Dynamic gene expression regulation model for growth and penicillin production in Penicillium chrysogenum.

As is often the case for microbial product formation, the penicillin production rate of Penicillium chrysogenum has been observed to be a function of the growth rate of the organism. The relation between the biomass specific rate of penicillin formation (q(p)) and growth rate (mu) has been measured under steady state conditions in carbon limited chemostats resulting in a steady state q(p)(mu) relation. Direct application of such a relation to predict the rate of product formation during dynamic conditions, as they occur, for example, in fed-batch experiments, leads to errors in the prediction, because q(p) is not an instantaneous function of the growth rate but rather lags behind because of adaptational and regulatory processes. In this paper a dynamic gene regulation model is presented, in which the specific rate of penicillin production is assumed to be a linear function of the amount of a rate-limiting enzyme in the penicillin production pathway. Enzyme activity assays were performed and strongly indicated that isopenicillin-N synthase (IPNS) was the main rate-limiting enzyme for penicillin-G biosynthesis in our strain. The developed gene regulation model predicts the expression of this rate limiting enzyme based on glucose repression, fast decay of the mRNA encoding for the enzyme as well as the decay of the enzyme itself. The gene regulation model was combined with a stoichiometric model and appeared to accurately describe the biomass and penicillin concentrations for both chemostat steady-state as well as the dynamics during chemostat start-up and fed-batch cultivation.

Development of efficient xylose fermentation in Saccharomyces cerevisiae: xylose isomerase as a key component.

Metabolic engineering of Saccharomyces cerevisiae for ethanol production from D-xylose, an abundant sugar in plant biomass hydrolysates, has been pursued vigorously for the past 15 years. Whereas wild-type S. cerevisiae cannot ferment D-xylose, the keto-isomer D-xylulose can be metabolised slowly. Conversion of D-xylose into D-xylulose is therefore crucial in metabolic engineering of xylose fermentation by S. cerevisiae. Expression of heterologous xylose reductase and xylitol dehydrogenase does enable D-xylose utilisation, but intrinsic redox constraints of this pathway result in undesirable byproduct formation in the absence of oxygen. In contrast, expression of xylose isomerase (XI, EC 5.3.1.5), which directly interconverts D-xylose and D-xylulose, does not have these constraints. However, several problems with the functional expression of various bacterial and Archaeal XI genes have precluded successful use of XI in yeast metabolic engineering. This changed with the discovery of a fungal XI gene in Piromyces sp. E2, expression of which led to high XI activities in S. cerevisiae. When combined with over-expression of the genes of the non-oxidative pentose phosphate pathway of S. cerevisiae, the resulting strain grew anaerobically on D-xylose with a doubling time of ca. 8 h, with the same ethanol yield as on glucose. Additional evolutionary engineering was used to improve the fermentation kinetics of mixed-substrate utilisation, resulting in efficient D-xylose utilisation in synthetic media. Although industrial pilot experiments have already demonstrated high ethanol yields from the D-xylose present in plant biomass hydrolysates, strain robustness, especially with respect to tolerance to inhibitors present in hydrolysates, can still be further improved.

High-level functional expression of a fungal xylose isomerase: the key to efficient ethanolic fermentation of xylose by Saccharomyces cerevisiae?

Evidence is presented that xylose metabolism in the anaerobic cellulolytic fungus Piromyces sp. E2 proceeds via a xylose isomerase rather than via the xylose reductase/xylitol-dehydrogenase pathway found in xylose-metabolising yeasts. The XylA gene encoding the Piromyces xylose isomerase was functionally expressed in Saccharomyces cerevisiae. Heterologous isomerase activities in cell extracts, assayed at 30 degrees C, were 0.3-1.1 micromol min(-1) (mg protein)(-1), with a Km for xylose of 20 mM. The engineered S. cerevisiae strain grew very slowly on xylose. It co-consumed xylose in aerobic and anaerobic glucose-limited chemostat cultures at rates of 0.33 and 0.73 mmol (g biomass)(-1) h(-1), respectively.

Xylose metabolism in the anaerobic fungus Piromyces sp. strain E2 follows the bacterial pathway.

The anaerobic fungus Piromyces sp. strain E2 metabolizes xylose via xylose isomerase and d-xylulokinase as was shown by enzymatic and molecular analyses. This resembles the situation in bacteria. The clones encoding the two enzymes were obtained from a cDNA library. The xylose isomerase gene sequence is the first gene of this type reported for a fungus. Northern blot analysis revealed a correlation between mRNA and enzyme activity levels on different growth substrates. Furthermore, the molecular mass calculated from the gene sequence was confirmed by gel permeation chromatography of crude extracts followed by activity measurements. Deduced amino acid sequences of both genes were used for phylogenetic analysis. The xylose isomerases can be divided into two distinct clusters. The Piromyces sp. strain E2 enzyme falls into the cluster comprising plant enzymes and enzymes from bacteria with a low G+C content in their DNA. The d-xylulokinase of Piromyces sp. strain E2 clusters with the bacterial d-xylulokinases. The xylose isomerase gene was expressed in the yeast Saccharomyces cerevisiae, resulting in a low activity (25+/-13 nmol min(-1)mg protein(-1)). These two fungal genes may be applicable to metabolic engineering of Saccharomyces cerevisiae for the alcoholic fermentation of hemicellulosic materials.

Clavulanic acid degradation in Streptomyces clavuligerus fed-batch cultivations.

Clavulanic acid (CA) is an important antibiotic that is produced by Streptomyces clavuligerus. CA is unstable and product degradation has turned out to have a major impact on product titers in fed-batch cultivations. Three different types of experiments have been used to elucidate CA degradation under fed-batch cultivation conditions. First, the influence of individual medium compounds was examined. Second, degradation was monitored during the exponential growth phase in batch cultivations. Third, CA degradation was studied in the supernatant of samples taken during a fed-batch. In addition, data from six fed-batch cultivations were studied to derive information about CA degradation during the production phase. These cultivations were based on a mineral medium, containing glycerol, glutamate, ammonium, and phosphate as the main nutrients. The ammonium concentration had a large influence on the degradation rate constant. In addition, either changes in the substrate availability or high concentrations of ammonium or glycerol cause a major increase in the degradation rate constant. Finally, a linear and a fuzzy logic model were made to predict CA degradation rates in these fed-batches.