Martin Siemann-Herzberg

Abstract

Cell-free protein synthesis is a versatile protein production system. Performance of the protein synthesis depends on highly active cytoplasmic extracts. Extracts from E. coli are believed to work best; they are routinely obtained from exponential growing cells, aiming to capture the most active translation system. Here, we report an active cell-free protein synthesis system derived from cells harvested at non-growth, stressed conditions. We found a downshift of ribosomes and proteins. However, a characterization revealed that the stoichiometry of ribosomes and key translation factors was conserved, pointing to a fully intact translation system. This was emphasized by synthesis rates, which were comparable to those of systems obtained from fast-growing cells. Our approach is less laborious than traditional extract preparation methods and multiplies the yield of extract per cultivation. This simplified growth protocol has the potential to attract new entrants to cell-free protein synthesis and to broaden the pool of applications. In this respect, a translation system originating from heat stressed, non-growing E. coli enabled an extension of endogenous transcription units. This was demonstrated by the sigma factor depending activation of parallel transcription. Our cell-free expression platform adds to the existing versatility of cell-free translation systems and presents a tool for cell-free biology.

Abstract

Cell-free (in vitro) protein synthesis (CFPS) systems provide a versatile tool that can be used to investigate different aspects of the transcription-translation machinery by reducing cells to the basic functions of protein formation. Recent improvements in reaction stability and lysate preparation offer the potential to expand the scope of in vitro biosynthesis from a research tool to a multifunctional and versatile platform for protein production and synthetic biology. To date, even the best-performing CFPS systems are drastically slower than in vivo references. Major limitations are imposed by ribosomal activities that progress in an order of magnitude slower on the mRNA template. Owing to the complex nature of the ribosomal machinery, conventional ``trial and error'' experiments only provide little insight into how the desired performance could be improved. By applying a DNA-sequence-oriented mechanistic model, we analyzed the major differences between cell-free in vitro and in vivo protein synthesis. We successfully identified major limiting elements of in vitro translation, namely the supply of ternary complexes consisting of EFTu and tRNA. Additionally, we showed that diluted in vitro systems suffer from reduced ribosome numbers. On the basis of our model, we propose a new experimental design predicting 90\% increased translation rates, which were well achieved in experiments. Furthermore, we identified a shifting control in the translation rate, which is characterized by availability of the ternary complex under in vitro conditions and the initiation of translation in a living cell. Accordingly, the model can successfully be applied to sensitivity analyses and experimental design.

Abstract

Ribosomes are a crucial component of the physiological state of a cell. Therefore, we aimed to monitor ribosome dynamics using a fast and easy fluorescence readout. Using fluorescent-labeled ribosomal proteins, the dynamics of ribosomes during batch cultivation and during nutritional shift conditions was investigated. The fluorescence readout was compared to the cellular rRNA content determined by capillary gel electrophoresis with laser-induced fluorescence detection during exponentially accelerating and decelerating growth. We found a linear correlation between the observed fluorescence and the extracted rRNA content throughout cultivation, demonstrating the applicability of this method. Moreover, the results show that ribosome dynamics, as a result of slowing growth, are accompanied by the passive effect of dilution of preexisting ribosomes, de novo ribosome synthesis and ribosome degradation. In light of the challenging task of deciphering ribosome regulatory mechanisms, our approach of using fluorescence to follow ribosome dynamics will allow more comprehensive studies of biological systems.

Abstract

Aerobic production-scale processes are constrained by the technical limitations of maximum oxygen transfer and heat removal. Consequently, microbial activity is often controlled via limited nutrient feeding to maintain it within technical operability. Here, we present an alternative approach based on a newly engineered Escherichia coli strain. This E. coli HGT (high glucose throughput) strain was engineered by modulating the stringent response regulation program and decreasing the activity of pyruvate dehydrogenase. The strain offers about three-fold higher rates of cell-specific glucose uptake under nitrogen-limitation (0.6 g(Glc) gCDW(-1) h(-1)) compared to that of wild type, with a maximum glucose uptake rate of about 1.8 gGlc gCDW(-1) h(-1) already at a 0.3 h(-1) specific growth rate. The surplus of imported glucose is almost completely available via pyruvate and is used to fuel pyruvate and lactate formation. Thus, E. coli HGT represents a novel chassis as a host for pyruvate-derived products.

Abstract

Cell-free protein synthesis, which mimics the biological protein production system, allows rapid expression of proteins without the need to maintain a viable cell. Nevertheless, cell free protein expression relies on active in vivo translation machinery including ribosomes and translation factors. Here, we examined the integrity of the protein synthesis machinery, namely the functionality of ribosomes, during (i) the cell-free extract preparation and (ii) the performance of in vitro protein synthesis by analyzing crucial components involved in translation. Monitoring the 16S rRNA, 23S rRNA, elongation factors and ribosomal protein Si, we show that processing of a cell-free extract results in no substantial alteration of the translation machinery. Moreover, we reveal that the 16S rRNA is specifically cleaved at helix 44 during in vitro translation reactions, resulting in the removal of the anti-Shine-Dalgarno sequence. These defective ribosomes accumulate in the cell-free system. We demonstrate that the specific cleavage of the 16S rRNA is triggered by the decreased concentrations of Mg2+. In addition, we provide evidence that helix 44 of the 30S ribosomal subunit serves as a point-of-entry for ribosome degradation in Escherichia coli. Our results suggest that Mg2+ homeostasis is fundamental to preserving functional ribosomes in cell-free protein synthesis systems, which is of major importance for cell-free protein synthesis at preparative scale, in order to create highly efficient technical in vitro systems.

Abstract

Bioprocess engineering is a highly interdisciplinary field of study which is strongly benefited by practical courses where students can actively experience the interconnection between biology, engineering, and physical sciences. This work describes a lab course developed for 2nd year undergraduate students of bioprocess engineering and related disciplines, where students are challenged with a real-life bioprocess-engineering application, the production of recombinant protein in a fed-batch process. The lab course was designed to introduce students to the subject of operating and supervising an experiment in a bioreactor, along with the analysis of collected data and a final critical evaluation of the experiment. To provide visual feedback of the experimental outcome, the organism used during class was Escherichia coli which carried a plasmid to recombinantly produce enhanced green fluorescent protein (eGFP) upon induction. This can easily be visualized in both the bioreactor and samples by using ultraviolet light. The lab course is performed with bioreactors of the simplest design, and is therefore highly flexible, robust and easy to reproduce. As part of this work the implementation and framework, the results, the evaluation and assessment of student learning combined with opinion surveys are presented, which provides a basis for instructors intending to implement a similar lab course at their respective institution. (c) 2015 by the International Union of Biochemistry and Molecular Biology, 43(3):189-202, 2015.

Abstract

To smoothen the process of n-butanol formation in Pseudomonas putida KT2440, detailed knowledge of the impact of this organic solvent on cell physiology and regulation is of outmost importance. Here, we conducted a detailed systems biology study to elucidate cellular responses at the metabolic, proteomic, and transcriptional level. Pseudomonas putida KT2440 was cultivated in multiple chemostat fermentations using n-butanol either as sole carbon source or together with glucose. Pseudomonas putida KT2440 revealed maximum growth rates (mu) of 0.3 h(-1) with n-butanol as sole carbon source and of 0.4 h(-1) using equal C-molar amounts of glucose and n-butanol. While C-mole specific substrate consumption and biomass/substrate yields appeared equal at these growth conditions, the cellular physiology was found to be substantially different: adenylate energy charge levels of 0.85 were found when n-butanol served as sole carbon source (similar to glucose as sole carbon source), but were reduced to 0.4 when n-butanol was coconsumed at stable growth conditions. Furthermore, characteristic maintenance parameters changed with increasing n-butanol consumption. C-13 flux analysis revealed that central metabolism was split into a glucose-fueled Entner-Doudoroff/pentose-phosphate pathway and an n-butanol-fueled tricarboxylic acid cycle when both substrates were coconsumed. With the help of transcriptome and proteome analysis, the degradation pathway of n-butanol could be unraveled, thus representing an important basis for rendering P. putida KT2440 from an n-butanol consumer to a producer in future metabolic engineering studies.

Abstract

What defines central carbon metabolism? The classic textbook scheme of central metabolism includes the Embden-Meyerhof-Parnas (EMP) pathway of glycolysis, the pentose phosphate pathway, and the citric acid cycle. The prevalence of this definition of central metabolism is, however, equivocal without experimental validation. We address this issue using a general experimental approach that combines the monitoring of transcriptional and metabolic flux changes between steady states on alternative carbon sources. This approach is investigated by using the model bacterium Pseudomonas putida with glucose, fructose, and benzoate as carbon sources. The catabolic reactions involved in the initial uptake and metabolism of these substrates are expected to show a correlated change in gene expressions and metabolic fluxes. However, there was no correlation for the reactions linking the 12 biomass precursor molecules, indicating a regulation mechanism other than mRNA synthesis for central metabolism. This result substantiates evidence for a (re) definition of central carbon metabolism including all reactions that are bound to tight regulation and transcriptional invariance. Contrary to expectations, the canonical Entner-Doudoroff and EMP pathways sensu stricto are not a part of central carbon metabolism in P. putida, as they are not regulated differently from the aromatic degradation pathway. The regulatory analyses presented here provide leads on a qualitative basis to address the use of alternative carbon sources by deregulation and overexpression at the transcriptional level, while rate improvements in central carbon metabolism require careful adjustment of metabolite concentrations, as regulation resides to a large extent in posttranslational and/or metabolic regulation.

Abstract

Prokaryotic production systems have been widely used to manufacture recombinant therapeutic proteins. Economically, the prokaryotic production - especially of small therapeutic molecules - is advantageous compared to eukaryotic production strategies. However, due to the potential endotoxin and host cell protein contamination, the requirements for the purification process are disproportionately higher and therefore more expensive and elaborate to circumvent. For this reason, the goal of this work was to develop and establish a rapid, simple, inexpensive and `up-scalable' production and purification process, using the therapeutic relevant protein anti-EGFR scFv hu225 as model molecule. Configuring high cell density cultivation of Escherichia coli - using the rha-BAD expression system as production platform - a specific product concentration up to 20 mg(scFv)/g(CDW) was obtained. By combining freeze-and-thaw, osmotic shock and pH induced host cell protein precipitation, almost 70\% of the product was extracted from the biomass. In a novel approach a mixed mode chromatography was implemented as a capturing and desalting step, which allowed the direct application of further ion exchange chromatography steps for purification up to pharmaceutical grade. Thereby, 50\% of the produced scFv could be purified within 10 h while maintaining the biological activity. (C) 2014 Elsevier B.V. All rights reserved.

Abstract

AimsThe aim of this study was to engineer Escherichia coli strains that efficiently produce succinate from glycerol under anaerobic conditions after an aerobic growth phase. Methods and ResultsWe constructed E.coli strain ss195 with deletions of pykA and pykF, which resulted in slow growth on glycerol as sole carbon source. This growth defect was overcome by the selection of fast-growing mutants. Whole-genome resequencing of the evolved mutant ss251 identified the mutation A595S in PEP carboxylase (Ppc). Reverse metabolic engineering by introducing the wild-type allele revealed that this mutation is crucial for the described phenotype. Strain ss251 and derivatives thereof produced succinate with high yields above 80\% molmol(-1) from glycerol under nongrowth conditions. ConclusionsThe results show that during the aerobic growth of ss251, the formation of pyruvate proceeds via the proposed POMP pathway, starting with the carboxylation of PEP by Ppc. The resulting oxaloacetate is reduced by malate dehydrogenase (Mdh) to malate, which is then decarboxylated back to pyruvate by a malic enzyme (MaeA or MaeB). Mutation of ppc is crucial for fast growth of pykAF mutants on glycerol. Significance and Impact of StudyAn E.coli mutant that is capable of achieving high yields of succinate (a top valued-added chemical) from glycerol (an abundant carbon source) was constructed. The identified ppc mutation could be applied to other production strains that require strong PEP carboxylation fluxes.

Abstract

A two-phase biotransformation process for selective hydroxylation of n-octane to 1-octanol via Pseudomonas putida KT2440 harboring heterologously expressed P450 monooxygenase from Mycobacterium marinum is presented. Maximum cell-specific conversion rates of 12.7mg(octanol)g(CDW)h(-1) were observed not only in shaking flasks but also in 3.7-L-bioreactor studies. The bioreactor experiments were performed avoiding explosive gas mixtures by lowering volumetric power input, aeration rates and substrate concentrations. Based on a stoichiometric network of P. putida KT2440 topological studies were carried out. As a conclusion, potential limitations of NAD(P)H and/or ATP supply at production conditions can be excluded. Hence, the great potential of the host for further increasing conversion is outlined.

Abstract

A novel technically compliant expression system was developed for heterologous protein production in Bacillus subtilis with the aim of increasing product yields at the same time as decreasing production costs. Standard systems involve the positively regulated manP promoter of the mannose operon, which led to relatively high product yields of 5.3\% (5.3 g enhanced green fluorescent protein eGFP per 100 g cell dry weight CDW) but required large quantities of mannose to induce the reactions, thus rendering the system's technical application rather expensive. To improve this situation, mutant B. subtilis strains were used: the Delta manA (mannose metabolism) strain TQ281 and the Delta manP (mannose uptake) strain TQ356. The total amount of inducer could be reduced with TQ281, which, however, displayed sensitivity to mannose. An inducer-independent self-induction system was developed with TQ356 to further improve the cost efficiency and product yield of the system, in which glucose prevents induction by carbon catabolite repression. To create optimal self-induction conditions, a glucose-limited process strategy, namely, a fed-batch process, was utilized as follows. The initiation of self-induction at the beginning of the glucose-restricted transition phase between the batch and fed-batch phase of fermentation and its maintenance throughout the glucose-limiting fed-batch phase led to a nearly 3-fold increase of product yield, to 14.6\%. The novel B. subtilis self-induction system thus makes a considerable contribution to improving product yield and reducing the costs associated with its technical application.

Abstract

Current messenger RNA (mRNA) quantification methods are sophisticated tools for the analysis of gene regulation. However, these methods are not suitable for more complex quantitative approaches such as the mathematical modeling of the in vivo regulation of transcription where dynamic cytosolic mRNA concentrations need to be taken into consideration. In the current study, the ``standard curve method'' for quantitative reverse transcription real-time polymerase chain reaction (qRT-PCR) was extended by including an internal RNA standard. This standard enables transcript losses that occur during the process, as well as variations resulting from nonquantitative processes, to be accounted for. The use of an internal standard yielded transcript concentration estimates that were on average seven times higher than those in cases where an internal standard is omitted. Choosing the cra modulon in Escherichia coli as an example, the method applied shows that the regulation of the Cra protein, as well as the growth rate-dependent regulation, need to be taken into consideration. The new method, which enables the determination of cytosolic mRNA concentrations, allows the quantitative representation of transcriptional dynamics. This is an important aspect of the analysis of the complex interactions of metabolism and regulation and in the application of mathematical modeling for systems biology. (C) 2009 Elsevier Inc. All rights reserved.

Abstract

The field of systems biology is often held back by difficulties in obtaining comprehensive, high-quality, quantitative data sets. In this paper, we undertook an interlaboratory effort to generate such a data set for a very large number of cellular components in the yeast Saccharomyces cerevisiae, a widely used model organism that is also used in the production of fuels, chemicals, food ingredients and pharmaceuticals. With the current focus on biofuels and sustainability, there is much interest in harnessing this species as a general cell factory. In this study, we characterized two yeast strains, under two standard growth conditions. We ensured the high quality of the experimental data by evaluating a wide range of sampling and analytical techniques. Here we show significant differences in the maximum specific growth rate and biomass yield between the two strains. On the basis of the integrated analysis of the high-throughput data, we hypothesize that differences in phenotype are due to differences in protein metabolism.

Abstract

The majority of dynamic gene regulatory network (GRN) models are comprised of only a few genes and do not take multiple transcription regulation into account. The models are conceived in this way in order to minimize the number of kinetic parameters. In this paper, we propose a new approach for predicting kinetic parameters from DNA-binding site sequences by correlating the protein-DNA binding affinities with nucleotide sequence conservation. We present the dynamic modeling of the cra modulon transcription in Escherichia coli during glucose-limited fed-batch cultivation. The concentration of the Cra regulator protein inhibitor, fructose1,6-bis(phosphate), decreases sharply, eventually leading to the repression of transcription. Total RNA concentration data indicate a strong regulation of transcription through the availability of RNA polymerase. A critical assessment of the results of the model simulations supports this finding. This new approach for the prediction of transcription dynamics may improve the metabolic engineering of gene regulation processes. (C) 2009 Published by Elsevier Inc.

Abstract

A time series of whole-genome transcription profiling of Escherichia coli K-12 W3110 was performed during a carbon-limited fed-batch process. The application of a constant feed rate led to the identification of a dynamic sequence of diverse carbon limitation responses ( e. g., the hunger response) and at the same time provided a global view of how cellular and extracellular resources are used: the synthesis of high-affinity transporters guarantees maximal glucose influx, thereby preserving the phosphoenolpyruvate pool, and energy-dependent chemotaxis is reduced in order to provide a more economic ``work mode.'' sigma(S)-mediated stress and starvation responses were both found to be of only minor relevance. Thus, the experimental setup provided access to the hunger response and enabled the differentiation of the hunger response from the general starvation response. Our previous topological model of the global regulation of the E. coli central carbon metabolism through the crp, cra, and relA/spoT modulons is supported by correlating transcript levels and metabolic fluxes and can now be extended. The substrate is extensively oxidized in the tricarboxylic acid (TCA) cycle to enhance energy generation. However, the general rate of oxidative decarboxylation within the pentose phosphate pathway and the TCA cycle is restricted to a minimum. Fine regulation of the carbon flux through these pathways supplies sufficient precursors for biosyntheses. The pools of at least three precursors are probably regulated through activation of the (phosphoenolpyruvate-)glyoxylate shunt. The present work shows that detailed understanding of the genetic regulation of bacterial metabolism provides useful insights for manipulating the carbon flux in technical production processes.

Abstract

The intracellular alarmone guanosine 3 `,5 `-bis(diphosphate) (ppGpp) has been thoroughly investigated over the past 40 years and has become one of the best-known effectors in bacterial physiology. ppGpp is also of great importance for biotechnological applications. Systems biology research, involving experimental and mathematical approaches, has contributed a great deal to uncovering the alarmone's complex regulatory effects. HPLC analysis and UV detection are used to quantify intracellular ppGpp. The samples analyzed also contain other phosphorylated guanine nucleotides and, therefore, are spiked with a standard ppGpp solution. A rapidly growing number of laboratories are turning to synthesizing the nucleotide in vitro involving time-consuming protocols and yielding only low amounts of ppGpp. The current article provides a protocol for the preparation of large quantities of a ribosome extract that contains high ppGpp synthesis activity. The demonstrated upscaling from shaking flask to bioreactor cultivation involves the continuous and refrigerated harvest of the biomass. C-13 NMR analysis enabled the structural characterization of the synthesis product and was complemented by mass spectrometry and methods that are commonly used to identify ppGpp. (C) 2008 Elsevier Inc. All rights reserved.

Abstract

One fundamental shortcoming of biotechnological processes operating under carbon-limiting conditions is the high-energy demand (maintenance) of the cells. Although the function of the central carbon metabolism in supplying precursors and energy for biosynthesis has been thoroughly characterized, its regulation and dynamic behaviour during carbon-limited growth has not yet been revealed. The current work demonstrates a time series of metabolic flux distributions during fed-batch cultivation of Escherichia coli K-12 W3110 applying a constant feed rate. The fluxes in glycolysis, pentose phosphate pathway and biosynthesis fell significantly, whereas TCA cycle fluxes remained constant. The flux redistribution resulted in an enhanced energy generation in the TCA cycle and consequently, in a 20\% lower biomass yield. The intracellular alarmones ppGpp and cAMP accumulated in large quantities after the onset of nutrient limitation, subsequently declining to basal levels. The network topology of the regulation of the central metabolic pathways was identified so that the observed metabolic and regulatory behaviour can be described. This provides novel aspects of global regulation of the metabolism by the cra, crp and relA/spoT modulons. The work constitutes an important step towards dynamic mathematical modelling of regulation and metabolism, which is needed for the rational optimization of biotechnological processes. (c) 2007 Elsevier B.V. All rights reserved.

Abstract

The application of functionalised magnetic adsorbent particles in combination with magnetic separation techniques has received considerable attention in recent years. The magnetically responsive nature of such adsorbent particles permits their selective manipulation and separation in the presence of other suspended solids. Thus, it becomes possible to magnetically separate selected target species directly out of crude biological process liquors (e.g. fermentation broths, cell disruptates, plasma, milk, whey and plant extracts) simply by binding them on magnetic adsorbents before application of a magnetic field. By using magnetic separation in this way, the several stages of sample pretreatment (especially centrifugation, filtration and membrane separation) that are normally necessary to condition an extract before its application on packed bed chromatography columns, may be eliminated. Magnetic separations are fast, gentle, scaleable, easily automated, can achieve separations that would be impossible or impractical to achieve by other techniques, and have demonstrated credibility in a wide range of disciplines, including minerals processing, wastewater treatment, molecular biology, cell sorting and clinical diagnostics. However, despite the highly attractive qualities of magnetic methods on a process scale, with the exception of wastewater treatment, few attempts to scale up magnetic operations in biotechnology have been reported thus far. The purpose of this review is to summarise the current state of development of protein separation using magnetic adsorbent particles and identify the obstacles that must be overcome if protein purification with magnetic adsorbent particles is to find its way into industrial practice.

Abstract

A dynamic model of prokaryotic gene expression is developed that makes considerable use of gene sequence information. The main contribution arises from the fact that the combined gene expression model allows us to access the impact of altering a nucleotide sequence on the dynamics of gene expression rates mechanistically. The high level of detail of the mathematical model is considered as an important step towards bringing together the tremendous amount of biological in-depth knowledge that has been accumulated at the molecular level, using a systems level analysis (in the sense of a bottom-up, inductive approach). This enables to the model to provide highly detailed insights into the various steps of the protein expression process and it allows us to access possible targets for model-based design. Taken as a whole, the mathematical gene expression model presented in this study provides a comprehensive framework for a thorough analysis of sequence-related effects on the stages of mRNA synthesis, mRNA degradation and ribosomal translation, as well as their nonlinear interconnectedness. Therefore, it may be useful in the rational design of recombinant bacterial protein synthesis systems, the modulation of enzyme activities in pathway design, in vitro protein biosynthesis, and RNA-based vaccination.

Abstract

A continuous-flow technique has been developed to analyse the deltaD and delta(13)C values for CH4 from gas samples, in a single run. This is achieved by splitting the sample gas stream and directing the streams simultaneously through a CuNiPt combustion reactor and an alumina pyrolysis reactor. The CO2 from CH4 combustion is trapped in a liquid nitrogen trap while the H-2 exiting the pyrolysis reactor is directed to the mass spectrometer for deltaD(CH4) determination. The CO2 is then sublimed and directed to the mass spectrometer for delta(13)C(CH4) determination. Sample runs take approximately 10 minutes. This technique gives accurate delta(13)C(CH4) results to within +/-0.3-0.5parts per thousand and deltaD(CH4) results to within +/-2-5parts per thousand. Injection volumes between 0.5 and 2.5 muL of CH4, equivalent to between 20 and 100 nmol CH4, are required for accurate delta(13)C and deltaD analyses, respectively, using sample injection into a split flow with a split ratio of 10. This method provides rapid, accurate and reproducible results on multiple sample runs and is, therefore, an ideal method for analysing natural gas samples from a variety of sources. Copyright (C) 2003 John Wiley Sons, Ltd.

Abstract

Arthrobacter crystallopoietes produces a D-specific hydantoinase and D-N-carbamoylase useful for the industrial production of enantiomerically pure D-amino acids. The D-hydantoinase was purified by conventional chromatographic methods. The enzyme was digested by trypsine and some of the oligopeptides sequenced. The amino acid sequence information was used to isolate a DNA fragment of the corresponding gene. By several steps of inverse PCR a region of 6011 bp was obtained from the A. crystallopoietes genome surrounding the hydantoinase gene fragment. DNA sequence analysis revealed the presence of a D-hydantoinase, the D-N-carbamoylase and a putative L-N-carbamoylase on the 6011 bp fragment. In addition, two incomplete open reading frames (ORFs) showed similarity to LacI type transcriptional regulators and transmembrane proteins responsible for the uptake of nucleosides and allantoin, respectively. The D-hydantoinase gene and the D-N-carbamoylase gene were expressed in Escherichia coli and the enzyme activity was determined. From the putative L-N-carbamoylase gene, expressed in the same way in E. coli, only insoluble protein was obtained and no carbamoylase activity was detected.

Abstract

The atrazine-specific single-chain variable antibody fragments (scFv) K411B was produced by expression in either the cytoplasm or the periplasm of Escherichia coli BL21 (DE3). For periplasmic production, the pelB leader was N-terminally fused to scFv, whereas the unfused variant resulted in cytoplasmic expression. The extent of protein accumulation differed significantly. Expression of scFv with leader was 2.3 times higher than that of the protein without leader. This was further investigated by generating the respective translation profiles using coupled in vitro transcription/translation assays, the results of which were in agreement. This comparative approach was also applied to functionality: Periplasmic expression and in vitro expression resulted in only 10\% correctly folded scFv, indicating that the oxidizing environment of the periplasm did not increase proper folding. Thus, the data obtained in vitro confirmed the findings observed in vivo and suggested that the discrepancy in expression levels was due to different translation efficiencies. However, the in vivo production of scFv with enhanced green fluorescent protein (EGFP) fused C-terminally (scFv-EGFP) was only successful in the cytoplasm, although in vitro the expression with and without the leader rendered the same production profile as for scFv. This indicated that neither the translation efficiency nor the solubility but other factors impeded periplasmic expression of the fusion protein.

Abstract

L-Hydantoinase from Arthrobacter aurescens (L-Hyd) is a member of the dihydropyrimidinases which in turn belong to the cyclic amidases. Dihydropyrimidinases catalyze the reversible hydrolytic ring opening of dihydropyrimidines as the second step in the catabolism of pyrimidines. In biotechnology, their hydroloytic activity on five-membered cyclic diamides (hydantoins) is used in the enantio-specific production of amino acids from racemic hydantoins. L-Hyd differs from most of the other dihydropyrimidinases by an L-enantio specificity and by lacking activity on possible natural substrates such as dihydropyrimidines. In this paper, we describe the three-dimensional structure of L-Hyd which Was solved by molecular replacement using a homology model and subsequently refined to 2.6 Angstrom resolution. Each subunit of the tetrameric L-Hyd consists of an elliptically distorted (alpha/beta)(s)-barrel domain, which hosts the active site, and a beta-sheet domain. In the active site, a binuclear zinc center activates a Water molecule for nucleophilic attack on the substrates' amide bond. L-Hyd shows a strong homology both in fold and in metal coordination in the active site to another dihydropyrimidinase from Thermus sp. (D-hydantoinase) and to a slightly lesser degree to ureases, dihydroorotase and phosphotriesterase. Using the homology to ureases, a model for the transition state was modeled in the active site of L-Hyd and D-hydantoinase. This model could provide an explanation for the different substrate and enantio selectivities of both dihydropyrimidinases.

Abstract

A cascade of hydantoinase, N-carbamoylase and hydantoinracemase can be used for the production of natural and unnatural chiral D- and L-amino acids from chemically synthesized hydantoin derivatives. Potentially, 100\% conversion and 100\% optically pure amino acids can be obtained at the same time if racemic substrates are used. Recent research activities concentrate on newly isolated or improved enzymes and include directed evolution techniques, structure elucidation, studies of fusion proteins and the use of specially designed whole cell biocatalysts.

Abstract

A high-cell-density fed-batch fermentation for the production of heterologous proteins in Escherichia coli was developed using the positively regulated Escherichia coli rhaBAD promoter. The expression system was improved by reducing of the amount of expensive L-rhamnose necessary for induction of the rhamnose promoter and by increasing the vector stability. Consumption of the inducer L-rhamnose was inhibited by inactivation of L-rhamnulose kinase encoding gene rhaB of Escherichia coli W3110, responsible for the first irreversible step in rhamnose catabolism. Plasmid instability caused by multimerization of the expression vector in the recombination-proficient W3110 was prevented by insertion of the multimer resolution site cer from the ColE1 plasmid into the vector. Fermentation experiments with the optimized system resulted in the production of 100 g L-1 cell dry weight and 3.8 g L-1 of recombinant L-N-carbamoylase, an enzyme, which is needed for the production of enantiomeric pure amino acids in a two-step reaction from hydantoins, (C) 2001 John Wiley & Sons, Inc.

Abstract

This study provides a mathematical model of T7 RNA polymerase (T7 RNAP) kinetics under in vitro conditions targeted at application of this model to simulation of dynamic transcription performance. A functional dependence of transcript synthesis rate is derived based on: (a) essential reactant concentrations, including T7 RNAP and its promoter, substrate nucleotides, and the inhibitory byproduct inorganic pyrophosphate; (b) a distinction among vector characteristics such as recognition sequences regulating transcription initiation and termination, respectively; and (c) specific properties of the nucleotide sequence including both transcript length and nucleotide composition. Inactivation kinetics showed a half-life of T7 RNAP activity of 50 min under the conditions applied in vitro using the isolated enzyme. Model parameters and their precision are estimated using dynamic simulation and nonlinear regression analysis. The particular novelty of this model is its capability to incorporate linear genomic sequence information for simulation of nonlinear in vitro transcription kinetics. (C) 2001 John Wiley & Sons, Inc.

Abstract

Cell-free extracts (lysates) from Escherichia coli were used for protein synthesis in vitro. Essential steps of the lysate preparation were modified and analyzed with respect to their impact on in vitro protein synthesis capacity, using the green fluorescent protein (GFP) as a target protein. Variably manufactured lysates of low, medium and higher protein synthesis activity, were examined by high resolution two-dimensional get electrophoresis to determine whether the modifications result in substantial alterations in protein composition of the final lysate. The total number of proteins calculated from the get maps did not vary for lysates with different activity and thus cannot serve as an evaluation parameter. Ribosomal proteins RP-S1, RP-L9, and RP-L10 were found in stoichiometric amounts for each of these lysates and in equal concentrations in comparison among the different lysates. Conversely, depending on the activity profiles, up to 7 different isoforms of the elongation factor EF-Ts were detected in the gel maps.

Abstract

Hydantoinases are valuable enzymes for the production of optically pure D- and L-amino acids. They catalyse the reversible hydrolytic ring cleavage of hydantoin or 5'-monosubstituted hydantoins and are therefore classified in the EC nomenclature as cyclic amidases (EC 3.5.2.). In the EC nomenclature, four different hydantoin-cleaving enzymes are described: dihydropyrimidinase (3,5.2.2), allantoinase (EC 3.5.2.5), carboxymethylhydantoinase (EC 3.5.2.4), and N-methylhydantoinase (EC 3.5.2.14). Beside these, other hydantoinases with known metabolic functions, such as imidase and carboxyethylhydantoinase and enzymes with unknown metabolic function, are described in the literature and have not yet been classified. An important question is whether the distinct hydantoinases, which are frequently classified as L-, D-, and non-selective hydantoinases depending on their substrate specificity and stereoselectivity, are related to each other. In order to investigate the evolutionary relationship, amino acid sequence data can be used for a phylogenetic analysis. Although most of these enzymes only share limited sequence homology (identity <15\%) and therefore are only distantly related, it can be shown (i) that most of them are members of a broad set of amidases with similarities to ureases and build a protein superfamily, whereas ATP-dependent hydantoinases are not related, (ii) that the urease-related amidases have evolved divergently from a common ancestor and (iii) that they share a metal-binding motif consisting of conserved histidine residues. The difference in enantioselectivity used for the classification of hydantoinases on the basis of their biotechnological value does not reflect their evolutionary relationship, which is to a more diverse group of enzymes than was assumed earlier. This protein superfamily probably has its origin in the prebiotic conditions of the primitive earth.

Abstract

A D-specific hydantoinase has been purified to homogeneity from Arthrobacter crystallopoietes DSM 20117 with a yield of 5\% related to the crude extract. The active enzyme is a tetramer of 257 kDa consisting of four identical subunits, each with a molecular mass of 60 kDa. Incubation of the enzyme with the metal-chelating agent EDTA had no inhibitory effect, while 8-hydroxyquinoline-5-sulfonic acid resulted in a complete and irreversible inactivation. The purified enzyme contains zinc as cofactor, which could be detected by subjection to direct analysis using inductive/coupled plasma-atomic emission spectrometry. The hydantoinase has a wide substrate specificity for the D-selective cleavage of 5-monosubstituted hydantoin derivatives with aliphatic and aromatic side chains. The V-max-value for phenylhydantoin is 217 U/mg, the K-m-value is 8 mM. Dihydrouracil was found to be a natural substrate (V-max = 35 U/mg). The N-terminal amino acid sequence of the enzyme shows distinct homologies to other metal-dependent cyclic amidases involved in the nucleotide metabolism especially to dihydropyrimidinases as well as to ureases, L- and unselective hydantoinases. Due to these findings, this enzyme has to be considered as a possible link in the evolution to related L-selective and unselective hydantoinases from the genus of Arthrobacter. (C) 1999 Elsevier Science B.V. All rights reserved.

Abstract

A cell-free extract from Escherichia coli, generated through a routine procedure according to Chen and Zubay (Methods Enzymol. 1983, 101, 674-690), was used for an in vitro protein synthesis. High-resolution two-dimensional gel electrophoresis (2-DE) was exploited to investigate the protein composition of the cell-extract and its dynamic development during a 24 h-period of cell-free protein synthesis performed in a membrane reactor device. Green fluorescent protein (GFP) was chosen as a target protein to be produced in a cell-free reactor because of its functional activity, which can easily be monitored by measurement of fluorescence, and because of its high sensitivity. GFP synthesis was observed by a standard fluorescence assay and was correlated to a quantitative assessment of the silver-stained GFP spot appearing on 2-DE gel maps. A constant protein synthesis rate was obtained for at least 8 h of process operation. While declining continuously, protein synthesis stopped entirely after 24 h. Both, the total protein content and total number of detectable spots were found to decrease over the reaction time, due to proteolytic digestion and protein precipitation. Certain proteins taking part in the translation process, such as the elongation factors (EF-Tu, EF-Ts) and the ribosomal protein RP-L9, were identified by Edman N-terminal sequencing and have thus been considered for reaction evaluation. The dynamics obtained during the entire process suggest that these translational factors were likewise affected by proteolytic decay.

Abstract

Metal dependency of the hydantoin amidohydrolase (hydantoinase) from Arthrobacter aurescens DSM 3745 has been analyzed based on kinetic studies of metal/chelator-caused enzyme inactivation, denaturation and reactivation, accompanied by the identification of specific metal binding ligands. The enzyme can be inactivated by metal chelating agents and-apart from the loss of its activity-completely dissociates into its subunits. Enzyme activity can be restored from recollected monomers by the addition of cobalt, manganese or zinc-ions, whereas nickel and magnesia remain ineffective. Subjection of the hydantoinase to metal analysis reveals a content of 10 mol zinc per mol enzyme. Zinc plays an essential role not only for the catalytic activity but also for the stabilization of the active quarternary structure of the hydantoinase. Histidine-specific chemical modification of the enzyme causes a complete loss of the catalytic activity and reveals histidine residues as putative zinc binding ligands. Both, the metal/chelator-caused enzyme inactivation as well as the metal-caused enzyme reactivation, can be reduced in the presence of the substrate. Therefore, it is very likely that at least one metal-ion acts specifically near or at the active site of the enzyme. (C) 1998 Elsevier Science B.V. All rights reserved.

Abstract

A hydantoinase from Arthrobacter aurescens DSM 3745 has been purified to homogeneity with a yield of 77\% using a three-step purification procedure. The active enzyme is a tetramer consisting of four identical subunits, each with a molecular mass of 49670 Da as determined by mass spectrometry. The N-terminal amino acid sequence of the enzyme indicates sequence identities to cyclic amidases involved in the nucleotide metabolism as the D-hydantoinase from Agrobacterium radiobacter (53\%), the D-selective dihydropyrimidinase from Bacillus stearothermophilus (38\%), the allantoinase from Rana catesbeiana (26\%), as well as to the catalytic subunit of the urease from Heliobacter pylori (50\%). However, all studies based on substrate-dependent growth, induction and catalytic behavior documented the novelty of the bacterial hydantoinase and that its physiological role is not related to any of these enzymes or known metabolic pathways. Its substrate specificity differs from hydantoinases listed in Enzyme Nomenclature and is rather more predominant for the cleavage of aryl-than for alkyl-hydantoin, derivatives. It is shown that the stereoselectivity of this enzyme depends on the substrate used for bioconversion: although it is strictly L-selective for the cleavage of D,L-5-indolylmethylhydantoin, it appears to be D-selective for the hydrolysis of D,L-methylthioethylhydantoin. Due to these findings we conclude that this novel bacterial hydantoinase should be classified as a new member of the EC-group 3.5.2 of cyclic amidases. (C) 1998 Elsevier Science B.V. All rights reserved.

Abstract

The hydantoin amidohydrolase (hydantoinase) from Arthrobacter aurescens DSM 3745 was purified to homogeneity and subjected to metal analysis under atomic absorption spectrometry (AAS) and inductive coupled plasma-atomic emission spectrometry (ICP-AES). Three independent preparations of homogeneous enzyme indicated that 1 mol of the active enzyme contains 10 mol zinc ions. This corresponds to 2.5 mol zinc per mol subunit, since the hydantoinase consists of four identical subunits. Only trace amounts of manganese, magnesia, nickel and cobalt were detected. Other metals were either absent or existed below detection levels. (C) 1998 Elsevier Science B.V. All rights reserved.

Abstract

The complete amino acid sequence of the hydantoinase from Arthrobacter aurescens DSM 3745 has been derived by automated Edman degradation. This is the fi rst ever reported amino acid sequence of a non-ATP-dependent hydantoinase, which hydrolyzes 5'-monosubstituted hydantoin derivatives L-selectively, A homology search performed in protein and nucleic acid databases retrieved only distantly related proteins. All of these are members of the recently described protein superfamily of amidohydrolases related to ureases (Holm and Sander, Proteins 28: 72-82, 1997). Phylogenetic analysis revealed that the novel hydantoinase forms a new branch separate from other hydantoin cleaving enzymes like dihydropyrimidinases (EC 3.5.2.2) and allantoinases (EC 3,5,2.5), Our results suggests that the enzymes of this protein superfamily have evolved from a common ancestor and therefore are the product of divergent evolution, We show further that the enclosed gene families developed very early in evolution, probably prior to the formation of the three domains, Archaea, Eukarya and Bacteria, Hydantoinases related to ATP-depdent N-methylhydantoinases (EC 3.5.2.14) or 5-oxoprolinases (EC 3.5.2.9) do not belong to this superfamily.

Abstract

A new and highly sensitive method was developed for the identification of hydantoinases on acrylamide gels. For this purpose, cell-lysates from different natural isolates are subjected on PAGE under non-denaturating conditions. The respective localisation of the hydantoinase is obtained by in situ product precipitation during the reverse enzyme reaction: in contrast to the used substrate (N-carbamoyltryptophan), the product (indolylmethylhydantoin) is barely soluble and gives a dense precipitation dot caused by crystallisation of the product inside of the polyacrylamide gel at the position corresponding to the location of the enzyme. This method can also be used for the subsequent differentiation between L- and D-selective hydantoinases, since L- or D-carbamoyltryptophan is used as substrate.

Abstract

L-Hydantoinase from Arthrobacter aurescens DSM 3745 has been purified to homogeneity and crystallized from polyethylene glycol solutions in a form suitable for X-ray diffraction analysis. The crystals have been grown by the sitting-drop variant of the vapour-diffusion method. X-ray diffraction studies show that the crystals belong to the monoclinic space group P2(1) with a = 111.2, b = 74.4, c = 146.5 Angstrom and beta = 106.7 degrees. Its asymmetric unit contains four monomers related by 222 symmetry. The crystals diffract to at least 2.6 Angstrom.

Abstract

We show that a simple cell-free translation system from Escherichia coli, programmed with phage MS2 RNA, is able to infect F+ E. coli cells, The plaques appearing on the E. coli host strain are morphologically indistinguishable from those derived from normal phage MS2 infection, This effect is strictly translation-dependent, since an incomplete translation system or the system inhibited by antibiotics leads to no infection, The cell-free based infection is maximal under conditions favouring the highest synthesis of maturation protein (one of the four phage-encoded proteins), The infection is abolished when RNase A or trypsin treatment is included before addition of cells, Similarly, due to RNA and maturation protein degradation, the continued incubation of the translation mixture under protein synthesis conditions significantly decreases infectivity, These findings suggest the formation of `minimal infectious units', simple complexes of MS2 RNA and maturation protein, Here we describe the first example of bacteriophage infectious unit formation directly performed in a cell-free translation system, A possible application of this phenomenon might be the construction of newly designed RNA vector delivery systems and, moreover, could be an approach for molecular evolution studies.

Abstract

Molecular imprinting was applied to the synthesis of methacrylic acid-ethylene glycol dimethacrylate copolymers specific for the herbicide atrazine. In toluene, these imprints bound atrazine with dissociation constant (K-D) values as low as 10(-6) M, and could be used for the development of a ligand binding assay for the detection of atrazine. The selectivity profile of the imprints for triazines structurally related to atrazine was comparable to those of antibodies. The substituent of carbon C1 is the most important feature determining the level of cross-reactivity, and the binding affinity decreased in the order Cl > OCH3 > OH > SCH3 (atrazine, the imprint species, has C1 at this position). No cross-reaction of structurally unrelated herbicides and other compounds was detected. Rebinding experiments in phosphate buffer containing 0.15\% Tween 20 gave similar results. The polymers could be packed into HPLC columns and used for the separation of triazine derivatives. The potential uses of imprinted polymers for the detection of pollutants in environmental analysis and as sorbents for the specific removal of toxic compounds in waste water treatment are discussed.

Abstract

Polyclonal antibodies were produced against the highly purified L-5-aryl-alkyl-hydantoinase and hydantoin-racemase of Arthrobacter aurescens DSM 3747. Serological interaction of the hydantoinase antibody with its corresponding antigenic fraction let to a remarkable improvement of the stability of the hydantoinase. The immobilization of the catalytic active enzyme-antibody complex onto a Sepharose 4B-support underlined this antibody-mediated stabilization effect, while control experiments with preimmunsera or the hydantoin-racemase antibodies gave no or even a negative effect.

Abstract

Polyclonal antibodies were produced against the highly purified enzymes L-hydantoinase, hydantoin-racemase and L-N-carbamoylamino acid amidohydrolase of Arthrobacter aurescens DSM 3747. Using these antibodies as screening tools, a colony transfer procedure allowed the rapid detection of highly active strains. Furthermore, common Western-blot analysis enabled the direct estimation of internal enzyme concentrations, protein turnover, efficiency of different inducers and a molecular comparison of enzymes derived from different sources. Using this method it is demonstrated that of several tested microorganisms, two Arthrobacter strains showed improved production abilities.

Abstract

Polyclonal antibodies were produced against the highly purified enzymes L-hydantoinase, hydantoin-racemase and L-N-carbamoylamino acid amidohydrolase of Arthrobacter aurescens DSM 3747. In order to exploit these antibodies for basic research (molecular biology) or bioengineering (process development), the serological properties had to be characterized. Both, the hydantoinase- and carbamoylase-antibodies were observed to be monofunctional, whereas the hydantoin-racemase-antibody was found to be additionally specific against the L-hydantoinase. Monospecificity was realized after affinity chromatography. Investigations on serological crossreactions with several linear- and cyclic amidases (e.g. hydantoinases) as well as hydantoin-racemases are demonstrated in this paper.