in a one-pot synthesis of cephalexin. The nitrile hydratase (from R. rhodochrous MAWE)-catalyzed hydration of D-phenylglycine nitrile to the corresponding amide was combined with the penicillin G acylase (penicillin amidohydrolase, E.C. 3.5.1.11)-catalyzed acylation of 7-ADCA with the in situ-formed amide to afford a two-step, one-pot synthesis of cephalexin. D-Phenylglycine nitrile appeared to have a remarkable selective inhibitory effect on the penicillin G acylase, resulting in a threefold increase in the synthesis/hydrolysis (S/H) ratio. 1,5-Dihydroxynaphthalene, when added to the reaction mixture, cocrystallized with cephalexin. The resulting low cephalexin concentration prevented its chemical as well as enzymatic degradation; cephalexin was obtained at 79% yield with an S/H ratio of 7.7.

Acetonitriles↗

Active site titration as a tool for the evaluation of immobilization procedures of penicillin acylase.

Native and immobilized preparations of penicillin acylase from Escherichia coli and Alcaligenes faecalis were studied using an active site titration technique. Knowledge of the number of active sites allowed the calculation of the average turnover rate of the enzyme in the various preparations and allowed us to quantify the contribution of irreversible inactivation of the enzyme to the loss of catalytic activity during the immobilization procedure. In most cases a loss of active sites as well as a decrease of catalytic activity per active site (turnover rate) was observed upon immobilization. Immobilization techniques affected the enzymes differently. The effect of increased loading of penicillin acylase on the average turnover rate was determined by active site titration to assess diffusion limitations in the carrier.

Alcaligenes↗

Advantages of using non-isothermal bioreactors for the enzymatic synthesis of antibiotics: the penicillin G acylase as enzyme model.

A new hydrophobic and catalytic membrane was prepared by immobilizing Penicillin G acylase (PGA, EC.3.5.1.11) from E. coli on a nylon membrane, chemically grafted with butylmethacrylate (BMA). Hexamethylenediamine (HMDA) and glutaraldehyde (Glu) were used as a spacer and coupling agent, respectively. PGA was used for the enzymatic synthesis of cephalexin, using D(-)-phenylglycine methyl ester (PGME) and 7-amino-3-deacetoxycephalosporanic acid (7-ADCA) as substrates. Several factors affecting this reaction, such as pH, temperature, and concentrations of substrates were investigated. The results indicated good enzyme-binding efficiency of the pre-treated membrane, and an increased stability of the immobilized PGA towards pH and temperature. Calculation of the activation energies showed that cephalexin production by the immobilized biocatalyst was limited by diffusion, resulting in a decrease of enzyme activity and substrate affinity. Temperature gradients were employed as a way to reduce the effects of diffusion limitation. Cephalexin was found to linearly increase with the applied temperature gradient. A temperature difference of about 3 degrees C across the catalytic membrane resulted into a cephalexin synthesis increase of 100% with a 50% reduction of the production times. The advantage of using non-isothermal bioreactors in biotechnological processes, including pharmaceutical applications, is also discussed.

Anti-Bacterial Agents↗

Integrated reactor concepts for the enzymatic kinetic synthesis of cephalexin.

Integrated process concepts for enzymatic cephalexin synthesis were investigated by our group, and this article focuses on the integration of reactions and product removal during the reactions. The last step in cephalexin production is the enzymatic kinetic coupling of activated phenylglycine (phenylglycine amide or phenylglycine methyl ester) and 7-aminodeacetoxycephalosporanic acid (7-ADCA). The traditional production of 7-ADCA takes place via a chemical ring expansion step and an enzymatic hydrolysis step starting from penicillin G. However, 7-ADCA can also be produced by the enzymatic hydrolysis of adipyl-7-ADCA. In this work, this reaction was combined with the enzymatic synthesis reaction and performed simultaneously (i.e., one-pot synthesis). Furthermore, in situ product removal by adsorption and complexation were investigated as means of preventing enzymatic hydrolysis of cephalexin. We found that adipyl-7-ADCA hydrolysis and cephalexin synthesis could be performed simultaneously. The maximum yield on conversion (reaction) of the combined process was very similar to the yield of the separate processes performed under the same reaction conditions with the enzyme concentrations adjusted correctly. This implied that the number of reaction steps in the cephalexin process could be reduced significantly. The removal of cephalexin by adsorption was not specific enough to be applied in situ. The adsorbents also bound the substrates and therewith caused lower yields. Complexation with beta-naphthol proved to be an effective removal technique; however, it also showed a drawback in that the activity of the cephalexin-synthesizing enzyme was influenced negatively. Complexation with beta-naphthol rendered a 50% higher cephalexin yield and considerably less byproduct formation (reduction of 40%) as compared to cephalexin synthesis only. If adipyl-7-ADCA hydrolysis and cephalexin synthesis were performed simultaneously and in combination with complexation with beta-naphthol, higher cephalexin concentrations also were found. In conclusion, a highly integrated process (two reactions simultaneously combined with in situ product removal) was shown possible, although further optimization is necessary.

Adsorption↗