High cell density cultivation of recombinant E. coli for hirudin variant 1 production by temperature shift controlled by pUC18-based replicative origin

Hirudin variants production by genetic engineered microbial factory

Hirudin was discovered as an active anticoagulant in leech extracts almost 60 years ago. Since their initial discovery, hirudin and its variants have been produced with various anti-thrombotic, cancer cell inhibition, diabetic cataract treatment and anti-fatigue activities. Some hirudin variants have been approved for clinical use and released into the marketplace. Recent progress has seen made in relation to hirudin variants expressed in several well-established microbial hosts, including Escherichia coli, Saccharomyces cerevisiae, Pichia pastoris and others, with high levels of activity and yield. This review summarizes the current progress on hirudin production using microbial producers, and considers the outlook for future development.

The production of a recombinant tandem single chain fragment variable capable of binding prolamins triggering celiac disease

Background

Celiac disease (CD) is one of the most common food-related chronic disorders. It is mediated by the dietary consumption of prolamins, which are storage proteins of different grains. So far, no therapy exists and patients are bound to maintain a lifelong diet to avoid symptoms and long-term complications. To support those patients we developed a tandem single chain Fragment variable (tscFv) acting as a neutralizing agent against prolamins. We recombinantly produced this molecule in E. coli, but mainly obtained misfolded product aggregates, so-called inclusion bodies, independent of the cultivation strategy we applied.

Results

In this study, we introduce this novel tscFv against CD and present our strategy of obtaining active product from inclusion bodies. The refolded tscFv shows binding capabilities towards all tested CD-triggering grains. Compared to a standard polyclonal anti-PT-gliadin-IgY, the tscFv displays a slightly reduced affinity towards digested gliadin, but an additional affinity towards prolamins of barley.

Conclusion

The high binding specificity of tscFv towards prolamin-containing grains makes this novel molecule a valuable candidate to support patients suffering from CD in the future.

Electronic supplementary material

The online version of this article (10.1186/s12896-018-0443-0) contains supplementary material, which is available to authorized users.

High cell density cultivation of recombinant Escherichia coli strains expressing 2-O-sulfotransferase and C5-epimerase for the production of bioengineered heparin

Bioengineered heparin is being investigated as a potential substitute for the animal-sourced anticoagulant drug. One step in the current process to prepare bioengineered heparin involves the conversion of N-sulfo heparosan, rich in → 4)GlcNS(1 → 4) GlcA(1 → sequences (where S is sulfo, GlcN is α-D-glucosamine, and GlcA is β-D-glucuronic acid), to a critical intermediate, rich in → 4)GlcNS(1 → 4) IdoA2S(1 → sequences (where S is sulfo and IdoA is α-L-iduronic acid), using 2-O-sulfotransferase (2-OST) and C5 epimerase (C5-epi). Until now, these heparan sulfate biosynthetic enzymes have been expressed in Escherichia coli grown in shake flask culture as fusion proteins. The current study is focused on the high cell density fed-batch cultivation of recombinant E. coli strains expressing both enzymes. We report the high productivity expression of active 2-OST and C5-epi enzymes of 6.0 and 2.2 mg/g dry cell weight, respectively.

Robust preparative-scale extracellular production of hirudin in Escherichia coli and its purification and characterization

Hirudin variant III (HV3) is potentially useful in the prevention and treatment of cataracts. To prepare sufficient amounts of rHV3 for further preclinical studies, we developed an effective process for robust preparative-scale extracellular production of rHV3 in Escherichia coli. In a 7-l bioreactor, under the optimal fed-batch fermentation conditions, rHV3 was excreted into the culture supernatant and yielded up to 915 mg l(-1). Then, a four-step purification procedure was applied to the product, which included ultrafiltration, hydrophobic chromatography, anion-exchange chromatography, and preparative reversed-phase fast protein liquid chromatography (FPLC). The overall maximum recovery attained was 56 %, the purity reached at least 99 % as evaluated by HPLC analysis, the molecular weight was determined to be 7,011.10 Da by matrix-assisted laser-desorption time-of-flight mass spectrometry (MALDI-TOF/MS) analysis, and the pI was 4.46 as analyzed by isoelectric focusing. The N- and C-terminal sequence analysis confirmed the product homogeneity. The final product contained at most 10 pg of residual DNA per dose (0.2 mg) of rHV3 by high-sensitivity hybridization assay and at most 3 EU endotoxin protein/mg by limulus amebocyte lysate assay. Taken together, the rHV3 produced in multigram quantities in E. coli by this bioprocess meets the regulatory criteria for biopharmaceuticals and can be used as a drug candidate for preclinical studies.

Optimized culture conditions for the efficient production of porcine adenylate kinase in recombinant Escherichia coli

Temperature shift cultivations with amino acid supplementation were optimized to produce porcine adenylate kinase (ADK) in recombinant Escherichia coli harboring a pUC-based recombinant plasmid under the control of the trp promoter. With regard to temperature control, the culture condition was initially maintained at 35 degrees C for cellular growth, but ADK expression was suppressed until the late logarithmic growth phase; subsequently, a temperature shift was applied (from 35 degrees C to 42 degrees C), which resulted in maximal ADK production. In addition, supplementation of amino acids, especially valine and leucine, during the temperature shift stimulated ADK expression from 3.5% to 9.2% and 8.6% of the total protein, respectively. After optimization, 1 g ADK per liter was produced within 16 h of cultivation with a dry cell weight of 21.8 g/l. In this system, there was no loss of the recombinant plasmid during cultivation without selective pressure.