Joe Max Risse

Factors that influence the extracellular expression of streptavidin in Escherichia coli using a bacteriocin release protein

Aiming to increase production of recombinant streptavidin in Escherichia coli, the effect of different leader sequences, different promoter strengths of the bacteriocin release protein (kil), host strain and medium composition on the expression and secretion into the medium was investigated. Expression vectors containing an expression or secretion unit were constructed with different combinations of leader sequence for the streptavidin gene and promoters for the kil gene and streptavidin gene. Results showed that a high-level extracellular production of streptavidin could be accomplished with E. coli BL21(DE3) by using the leader sequence of the phoA gene, a strong stationary-phase promoter for the kil gene and supplementation of the medium by glycine. Using a stationary-phase promoter for the expression of streptavidin had a negative effect.

Applicability of Euglena gracilis for biorefineries demonstrated by the production of α-tocopherol and paramylon followed by anaerobic digestion.

In this study the use of Euglena gracilis biomass for α-tocopherol, paramylon and biogas production in a value-added chain was investigated. Therefore, we analyzed the dry cell weight and product concentrations at different growth phases during heterotrophic, photoheterotrophic and photoautotrophic cultivation in a low-cost minimal medium. Furthermore, the specific biogas yields for differently derived biomass with and without product recovery were investigated. We demonstrate that growth phase and cultivation mode not only have a significant impact on product formation, but also influence the yield of biogas obtained from anaerobic digestion of Euglena gracilis biomass. The maximum dry cell weight concentration ranged from 12.3±0.14gL(-1) for heterotrophically to 3.4±0.02gL(-1) for photoautotrophically grown Euglena gracilis cells. The heterotrophically grown biomass accumulated product concentrations of 5.3±0.12mgL(-1) of α-tocopherol and 9.3±0.1gL(-1) of paramylon or 805±10.9mL of biogasgvs(-1) (per gram volatile solids). The results for photoautotrophically grown cells were 8.6±0.22mgL(-1) of α-tocopherol and 0.78±0.01gL(-1) of paramylon or 648±7.2mL of biogasgvs(-1). For an energy-saving downstream procedure the extracting agent methanol does not have to be removed strictly. Samples with residual methanol showed a significantly increased biogas yield, because the solvent can be used as an additional substrate for methane production by archaebacteria.

Fermentative production of L-pipecolic acid from glucose and alternative carbon sources.

Corynebacterium glutamicum is used for the million-ton scale production of amino acids and has recently been engineered for production of the cyclic non-proteinogenic amino acid L-pipecolic acid (L-PA). In this synthetic pathway L-lysine was converted to L-PA by oxidative deamination, dehydration and reduction by L-lysine 6-dehydrogenase (deaminating) from Silicibacter pomeroyi and pyrroline 5-carboxylate reductase from C. glutamicum. However, production of L-PA occurred as by-product of L-lysine production only. Here, the author show that abolishing L-lysine export by the respective gene deletion resulted in production of L-PA as major product without concomitant lysine production while the specific growth rate was reduced due to accumulation of high intracellular lysine concentrations. Increasing expression of the genes encoding L-lysine 6-dehydrogenase and pyrroline 5-carboxylate reductase in C. glutamicum strain PIPE4 increased the L-PA titer to 3.9 g L-1 , and allowed faster growth and, thus, a higher volumetric productivity of 0.08 ± 0.00 g L-1 h-1 respectively. Secondly, expression of heterologous genes for utilization of glycerol, xylose, glucosamine, and starch in strain PIPE4 enabled L-PA production from these alternative carbon sources. Third, in a glucose/sucrose-based fed-batch fermentation with C. glutamicum PIPE4 L-PA was produced to a titer of 14.4 g L-1 with a volumetric productivity of 0.21 g L-1 h-1 and an overall yield of 0.20 g g-1 .

Development of fed-batch strategies for the production of streptavidin by Streptomyces avidinii based on power input and oxygen supply studies

Streptavidin is a tetrameric protein with an extremely high affinity to biotin and different biotin-like peptide-tags. This characteristic causes its widespread use in biotechnology. Streptavidin is produced by the fermentation of wild type Streptomyces avidinii or by recombinant Streptomyces lavendulae, Escherichia coli, and Bacillus subtilis strains. However, little is known about the influence of power input and oxygen supply as well as feeding strategies on the production of streptavidin by S. avidinii. This paper provides a systematic analysis of the effect of rotary frequency of the stirrer, leading to a plateau-like streptavidin formation behaviour between 400 and 700 min(-1). This plateau was characterized by specific power inputs between 79 and 107 W L(-1) and corresponding maximal product concentrations of 6.90 μM in 6 days. Lower as well as higher rotary frequencies were not beneficial. Subsequently, a linear fed-batch procedure could be established reproducibly yielding 39.20 μM streptavidin in 14 days, characterized by a constant productivity of 114 nM h(-1). Fed-batch procedures based on dissolved oxygen were less efficient. The linear feeding strategy presented in this paper led to the highest streptavidin concentration ever reported and exceeded the maximal product level given in the literature drastically by a factor of 8.5.

Dependency of the fatty acid composition of Euglena gracilis on growth phase and culture conditions

Usually, the fatty acid (FA) composition of lipids from microalgae is determined using samples taken at a single time point only, often without considering the medium composition and cultivation conditions. Therefore, the results only represent the FA composition of cells in a certain growth phase. Furthermore, they may misrepresent the capability of the organism to produce certain FA or lipid mixtures. In this study, 22 FA were analysed quantitatively during the cultivation of Euglena gracilis under different cultivation modes and conditions. For cell growth, various media compositions for heterotrophic and photoheterotrophic conditions were used. Results of extensive FA analysis allowed the determination of appropriate cultivation conditions and durations for yielding lipid mixtures with optimal composition, e.g. for the production of biodiesel or functional food. Drastic differences in the ratio between n3- and n6-polyunsaturated fatty acid (PUFA) ranging from 0.04 to 1.81 were detected. This effect was strongly influenced by the cultivation mode. In addition, media with higher nitrogen concentration resulted in a higher n3/n6-PUFA-ratio as well as improved specific growth rates for all analysed combinations of glucose and nitrogen concentrations. Furthermore, it was demonstrated that the inexpensive proteose peptone medium is ideal for lipid production by E. gracilis. This work provides valuable tools to optimise yield, productivity and n3/n6-PUFA ratio concerning the cultivation of E. gracilis as well as potentially other microalgae in general.

Fed-batch production and secretion of streptavidin by Hansenula polymorpha: Evaluation of genetic factors and bioprocess development

Streptavidin - a protein secreted by the filamentous bacterium Streptomyces avidinii - is applied in a variety of methods, leading to numerous studies on its heterologous production. Development and characterization of a novel expression system for streptavidin genes by Hansenula polymorpha is described utilizing different target gene variants along with the two methanol-inducible promoters PMOX and PFMD. Extracellular product concentrations were higher for cultivation at 30 instead of 37°C. The best performing strain carrying the full-length streptavidin gene under control of PFMD was characterized in the bioreactor applying a synthetic medium and oxygen-controlled feeding of glucose. Derepression resulted in an extracellular concentration of 1.31±0.07μM of tetrameric streptavidin after 48h (27.3nMh(-1)). Feeding of glycerol improved biomass formation, but lowered the product concentration. By combining derepression and methanol induction the final extracellular streptavidin concentration increased to 11.42±0.22μM (approx. 751mgL(-1)), yielding a productivity of 52.5nMh(-1). Despite supplementing biotin the proportion of biotin-blocked binding sites in the supernatant dropped from 54.4±5.0 % after 18h to 17.2±6.5 % towards the end of glucose feeding to a final value of 1.1±3.8 %, indicating a highly bioactive product. Thus, H. polymorpha proved to be a suitable host for the production of streptavidin.

Model‐based development of an assay for the rapid detection of biotin‐blocked binding sites of streptavidin

The protein streptavidin (SAV) is applied in a large variety of molecular methods due to an extraordinarily strong binding to the vitamin biotin (BIO). The protein structure is homotetrameric, characterized by one binding site for BIO per subunit. Therefore, one of the major criteria to determine the quality of SAV isolates is the proportion of BIO‐blocked binding sites per tetramer. A rapid analysis of BIO‐free binding sites is achieved by fluorescence quenching of biotin‐4‐fluorescein (B4F). However, BIO‐blocked binding sites can only be determined by costly and laborious procedures such as ELISA‐based methods or radioactive labeling. This study describes the systematic, model‐supported development of a method for the quick and simple detection of BIO‐blocked binding sites, based on a short‐term heat incubation of the sample in the presence of B4F. Kinetic modeling and parameter estimation yielded dissociation constants of 1.22 ± 0.27 × 10−11 M for the complex SAV–BIO and 5.16 ± 0.70 × 10−13 M for SAV–B4F at 70°C, allowing a displacement of SAV‐bound BIO by B4F. This method allows the rapid monitoring of BIO‐blocked binding sites in fermentation processes, independent from the chain length of SAV and the concentration of contaminating proteins, e.g. when optimizing the BIO concentration in cultivation media.

Patchoulol Production with Metabolically Engineered Corynebacterium glutamicum.

Patchoulol is a sesquiterpene alcohol and an important natural product for the perfume industry. Corynebacterium glutamicum is the prominent host for the fermentative production of amino acids with an average annual production volume of ~6 million tons. Due to its robustness and well established large-scale fermentation, C. glutamicum has been engineered for the production of a number of value-added compounds including terpenoids. Both C40 and C50 carotenoids, including the industrially relevant astaxanthin, and short-chain terpenes such as the sesquiterpene valencene can be produced with this organism. In this study, systematic metabolic engineering enabled construction of a patchoulol producing C. glutamicum strain by applying the following strategies: (i) construction of a farnesyl pyrophosphate-producing platform strain by combining genomic deletions with heterologous expression of ispA from Escherichia coli; (ii) prevention of carotenoid-like byproduct formation; (iii) overproduction of limiting enzymes from the 2-c-methyl-d-erythritol 4-phosphate (MEP)-pathway to increase precursor supply; and (iv) heterologous expression of the plant patchoulol synthase gene PcPS from Pogostemon cablin. Additionally, a proof of principle liter-scale fermentation with a two-phase organic overlay-culture medium system for terpenoid capture was performed. To the best of our knowledge, the patchoulol titers demonstrated here are the highest reported to date with up to 60 mg L−1 and volumetric productivities of up to 18 mg L−1 d−1.

GAP promoter-based fed-batch production of highly bioactive core streptavidin by Pichia pastoris.

Streptavidin is a homotetrameric protein binding the vitamin biotin and peptide analogues with an extremely high affinity, which leads to a large variety of applications. The biotin‐auxotrophic yeast Pichia pastoris has recently been identified as a suitable host for the expression of the streptavidin gene, allowing both high product concentrations and productivities. However, so far only methanol‐based expression systems have been applied, bringing about increased oxygen demand, strong heat evolution and high requirements for process safety, causing increased cost. Moreover, common methanol‐based processes lead to large proportions of biotin‐blocked binding sites of streptavidin due to biotin‐supplemented media. Targeting these problems, this paper provides strategies for the methanol‐free production of highly bioactive core streptavidin by P. pastoris under control of the constitutive GAP promoter. Complex were superior to synthetic production media regarding the proportion of biotin‐blocked streptavidin. The optimized, easily scalable fed‐batch process led to a tetrameric product concentration of up to 4.16 ± 0.11 µM of biotin‐free streptavidin and a productivity of 57.8 nM h−1 based on constant glucose feeding and a successive shift of temperature and pH throughout the cultivation, surpassing the concentration in un‐optimized conditions by a factor of 3.4. Parameter estimation indicates that the optimized conditions caused a strongly increased accumulation of product at diminishing specific growth rates (μ ≈ D < 0.01 h−1), supporting the strategy of feeding.

One-step process for production of N -methylated amino acids from sugars and methylamine using recombinant Corynebacterium glutamicum as biocatalyst

N-methylated amino acids are found in Nature in various biological compounds. N-methylation of amino acids has been shown to improve pharmacokinetic properties of peptide drugs due to conformational changes, improved proteolytic stability and/or higher lipophilicity. Due to these characteristics N-methylated amino acids received increasing interest by the pharmaceutical industry. Syntheses of N-methylated amino acids by chemical and biocatalytic approaches are known, but often show incomplete stereoselectivity, low yields or expensive co-factor regeneration. So far a one-step fermentative process from sugars has not yet been described. Here, a one-step conversion of sugars and methylamine to the N-methylated amino acid N-methyl-l-alanine was developed. A whole-cell biocatalyst was derived from a pyruvate overproducing C. glutamicum strain by heterologous expression of the N-methyl-l-amino acid dehydrogenase gene from Pseudomonas putida. As proof-of-concept, N-methyl-l-alanine titers of 31.7 g L−1 with a yield of 0.71 g per g glucose were achieved in fed-batch cultivation. The C. glutamicum strain producing this imine reductase enzyme was engineered further to extend this green chemistry route to production of N-methyl-l-alanine from alternative feed stocks such as starch or the lignocellulosic sugars xylose and arabinose.