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The partitioning of a variety of extracellular lipases, both pro‐ and eucaryotic, in detergent‐based aqueous two‐phase systems was examined. The results revealed that all procaryotic lipases showed a clear preference for the detergent‐rich coacervate phase. In contrast, all eucaryotic lipases were significantly excluded from this phase, most probably caused by their glycosylation. The potential of such detergent‐based systems for the isolation of extracellular lipases directly from cell‐free culture broth was analyzed using the bacterium Pseudomonas cepacia (DSM 50181). This strain was identified after a limited screening for lipase activity. About 76% of the lipase could be extracted into the coacervate phase in just one purification step, leading to a four‐fold concentration of lipase and a purification factor of 24. [ABSTRACT FROM AUTHOR]

Future developments in gene therapy and DNA vaccination depend on cost-effective large-scale production of pharmaceutical-grade pDNA (plasmid DNA). Given the large amount of impurities present in the feedstock, purification processes that have high specificity and capacity at a moderate cost are required. In the present study, we describe a non-chromatographic procedure based on aqueous two-phase extraction allowing a fast and simply scalable capture step. PEG [poly(ethylene glycol)] in combination with potassium citrate or potassium phosphate was tested as phase component for extraction. By increasing either PEG or salt concentration, the partitioning of nucleic acids changed from bottom to top phase. Phase systems with a composition of 15% PEG 800 and 20% potassium phosphate at pH 7.0 showed a strong partitioning of pDNA to the bottom phase, linked to a clear decrease in open circular pDNA, while proteins, genomic DNA and RNA remain at the top or at the interphase. A great advantage of the current process is that the complete procedure of lysis, precipitation, clarification and extraction can be performed in a single vessel. The number of denatured and sheared genomic DNAs in a spiking experiment was found to be depleted by more than 99%.

The peptide amidase from Stenotrophomonas maltophilia selectively hydrolyses the C-terminal amide bond in peptide amides. Crystals have been obtained by sitting-drop vapour diffusion from solution containing polyethylene glycol (PEG) 6000, HEPES pH 7.5, glycerine and sodium azide (NaN(3)). The crystals belong to the monoclinic space group P2(1), with unit-cell parameters a = 74.18, b = 62.60, c = 101.91 A, beta = 90 degrees. X-ray data from these crystals diffracted at the European Synchrotron Radiation Facility (ESRF, France) ID14-1 beamline to 1.4 A.

The suitability of ion-selective electrodes (ISE) for the determination of residence time distribution (RTD) in turbid, cell-containing fluids was examined. The electrodes were found to give reproducible signals in biomass-containing feedstock with up to 20% wet weight of solids. The enhanced feedstock compatibility of IES, when compared to other tracer sensing devices, allows the study of expanded bed system hydrodynamics under relevant operating conditions. Within the linear range of the corresponding ISE-tracer pair, both examined ISE (Li(+)- or Br(-)-selective) showed to be insensitive against the range of flow rate and pH normally employed during expanded bed adsorption (EBA) of proteins. Analyzing the RTD obtained after a perfect ion tracer pulse in terms of the PDE model (PDE, axially dispersed plug-flow exchanging mass with stagnant zones) gave a quantitative description of the underlying hydrodynamic situation during EBA processing. These data provided a powerful tool to make predictions on the adsorptive global process performance with a defined feedstock type and composition. The link between the hydrodynamic events during feedstock application and the actual process performance was shown when applying intact yeast cell suspensions at different biomass content (up to 7.5% wet weight) and buffer conductivity (5-12 mS) onto an EBA column filled with the adsorbent Streamline Q XL as fluidized phase. On the basis of our experimental results, a guideline for the successful application of the ISE/RTD method to EBA process design is presented.

Peptide amidase-catalysed amidations of the C- terminal carboxylic group of peptides were studied using model substrates of a large series of N(alpha)-protected di-, tri-, tetra- and penta-peptides in the presence of NH4HCO3 as the ammonium source. The maximal yields of amide syntheses were achieved in a medium consisting of acetonitrile with 20-25 vol% of dimethylformamide and 3 vol% of water. Under these conditions, the substrate specificity of the enzyme was more restricted in the synthetic reaction than was found for the amide hydrolysis. Elongation of the peptide chain had a negative effect on enzymic amidation. Thus the direct amidation of N(alpha)-t-butoxycarbonyl-protected Leu-enkephalin resulted in a low yield of protected enkephalin amide.

The purification of human chymotrypsinogen B (hCTRB) after expression and secretion by the yeast Pichia pastoris is described based on two different approaches using integrated initial recovery. Extraction employing aqueous two-phase systems (ATPS) from poly(ethylene glycol) and sodium sulfate allows direct processing of cell containing yeast suspensions of 50% wet weight. The target protein is obtained partially purified in the top phase while cells and cell debris are partitioned to the bottom phase of the system. hCTRB is further purified by adsorption from the top phase to the cation exchanger SP Sepharose Big Beads and elution in a salt step. The single step isolation of hCTRB is possible by expanded bed adsorption (EBA) using a fluidized cation exchanger (Streamline SP XL). A design strategy is shown taking both target protein binding and stable fluidization of the stationary phase in cell containing suspensions into consideration. For the example of hCTRB isolation from cell containing P. pastoris suspensions, a successful use of this strategy is demonstrated. Both initial recovery strategies deliver a product that can be further purified and formulated by ultrafiltration/diafiltration followed by lyophilization, resulting in a homogeneous product. Scale-up to 30-90 L of culture suspension was shown for both methods, resulting in a product of similar quality. Comparing both strategies reveals that the two-step ATPS route is better suited for high cell density cultures, while the single step EBA method is preferred for cultures of moderate cell density. This is due to the fact that application of EBA is restricted to suspensions of 10-12.5% wet weight cell concentration, thus necessitating dilution of the original broth prior to sample application. The data presented show that integrated recovery operations are a valuable alternative to traditional processing for systems that are problematic during initial solid-liquid separation.

During recombinant Escherichia coli fermentation with high expression levels, inclusion bodies are often formed. Aqueous two-phase systems have been used in the presence of urea for the initial recovery steps. To investigate phase behavior of such systems we determined phase diagrams of poly(ethylene glycol) (PEG)/sodium sulfate/urea/water and PEG/dextran T-500 (DEX)/urea/phosphate buffer/water at different concentrations of urea and different molecular weight of PEG. PEG/Na2SO4 aqueous two-phase systems could be obtained including up to 30% w/w urea at 25 degrees C and PEG/dextran T-500 up to 35% w/w urea. The binodial was displaced toward higher concentrations with increasing urea concentrations. The partition coefficient of urea was near unity. An unstable mutant of T4-lysozyme with an amino acid replacement in the core (V149T) was used to analyze the effect of phase components on the conformation of the enzyme. We showed that partitioning of tryptophan was not dependent on the concentration of urea in the phase system.

SDS/gel capillary electrophoresis (SDS/gel CE) and matrix-assisted laser desorption ionization-time-of-flight MS (MALDI-TOF-MS) were employed to analyse changes in the culture broth during batch and continuous cultivation of hybridoma cells. The stability of IgG was analysed by SDS/gel CE and capillary zone electrophoresis (CZE). The results obtained by the new analytical procedures reflect the changes in the cultivation conditions very well, indicating that these tools can be used to follow animal cell culture processes. A new technique to collect fractions of very small volumes during the CZE separation is described, and the successful off-line coupling of CZE and MALDI-TOF-MS for the analysis of biotechnological processes is demonstrated.

The application of a chemiluminometric method for the on-line monitoring of a hybridoma cell culture is described. Enzyme sensors for glucose, lactate, glutamine, glutamate and ammonia, based on oxidase-catalysed reactions, were developed and connected to a flow-injection-analysis (f.i.a.) biosensor. H2O2 produced by the oxidase-catalysed enzyme reaction was detected by luminol chemiluminescence with a fibre-optic H2O2 biosensor. The system has been used to monitor animal cell cultures. A continuous hybridoma cell cultivation for the production of monoclonal antibodies is presented as an example. It was possible to monitor the bioprocess over a period of 15 days. A complete analysis of all five components could be performed within 42 min. The enzyme sensors were stable during the whole cultivation time without significant loss of activity. The computer-controlled biosensor f.i.a. works with good reliability. The precision for all five components ranged between 2.2 and 4.5%. It was possible to determine glutamine in one step using an anti-interference enzyme reactor. Endogenous glutamate was completely removed up to a level of 0.5 mM.

The purification of (R)-oxynitrilase (EC 4.1.2.10) from Linum usitatissimum (flax) has been improved considerably. The enzyme is obtained from seedlings in 60% yield by fractional salt precipitation followed by ion-exchange and hydrophobic-interaction chromatography. Final gel-permeation chromatography yields a protein with a specific activity of 53 units/mg at pH 4.1. The N-terminal sequence is reported and microheterogeneity demonstrated. The substrate range was investigated using (R)-oxynitrilase immobilized on Eupergit and t-butyl methyl ether as solvent. The addition of HCN to various aliphatic ketones and aldehydes is catalysed by the enzyme, while aromatic ketones are not converted. (R)-Butan-2-one cyanohydrin was synthesized on a preparative scale and the product characterized.

Pyruvate decarboxylase (E.C. 4.1.1.1), the key enzyme in the glycolytic pathway to ethanol, was isolated in gram amounts from Zymomonas mobilis for structural studies. The primary structure was determined by automated Edman degradation and compared with that deduced from the DNA sequence of the structural gene, previously published by two groups (A. D. Neale, R. K. Scopes, R. E. H. Wettenhall, and N. J. Hoogenraad, 1987, Nucleic Acids Res. 15, 1753-1761; M. Reynen, and H. Sahm, 1988, J. Bacteriol. 170, 3310-3313). The peptide data differ from the published DNA sequences, which also deviate from each other. Crystals diffracting to about 0.3 nm resolution have been obtained by the hanging drop vapor diffusion method. The space group was identified as P4(1)22 or its enantiomorphs containing presumably one tetramer per asymmetric unit.

An optimized coupled enzyme assay for UDP-glucose pyrophosphorylase (EC 2.7.7.9) using UDP-glucose dehydrogenase (EC 1.1.1.22) is presented. This optimized assay was developed by a detailed investigation of the kinetics of the UDP-glucose dehydrogenase reaction. In addition the data provide a basis for the enzymatic synthesis of UDP-glucuronic acid. The results demonstrate that the two binding sites of the dehydrogenase differ since a different modulation of the enzyme activity and stability is observed after preincubation with UDP-glucose or NAD+ at various pH values. This is of general interest for the preparation of assay mixtures where UDP-glucose dehydrogenase is used as an auxiliary enzyme.

Polyethylene glycol (PEG)-oxirane was synthesized by reacting aminated monomethoxy-PEG 5000 (NH2-MPEG 5000) with butanediol diglycidyl ether and used to derivatize bovine serum albumin (BSA) and monoclonal antibodies (mAb) against horseradish peroxidase (HRP) and porcine lactate dehydrogenase isoenzyme 5, respectively. Determination of oxirane end groups revealed a very high number, which arise from the chain breaks of the polymer. Covalent coupling of PEG-oxirane to BSA resulted in 30-50 times higher partition coefficients under optimized conditions. The mAb investigated could be modified with PEG-oxirane while retaining its binding properties and could be used as an affinity ligand for selective extraction of Ag in immunoaffinity partitioning. However, a high degree of modification results in a lower binding constant of mAb anti-HRP and higher [mAb]/[Ag] concentration ratios in immunoaffinity partition experiments.

Microorganisms are a source of protein with catalytic and/or biological activity, which are of increasing commercial interest for applications in industry or therapy. For the isolation of intracellular products cell disruption is necessary. In principle, chemical, biological, or physical means may be employed to release proteins from cells. These different approaches are reviewed with special emphasis on scale-up and possible industrial operation. Mechanical devices have been improved considerably in recent years and appear most universally suited to cell disintegration. Chemical extraction or enzymatic lysis offers improved selectivity but requires individual procedures for each product. For a final process design, product yield and cost of the unit operation must be considered as well as the possible implications for the subsequent steps in product recovery, especially on solid/liquid separation.

Enzyme-catalyzed peptide bond formation requires thorough examination and optimization of each coupling step. In order to identify factors influencing the selectivity between aminolysis and hydrolysis, a systematic study was carried out for the kinetically controlled peptide synthesis. The reaction temperature, the type of C-terminal protecting group, and different organic cosolvents showed little influence on the selectivity. The enzyme, excess nucleophile, pH, N-terminal protecting group, and ionic strength of the solution were identified as major factors controlling the selectivity and, therefore, the yield of the dipeptide synthesis. Under optimized conditions, the selectivity of the chymotrypsin-catalyzed synthesis of PheSer could be increased from 35 to 100%.

Several commercially available enzymes were tested for their ability to hydrolyze amino acid carbamates. No activity was found with pig liver esterase, the hydantoinase from Pseudomonas fluorescens DSM 84, or the urease from jack beans. A stereoselective cleavage of the carbamyl group yielding L-amino acids was observed by acylase and acetylcholinesterases from bovine and human erythrocytes. Racemic mixtures of N-(methoxycarbonyl)-DL-alanine, N-(ethoxycarbonyl)-DL-alanine, and the corresponding valine carbamates are hydrolyzed to L-alanine and L-valine, respectively, by acylases leaving the D-amino acid carbamates unchanged. The lysine carbamates were not hydrolyzed by acylases. In contrast only the methoxycarbonyl amino acids were split by acetylcholinesterases, which, however, also cleave alpha, epsilon-(N-methoxycarbonyl)-DL-lysine stereoselectively at the alpha position, yielding epsilon-N-methoxycarbonyl-L-lysine. The optimum pH for enzymatic activity of hog kidney acylase was 7.5 and a Km value of 8.2 mM for N-(methoxycarbonyl)-DL-alanine was determined. For the acetylcholinesterases the reaction rate reaches an optimum between pH 7.5 and 8. The Km value was 68 mM for N-(methoxycarbonyl)-DL-alanine.

The hydantoinase (EC 3.5.2.2) from Pseudomonas fluorescens strain DSM 84 was purified either by hydrophobic interaction chromatography on phenyl-Sepharose or by salting out chromatography on Sepharose 4B, gel filtration on Sephacryl S-400, and preparative electrophoresis. Molecular weight values of 230,000 and 60,000 for the native enzyme and each of the four subunits were estimated for the hydantoin hydrolysing activity. The hydantoinase was stable at temperatures up to 40 degrees C but showed an optimal activity at 55 degrees C. The enzyme was markedly inhibited by copper, para-hydroxymercuribenzoate, 8-hydroxyquinoline, and 2,2'-dipyridyl but not by zinc, and poorly by EDTA and o-phenanthroline. The hydantoin-hydrolyzing activity could be reactivated by ferrous ions. Dihydrouracil was the most readily hydrolyzed substrate. The dihydropyrimidinase produced by strain DSM 84 could also hydrolyze 5-substituted hydantions such as isopropylhydantoin (valine derivative) continuously for 10 days in a membrane reactor at a conversion rate of 30%. The only identified end product was N-carbamyl-D-valine.

We report a new convenient assay of the activity of gamma-glutamylcysteine synthetase (EC 6.3.2.2) and glutathione synthetase (EC 6.3.2.3) in crude microbial extracts as well as in purified enzyme preparations. The assay is based on the quantitative analysis of the reaction products by high-performance liquid chromatography after derivatization of the thiol group with 5,5'-dithiobis-(2-nitrobenzoic acid) as described by J. Reeve, J. Kuhlenkamp, and N. Kaplowitz [(1980) J. Chromatogr. 194, 424-428]. In addition, the procedure yields information on basal levels of gamma-glutamylcysteine and glutathione in crude microbial extracts. The two enzymes responsible for glutathione biosynthesis can be determined in parallel under the same chromatographic conditions. No prior separation from substrates and by-products is necessary. Product formation is linear with time for at least 30 min between 0.03 and 12 mU for both enzymes. Even in crude extracts 0.2-0.5 nmol of products formed can be detected with certainty. The method was found to be sensitive and highly reproducible.