Reaction engineering aspects of activated sugar production. CMP-Neu5Ac as an example.
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Biomedical subjects
Publications and source records attributed to C Wandrey.
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beta-1,4-Galactosyltransferase (Gal-T, EC 2.4.1.38) transfers galactose (Gal) from UDP-Gal to N-acetyl-D-glucosamine or a derivative GlcNAc-R. Soluble Gal-T, purified from human breast milk, was shown to be very heterogeneous by isoelectric focusing (IEF). In order to produce sufficient homogeneous enzyme for three-dimensional analysis, the human enzyme (hGal-T) has been expressed in Saccharomyces cerevisiae, production scaled up to 187 U recombinant Gal-T (rGal-T) and purified. The purification protocol was based on chromatography on concanavalin-A-Sepharose followed by affinity chromatographies on GlcNAc-Sepharose and alpha-lactalbumin-Sepharose. Analysis by SDS/PAGE revealed hyperglycosylation at the single N-glycosylation site, preventing recognition by antibodies. Analysis by IEF revealed considerable heterogeneity of rGal-T. The N-glycan could be removed by treatment with endoglycosidase H (endo H). The N-deglycosylated form of rGal-T retained full activity and showed only three isoforms by IEF analysis. Then we abolished the single N-glycosylation consensus sequence by site-directed mutagenesis changing Asn69-->Asp. The soluble mutated enzyme (N-deglycosylated rGal-T) was expressed in S. cerevisiae and its production scaled up to 60 U.N-deglycosylated rGal-T was purified to electrophoretic homogeneity. When analyzed by IEF, N-deglycosylated rGal-T was resolved in two bands. The O-glycans could be removed by jack bean alpha-mannosidase treatment and the completely deglycosylated Gal-T appeared homogeneous by IEF. The kinetic parameters of N-deglycosylated rGal-T were shown not to differ to any significant extent from those of the hGal-T. No significant changes in CD spectra were observed between hGal-T and N-deglycosylated rGal-T. Light-scattering analysis revealed dimerization of both enzymes. These data indicate that N-deglycosylated rGal-T was correctly folded, homogeneous and thus suitable for crystallization experiments.
On-line analysis of one component in a complex media used for bioprocesses requires the application of selective tests such as enzymes assays. Because these assays are susceptible to interference by other medium components and have a limited detection range, automatic sample pretreatment is a prerequisite. The progress made with automatic sample pretreatment in flow-injection analysis makes this technique particularly suitable for on-line monitoring of bioprocesses. Moreover, newly developed software control systems may improve the necessary robustness of flow-infection analysis systems.
An immobilized hybridoma cell line was cultivated at controlled glucose and glutamine concentrations. On-line analysis of the substrates was carried out with a multi-channel flow injection analysis system. The analysis system also determined on-line the lactate and ammonium concentration. The substrate concentrations were controlled using an adaptive-control strategy. This strategy consisted of the estimation of the real-time concentrations and volumetric substrate consumption rates by an Extended Kalman Filter, and a minimum variance controller, which used the estimated parameters to set the feed rates of the substrates. The closed-loop control was used to start-up two cultures with either glucose or glutamine as control-substrate for the medium feed rate. The controller kept the concentration of the control-substrate constant by enhancing the medium feed rate simultaneously to the increasing volumetric consumption rate of the substrate. When glutamine was used as control-substrate, the glucose concentration remained relatively constant, whereas the glutamine concentration decreased during the start-up at a constant glucose concentration. This indicates that glutamine is consumed faster than glucose and will be a better control-substrate to avoid limitation during the start-up of a culture with the applied hybridoma cell line. During the colonization of the microcarriers, the yield of ammonium on glutamine decreased from 0.80 to 0.55 (mol mol-1), indicating a change in the glutamine metabolism. The yield of lactate on glucose stayed constant for both experiments. During long-term culture of more than 800 h, the controller kept both the glucose and glutamine concentrations constant at perfusion rates between 0.50 h-1 and 0.15 h-1. The medium, glucose and glutamine feed rate were independently controlled. Both the specific glutamine and glucose consumption rates remained constant for all perfusion rates, which was probably as a result of the constant concentrations. The specific monoclonal antibody production rate decreased with the perfusion rate decreasing from 0.40 h-1 to 0.20 h-1. The immobilized-cell concentration decreased only at the lowest perfusion rate. Both effects could not be explained directly by the increasing ammonium and lactate concentrations nor by the decreasing amino-acid concentrations.
Expression of recombinant full length human alpha 2,6(N)sialyltransferase has been scaled-up in S. cerevisiae in a 150-l bioreactor yielding 47 U at a concentration of 0.31 U/l. The protein specific activity as measured in reconstituted yeast lyophilisate was 0.8 mU/mg protein. The recombinant enzyme exhibited similar Michaelis constants as previously determined for the native rat enzyme. By immunoblotting the enzyme was shown to be heterogeneous by size (44-48 kD) and N-glycosylated. We conclude that recombinant alpha 2,6(N)sialyltransferase expressed in S. cerevisiae is retained in the endoplasmic reticulum as a fully active enzyme.
We report in this communication the first large-scale heterologous expression of a glycosyltransferase in yeast. A soluble form of a human beta-1,4-galactosyltransferase (EC 2.4.1.38) was expressed using a Saccharomyces cerevisiae expression system. Fermentation technology afforded the means to increase the expression level of the beta-1,4-galactosyltransferase up to a concentration of 700 mU/liter. The enzyme was produced at a scale of 200 units. The recombinant soluble enzyme was purified 766-fold to a specific activity of approx. 2 U/mg using a purification protocol based on sequential affinity chromatography on N-acetylglucosaminyl- and alpha-lactalbumin-Sepharose, respectively. This study demonstrates that heterologous expression of a glycosyltransferase is possible on a large scale and offers an alternative to natural sources like human breast milk or bovine colostrum.
In an optimized sorbitol/yeast extract/mineral salt medium up to 12 U/l CMP-N-acetyl-neuraminic-acid (Neu5Ac) synthetase was produced by Escherichia coli K-235 in shake-flask culture. A colony mutant of this strain, E. coli K-235/CS1, was isolated with improved enzyme formation: in shake flasks with a yield of up to 20.8 U/l and 54 mU/mg protein in the cell extract. With this strain 26500 U CMP-Neu5Ac synthetase was produced with a high specific activity (0.128 U/mg) by fed-batch fermentation on 230-l scale. On a 10-1 scale the enzyme yield was 191 U/l culture medium. The enzyme was partially purified by precipitation with polyethyleneglycol resulting in a three- to fourfold enrichment and a recovery rate of more than 80%; most of the CTP hydrolysing enzymes were removed. The native synthetase was deactivated completely by incubation at 45 degrees C for 10 min, but could be stabilized remarkably by glycerol and different salts. The enzyme was used for the preparative synthesis of CMP-Neu5Ac with a conversion yield of 87% based on CTP.
A multi-channel flow injection analysis system was used for on-line monitoring of a continuous animal cell culture with high cell density. With this system, the glucose, lactate and glutamine concentration were determined using immobilized dehydrogenases, ammonium using an aqueous o-phthaldialdehyde solution. Glutamine concentration was determined on the basis of the difference between a glutamine and a glutamate measurement. To prevent disturbance of the measurement and pollution of the system, the analytes in the sample were separated from high molecular compounds by on-line dialysis. On-line gas dialysis was used to avoid interference of other amino groups with the ammonium determination. In addition, dialysis was used as a dilution step. The measurement time for all four components was 42 min. This time included a final washing period after the analysis cycle. The system was calibrated once a day. Two continuous cultivations of a hybridoma cell line immobilized in open-porous glass carriers were monitored, using a fluidized bed reactor as cultivation system. The concentration of glutamine, glucose and ammonium determined with the on-line FIA system were in good agreement with the off-line data determined once a day. Only the lactate data showed some deviation. The immobilized enzyme reactors could be used for up to 3000-5000 injections. During the first cultivation, lasting 200 h, the start up period of the reactor was monitored. The on-line measurements described much better the time-course of the concentrations than the off-line data. It was possible to estimate the growth rate of the cells in the micro-carriers by the on-line data. In the course of the second cultivation, which lasted almost 1000 h, the influence of the dissolved oxygen concentration on the cell metabolism was monitored. It was noted that a sudden change of the glutamine concentration in the feed caused a fast change of the consumption and production rate of the measured metabolites.
Sequences coding for the cytoplasmic and transmembrane domains were removed from the cDNA of the human Golgi resident membrane protein beta 1,4 galactosyltransferase (gal-T). The remaining sequences coding for the stem and catalytical domains of this glycosyltransferase were fused to sequences coding for the yeast invertase signal sequence. The hybrid was inserted together with a constitutive yeast promoter and a terminator into a E. coli/yeast shuttle vector. Saccharomyces cerevisiae strain BT150 transformed with this new expression vector expressed enzymically active soluble enzyme, whereas no activity was detectable in mock-transformed yeasts. The enzyme product was identified by HPLC analysis and shown to correspond to the expected product N-acetyllactosamine.
To elucidate the adsorption characteristics of lipases and to study the influence of the reaction conditions on the catalytic properties of lipases, the hydrolysis of decylchloroacetate by Pseudomonas fluorescens lipase in an emulsion reactor was studied as a model system. During the reaction the droplet size distribution of the emulsion was measured on-line using a particle sizer based on light scattering. Desorption experiments revealed that, at low surface coverage, the initial rate of reaction was not influenced by either the stirring speed or the organic volume fraction. Dilution of the reaction mixture during hydrolysis did not result in a decrease in activity. Based on these results, it is assumed that under the specified conditions adsorption of Pseudomonas fluorescens lipase is quantitative and probably irreversible. Based on activity measurements and assuming that only a monolayer of lipase is active, it is calculated that at saturation the emulsion interface is covered with 3 mg lipase per m2. From these data the average interfacial area covered by one lipase molecule at saturation was calculated to be 1700-2100 A2 per molecule. The emulsion was shown to be dynamic, e.g., during hydrolysis a significant increase in interfacial area was observed as a result of a shift in droplet size distribution to smaller diameters. Experiments indicated that both the formation of decanol and the emulgating effect of the lipase account for these observations. The formation of decanol also resulted in a dramatic decrease in hydrolytic activity. Taking interfacial tension measurements into account, it is shown that decanol accumulates at the liquid-liquid interface.(ABSTRACT TRUNCATED AT 250 WORDS)
In the study presented here a laboratory scale (150 ml) fluidized bed bioreactor was used as a tool for making kinetic measurements on the production of monoclonal antibodies (MAb) with a hybridoma cell line. We determined the influence of dissolved oxygen tension (DOT) on the metabolic activity of a hybridoma population immobilized in macroporous collagen microspheres. The data obtained showed a reduction of the metabolic activity of the immobilized population at reduced DOT, the total number of immobilized cells, however, remained constant. At decreasing DOT an increasing lactate yield from glucose at reduced glutamine consumption was noticed, indicating a shift in the pattern of substrate usage. A mathematical description of maintenance metabolism was formulated and the parameters of growth and maintenance requirements were calculated. A growth associated MAb production was determined under the conditions applied leading to space time yields of 225 mg MAb per liter of total reactor volume and day.
We recently reported the isolation and some properties of an unusual enzyme called peptide amidase (Steinke, D. and Kula, M. R. Angew. Chem. Int. Ed. Engl. 1990, 29, 1139-1140). Here we describe the partial purification of the enzyme from the flavedo of orange fruits and discuss results of a detailed study of the substrate range of the peptide amidase, which is extremely wide and useful for a C-terminal enzymatic deprotection in peptide synthesis under very mild conditions. The substrate spectrum includes protected or unprotected peptide amides and N-protected amino acid amides. The chain length of the substrate peptide amide, as well as the amino acid composition, including the C-terminal amino acid side chain, are of minor importance. The peptide amidase is stereoselective with regard to the C-terminal position, since only L-amino acid amides are accepted as substrates, with the exception of proline. Notably, side chain amides are not deamidated. The peptide amidase is free of any proteolytic activity, which would hydrolyze internal peptide bonds of substrate peptides. In the penultimate position D-amino acids are tolerated; peptide modifications toward the N-terminal region do not abolish the enzymatic deamidation at the C-terminus.
The method of measuring enzyme deactivation by monitoring necessary addition of fresh enzyme to keep a constant degree of conversion in a CSTR at constant [E] x tau, the product of concentration of active enzyme [E] and residence time tau, was successfully applied to acylase I from porcine kidney and Aspergillus oryzae fungus. Fungal enzyme was found to be more stable than kidney enzyme. Activation by both Co2+ and Zn2+ ions also yielded increased operational enzyme stability: Co2+ and Zn2+ are better stabilizers than activators. Mg2+ and Ca2+ are found to be neither activators nor stabilizers. Fungal acylase partially deactivated by exposition to a metal-free medium in the CSTR was reactivated by addition of Zn2+, demonstrating that loss of Zn2+ from the enzyme molecule is mainly responsible for deactivation in a continuous reactor.
Using Escherichia coli K-235 as a production strain in a fed-batch fermentation process with an optimized sorbitol/yeast extract medium, we were able to produce 640 U of CMP-Neu5Ac synthetase in 10 l scale (64 U/l) and 9200 U (total enzyme) in 200 l scale (390 U/kg wet weight). By simple one-step purification procedures, enzyme preparations were obtained that could be used efficiently for the synthesis of CMP-Neu5Ac from CTP and Neu5Ac with over 90% yield, from Neu5Ac, CMP, and ATP or phosphoenolpyruvate by in situ generation of CTP, and from CTP, pyruvate, and ManNAc or GlcNAc by in situ generation of Neu5Ac.
Carboxypeptidase c partially purified from orange leaves was studied as a catalyst for enzymatic peptide synthesis. Various N-protected ester- and nucleophile compounds were evaluated in order to determine the substrate specificity. For further characterization of the synthetic reaction, optimum pH and the influence of the N-terminal protecting group were studied. Kinetic investigations revealed considerable differences in Km and Vmax for the nucleophile when the N-terminal protecting group of the substrate was varied.
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Several amino acid derivatives with the negatively charged N alpha-protecting groups Maleyl (Mal) and Citraconyl (Cit) were synthesized and used in enzyme-catalyzed peptide synthesis. Compared to commonly used alpha-amino protecting groups in chemical peptide synthesis (Z, Fmoc, Boc, etc.), these charged protecting groups strongly increase both water solubility of different aromatic amino acid derivatives and activities of synthesis reactions. As a consequence of the solubilizing effect, we used these groups in the kinetically controlled peptide synthesis choosing kyotorphin (tyrosyl-arginine) as a model peptide. With Mal-Tyr-OEt as substrate and Arg-OEt as nucleophile, we succeeded in the alpha-chymotrypsin-catalyzed production of about 12 kg of Tyr-Arg (50.4% overall yield) in a 300 l batch experiment.
The production of D-ribulose-5-phosphate in an enzyme membrane reactor was examined. Phosphoryl transfer from ATP to D-ribulose was catalysed by D-ribulokinase isolated from Klebsiella pneumoniae. For production of D-ribulose-5-phosphate the phosphoryl donor ATP was used either in stoichiometric or in catalytic amounts. Using catalytic amounts of ATP requires a second enzyme, e.g. pyruvate kinase, to regenerate ATP. The kinetic parameters for D-ribulokinase and pyruvate kinase were determined to calculate the performance of an enzyme membrane reactor for continuous production of D-ribulose-5-phosphate. Both processes operated for more than 200 h. Regardless of whether ATP was used in catalytic or stoichiometric amounts, about the same production parameters were determined. In continuous production space/time yields of 117 g (with ATP regeneration) and 103 g (without ATP regeneration) of D-ribulose-5-phosphate l -1 per day were reached.