Caspase-2 is the most specific protease of all caspases and therefore highly suitable as tag removal enzyme creating an authentic N-terminus of overexpressed tagged proteins of interest. The wild type human caspase-2 is a dimer of heterodimers generated by autocatalytic processing which is required for its enzymatic activity. We designed a circularly permuted caspase-2 (cpCasp2) to overcome the drawback of complex recombinant expression, purification and activation, cpCasp2 was constitutively active and expressed as a single chain protein. A 22 amino acid solubility tag and an optimized fermentation strategy realized with a model-based control algorithm further improved expression in Escherichia coli and 5.3 g/L of cpCasp2 in soluble form were obtained. The generated protease cleaved peptide and protein substrates, regardless of N-terminal amino acid with high activity and specificity. Edman degradation confirmed the correct N-terminal amino acid after tag removal, using Ubiquitin-conjugating enzyme E2 L3 as model substrate. Moreover, the generated enzyme is highly stable at −20 °C for one year and can undergo 25 freeze/thaw cycles without loss of enzyme activity. The generated cpCasp2 possesses all biophysical and biochemical properties required for efficient and economic tag removal and is ready for a platform fusion protein process.

We report a novel plastidic NAD-dependent malate dehydrogenase (EC 1.1.1.37), which is not redox-regulated in contrast to its NADP-specific counterpart (EC 1.1.1.82). Analysis of isoenzyme patterns revealed a single NAD-MDH associated with highly purified chloroplasts isolated from Arabidopsis and spinach. A cDNA clone encoding the novel enzyme was found in the Arabidopsis EST data base by sorting all putative clones for NAD-dependent malate dehydrogenase. A derived amino acid sequence is very similar to mitochondrial and peroxisomal NAD-MDHs within the region coding for the mature protein but possesses a 80-amino acid long N-terminal domain with typical characteristics of a chloroplast transit peptide. In vitro synthesized labeled precursor protein was imported into the stroma of spinach chloroplasts and processed to a mature enzyme subunit of 34 kDa. Expressed in Escherichia coli, the recombinant enzyme exhibited the same distinctive isoelectric point of 5.35 as the original enzyme from Arabidopsis chloroplasts. Northern analysis revealed that the protein is expressed in both autotrophic and heterotrophic tissues. The findings reported here indicate that the "malate valve" operates not only in the illuminated chloroplasts but also in dark chloroplasts and in heterotrophic plastids and is therefore a general mechanism to maintain the optimal ratio between ATP and reducing equivalents in plastids.

Process analytical technology combines understanding and control of the process with real‐time monitoring of critical quality and performance attributes. The goal is to ensure the quality of the final product. Currently, chromatographic processes in biopharmaceutical production are predominantly monitored with UV/Vis absorbance and a direct correlation with purity and quantity is limited. In this study, a chromatographic workstation was equipped with additional online sensors, such as multi‐angle light scattering, refractive index, attenuated total reflection Fourier‐transform infrared, and fluorescence spectroscopy. Models to predict quantity, host cell proteins (HCP), and double‐stranded DNA (dsDNA) content simultaneously were developed and exemplified by a cation exchange capture step for fibroblast growth factor 2 expressed in Escherichia coliOnline data and corresponding offline data for product quantity and co‐eluting impurities, such as dsDNA and HCP, were analyzed using boosted structured additive regression. Different sensor combinations were used to achieve the best prediction performance for each quality attribute. Quantity can be adequately predicted by applying a small predictor set of the typical chromatographic workstation sensor signals with a test error of 0.85 mg/ml (range in training data: 0.1–28 mg/ml). For HCP and dsDNA additional fluorescence and/or attenuated total reflection Fourier‐transform infrared spectral information was important to achieve prediction errors of 200 (2–6579 ppm) and 340 ppm (8–3773 ppm), respectively.

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BACKGROUND: Recombinant proteins produced for use as biopharmaceuticals need to harbor their native N-terminus. A drawback in expression of recombinant proteins as fusion proteins with an affinity fusion-tag is that enzymatic or chemical processing is required to trim the artificial tag and release the true protein of interest. In many cases, however, this processing step generates an incorrect N-terminus.RESULTS: Human fibroblast growth factor 2 (FGF2) was expressed as a fusion protein in Escherichia coli fed-batch cultivations. The protein of interest (POI) carried an N-terminal affinity fusion-tag which enabled purification via affinity chromatography. After enzymatic removal of the affinity fusion-tag with a circularly permuted human caspase-2 (cpCasp2), the POI was further purified using subtractive affinity chromatography. Mass spectrometric analysis confirmed the authentic N-terminus of the POI. The generated POI was highly pure with 42 ppm host cell protein, 3.7 ∼g mL −1 dsDNA and ∼ 1000 EU mL −1 endotoxin. Only a small number of E. coli host cell proteins were co-purified with the POI. Because of the high specificity of the novel protease cpCasp2, no off-target cleavage could be observed. CONCLUSION: Our findings demonstrate that cpCasp2 can be used for the production of native proteins using a fusionprotein process. This represents a first case study at large laboratory scale for the production of an industrially relevant protein. This technology constitutes the basis of a highly scalable cpCasp2-based platform fusion protein process (CASPON technology) purification platform.

A typical soybean (Glycine max) plant assimilates nitrogen rapidly both in active root nodules and in developing seeds and pods. Oxaloacetate and 2-ketoglutarate are major acceptors of ammonia during rapid nitrogen assimilation. Oxaloacetate can be derived from the tricarboxylic acid (TCA) cycle, and it also can be synthesized from phosphoenolpyruvate and carbon dioxide by phosphoenolpyruvate carboxylase. An active malate dehydrogenase is required to facilitate carbon flow from phosphoenolpyruvate to oxaloacetate. We report the cloning and sequence analyses of a complete and novel malate dehydrogenase gene in soybean. The derived amino acid sequence was highly similar to the nodule-enhanced malate dehydrogenases from Medicago sativa and Pisum sativum in terms of the transit peptide and the mature subunit (i.e., the functional enzyme). Furthermore, the mature subunit exhibited a very high homology to the plastid-localized NAD-dependent malate dehydrogenase from Arabidopsis thaliana, which has a completely different transit peptide. In addition, the soybean nodule-enhanced malate dehydrogenase was abundant in both immature soybean seeds and pods. Only trace amounts of the enzyme were found in leaves and nonnodulated roots. In vitro synthesized labeled precursor protein was imported into the stroma of spinach chloroplasts and processed to the mature subunit, which has a molecular mass of ∼34 kDa. We propose that this new malate dehydrogenase facilitates rapid nitrogen assimilation both in soybean root nodules and in developing soybean seeds, which are rich in protein. In addition, the complete coding region of a geranylgeranyl hydrogenase gene, which is essential for chlorophyll synthesis, was found immediately upstream from the new malate dehydrogenase gene.

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A simultaneous crystallization and aqueous two-phase extraction of a single chain antibody was developed, demonstrating process integration. The process conditions were designed to form an aqueous two-phase system, and to favor crystallization, using sodium sulfate and PEG-2000. At sufficiently high concentrations of PEG, a second phase was generated in which the protein crystallization occurred simultaneously. The single chain antibody crystals were partitioned to the top, polyethylene glycol-rich phase. The crystal nucleation took place in the sodium sulfate-rich phase and at the phase boundary, whereas crystal growth was progressing mainly in the polyethylene glycol-rich phase. The crystals in the polyethylene glycol-rich phase grew to a size of >50 µm. Additionally, polyethylene glycol acted as an anti-solvent, thus, it influenced the crystallization yield. A phase diagram with an undersaturation zone, crystallization area, and amorphous precipitation zone was established. Only small differences in polyethylene glycol concentration caused significant shifts of the crystallization yield. An increase of the polyethylene glycol content from 2% (w/v) to 4% (w/v) increased the yield from approximately 63-87%, respectively. Our results show that crystallization in aqueous two-phase systems is an opportunity to foster process integration.