Carboxylic acid consumption and production by Corynebacterium glutamicum.

Corynebacterium glutamicum is well-known as an industrial workhorse, most notably for its use in the bulk production of amino acids in the feed and food sector. Previous studies of the effect of gradients in scale-down reactors with complex media disclosed an accumulation of several carboxylic acids and a parallel decrease of growth and product accumulation. This study, therefore, addresses the impact of carboxylic acids, for example, acetate and l-lactate, on the cultivation of the cadaverine producing strain C. glutamicum DM1945Δact3:Ptuf -ldcCopt and their potential role in scale up related performance losses. A fluctuating power input in shake flask and stirred tank cultivations with mineral salt was applied to mimic discontinuous oxygen availability. Results demonstrate, whenever sufficient oxygen was available, C. glutamicum recovered from previously occurring stressful conditions like an oxygen limiting phase. Reassimilation of acids was detected simultaneously. In cultures, which were supplemented with either acetate or l-lactate, a rapid cometabolization of both acids in presence of glucose was observed, showing conversion rates of 7.8 and 3.8 mmol gcell dry weight-1 hr-1 , respectively. Uptake of these acids was accompanied by increased oxygen consumption. Proteins related to oxidative stress response, glycogen synthesis, and the main carbon metabolism were found in altered concentrations under oscillatory cultivation conditions. (Proteomics data are available via ProteomeXchange with identifier PXD012760). Virtually no impact on growth or product formation was observed. We conclude that the reduced growth and product formation in scale-down cultivations when complex media was used is not caused by the accumulation of carboxylic acids.

Catalytically active inclusion bodies of L-lysine decarboxylase from E. coli for 1,5-diaminopentane production.

Sustainable and eco-efficient alternatives for the production of platform chemicals, fuels and chemical building blocks require the development of stable, reusable and recyclable biocatalysts. Here we present a novel concept for the biocatalytic production of 1,5-diaminopentane (DAP, trivial name: cadaverine) using catalytically active inclusion bodies (CatIBs) of the constitutive L-lysine decarboxylase from E. coli (EcLDCc-CatIBs) to process L-lysine-containing culture supernatants from Corynebacterium glutamicum. EcLDCc-CatIBs can easily be produced in E. coli followed by a simple purification protocol yielding up to 43% dry CatIBs per dry cell weight. The stability and recyclability of EcLDCc-CatIBs was demonstrated in (repetitive) batch experiments starting from L-lysine concentrations of 0.1 M and 1 M. EcLDC-CatIBs exhibited great stability under reaction conditions with an estimated half-life of about 54 h. High conversions to DAP of 87-100% were obtained in 30-60 ml batch reactions using approx. 180-300 mg EcLDCc-CatIBs, respectively. This resulted in DAP titres of up to 88.4 g l-1 and space-time yields of up to 660 gDAP l-1 d-1 per gram dry EcLDCc-CatIBs. The new process for DAP production can therefore compete with the currently best fermentative process as described in the literature.

pH fluctuations imperil the robustness of C. glutamicum to short term oxygen limitation.

The presence of complex gradients for, e.g., nutrients, oxygen or pH in industrial scale fed batch processes are a major challenge for process performance. To consider such impact of scale-up during laboratory scale process development, scale-down bioreactor simulation, i.e. mimicking inhomogeneous conditions, became the method of choice. However, most scale-down studies simulate combined inhomogeneities of more than one parameter, so that the impact of the individual parameters remains unclear. The presented scale down study addresses this challenge by separating the influence of glucose, pH and oxygen fluctuations in terms of their specific impact in a well-established two compartment scale down device. This was carried out for an 1,5-diaminopentane production process using the industrial production host Corynebacterium glutamicum. Strikingly, oxygen depletion alone showed no effect on the process performance while changes of only one pH unit in acidic as well as alkaline direction reduced the biomass and product formation. Even more pronounced phenotypes up to -13% of µ and -39% of YX/S were observed, when an oscillatory acidic pH shift was combined with dissolved oxygen fluctuations. These losses are accompanied by a missing regulation of fermentative pathways. In conclusion, large-scale C. glutamicum processes seem to be most sensitive to pH variation.

Metabolic profile of 1,5-diaminopentane producing Corynebacterium glutamicum under scale-down conditions: Blueprint for robustness to bioreactor inhomogeneities.

Performance losses during scale-up are described since decades, but are still one of the major obstacles for industrial bioprocess development. Consequently, robustness to inhomogeneous cultivation environments is an important quality of industrial production organisms. Especially, Corynebacterium glutamicum was proven to have an outstanding resistance against rapid changes of oxygen and substrate availability as occurring in industrial scale bioreactors. This study focuses on the identification of metabolic key mechanisms for this robustness to get a deeper insight and provide future targets for process orientated strain development. A 1,5-diaminopentane producing C. glutamicum strain was cultivated in a two compartment scale-down device to create short-term environmental changes simulating industrial scale cultivation conditions. Using multi omics based methods, it is shown, that central metabolism is flexibly rearranged under short-term oxygen depletion and carbon source excess to overcome shortage in NAD+ recycling. In order to balance the redox state, key enzymes for the non-oxygen dependent fermentative NAD+ regeneration were significantly up-regulated while parts of non-essential pathways were down-regulated. The transfer of the cells back into the well aerated zones with low substrate concentration triggers an additional upregulation of genes for the re-assimilation of previously formed side products, showing L-lactate forming and utilizing reactions being active at the same time. Especially L-lactate as reversible and flexible external buffer for carbon and redox equivalents puts C. glutamicum in a robust position to deal with inhomogeneity in large scale processes. Biotechnol. Bioeng. 2017;114: 560-575. © 2016 Wiley Periodicals, Inc.