Based on assumed reaction network structures, NADPH availability has been proposed to be a key constraint in β-lactam production by Penicillium chrysogenum. In this study, NADPH metabolism was investigated in glucose-limited chemostat cultures of an industrial P. chrysogenum strain. Enzyme assays confirmed the NADP+-specificity of the dehydrogenases of the pentose-phosphate pathway and the presence of NADP+-dependent isocitrate dehydrogenase. Pyruvate decarboxylase/NADP+-linked acetaldehyde dehydrogenase and NADP+-linked glyceraldehyde-3- phosphate dehydrogenase were not detected. Although the NADPH requirement of penicillin-G-producing chemostat cultures was calculated to be 1.4-1.6-fold higher than that of non-producing cultures, in vitro measured activities of the major NADPH-providing enzymes were the same. Isolated mitochondria showed high rates of antimycin A-sensitive respiration of NADPH, thus indicating the presence of a mitochondrial NADPH dehydrogenase that oxidises cytosolic NADPH. The presence of this enzyme in P. chrysogenum might have important implications for stoichiometric modelling of central carbon metabolism and β-lactam production and may provide an interesting target for metabolic engineering.

Commercial production of heterologous proteins by yeasts has gained considerable interest. Expression systems have been developed for Saccharomyces cerevisiae and a number of other yeasts. Generally, much attention is paid to the molecular aspects of heterologous-gene expression. The success of this approach is indicated by the high expression levels that have been obtained in shake-flask cultures. For large-scale production however, possibilities and restrictions related to host-strain physiology and fermentation technology also have to be considered. In this review, these physiological and technological aspects have been evaluated with the aid of numerical simulations. Factors that affect the choice of a carbon substrate for large-scale production involve price, purity and solubility. Since oxygen demand and heat production (which are closely linked) limit the attainable growth rate in large-scale processes, the biomass yield on oxygen is also a key parameter. Large-scale processes impose restrictions on the expression system. Many promoter systems that work well in small-scale systems cannot be implemented in industrial environments. Furthermore, large-scale fed-batch fermentations involve a substantial number of generations. Therefore, even low expression-cassette instability has a profound effect on the overall productivity of the system. Multicopy-integration systems may provide highly stable expression systems for industrial processes. Large-scale fed-batch processes are typically performed at a low growth rate. Therefore, effects of a low growth rate on the physiology and product formation rates of yeasts are of key importance. Due to the low growth rates in the industrial process, a substantial part of the substrate carbon is expended to meet maintenance-energy requirements. Factors that reduce maintenance-energy requirements will therefore have a positive effect on product yield. The relationship between specific growth rate and specific product formation rate (kg product·[kg biomass]−1·h−1) is the main factor influencing production levels in large-scale production processes. Expression systems characterized by a high specific rate of product formation at low specific growth rates are highly favourable for large-scale heterologous-protein production.

Production of extracellular inulinase by low-cell-density (2 kg dry weight·m-3) sucrose-limited chemostat cultures of Kluyveromyces marxianus obeyed saturated kinetics at dilution rates ranging from 0.02 to 0.5 h-1. A non-structured Monod-type equation, describing the relation between specific growth rate and specific extracellular-inulinase production rate, was used to fit experimental data. THis equation was subsequently incorporated in a model for the production of biomass and extracellular inulinase in a high-cell-density (> 100 kg dry weight·m-3) fed-batchculture of K. marxianus grown on sucrose. The model adequately described biomass production in the fed-batch culture. However, the production of extracellular inulinase in the fed-batch process was slightly higher than predicted by the model. This observation may be related to differences in growth conditions between in the chemostat and fed-batch cultures.

Chemostat cultivation enables investigations into the effects of individual environmental parameters on sugar transport in yeasts. Various means are available to manipulate the specific rate of sugar uptake (qs) in sugar-limited chemostat cultures. A straightforward way to manipulate qs is variation of the dilution rate, which, in substrate-limited chemostat cultures, is equal to the specific growth rate. Alternatively, qs can be varied independently of the growth rate by mixed-substrate cultivation or by variation of the biomass yield on sugar. The latter can be achieved, for example, by addition of nonmetabolizable weak acids to the growth medium or by variation of the oxygen supply. Such controlled manipulation of metabolic fluxes cannot be achieved in batch cultures, in which various parameters that are essential for the kinetics of sugar transport cannot be controlled. In sugar-limited chemostat cultures, yeasts adapt their sugar transport systems to cope with the low residual sugar concentrations, which are often in the micromolar range. Under the conditions, yeasts with high-affinity proton symport carriers have a competitive advantage over yeasts that transport sugars via facilitated-diffusion carriers. Chemostat cultivation offers unique possibilities to study the energetic consequences of sugar transport in growing cells. For example, anaerobic, sugar-limited chemostat cultivation has been used to quantify the energy requirement for maltose-proton symport in Saccharomyces cerevisiae. Controlled variation of growth conditions in chemostat cultures can be used to study the differential expression of genes involved in sugar transport and as such can make an important contribution to the ongoing studies on the molecular biology of sugar transport in yeasts.

Acinetobacter calcoaceticus can incompletely oxidize aldose sugars to the corresponding aldonic acids. This reaction can serve as an auxiliary energy source for the organism. An increase in biomass yields is observed in acetate-limited chemostat cultures grown in the presence of, for example, xylose. However, experimental and theoretical discrepancies exist with respect to the magnitude of the yield enhancement as a result of xylose addition. We previously observed increases in cell yields that were unexpectedly high. In contrast, other data were in agreement with the theoretical predictions. In this paper, evidence is presented indicating that this discrepancy is likely to be due to errors in the methodology used for our previous investigation, in particular with respect to the determination of biomass concentrations.

Evidence is presented that in Acinetobacter calcoaceticus oxidation of glucose to gluconate by the periplasmic quinoprotein glucose dehydrogenase (EC 1 . 1 .99.17) leads to energy conservation. Membrane vesicles prepared from cells grown in carbon-limited chemostat culture exhibited (1) a high rate of glucose-dependent oxygen consumption and gluconate production, (2) glucosemediated cytochrome reduction, (3) uncoupler sensitive, glucose-dependent generation of a membrane potential and (4) glucose-driven accumulation of amino acids. Furthermore, oxidation of glucose to gluconate by whole cells was associated with ATP synthesis. These results confirm and extend previous observations that periplasmic glucose oxidation can act as a driving force for energy-requiring processes. It is therefore concluded that the incomplete oxidation of glucose by bacteria may serve as an auxiliary energy-generating system.