Bioreactor Culture Research Articles

Bioreactor Systems for Plant Cell Cultivation at the Institute of Plant Physiology of the Russian Academy of Sciences: 50 Years of Technology Evolution from Laboratory to Industrial Implications.

The cultivation of plant cells in large-scale bioreactor systems has long been considered a promising alternative for the overexploitation of wild plants as a source of bioactive phytochemicals. This idea, however, faced multiple constraints upon realization, resulting in very few examples of technologically feasible and economically effective biotechnological companies. The bioreactor cultivation of plant cells is challenging. Even well-growing and highly biosynthetically potent cell lines require a thorough optimization of cultivation parameters when upscaling the cultivation process from laboratory to industrial volumes. The optimization includes, but is not limited to, the bioreactor's shape and design, cultivation regime (batch, fed-batch, continuous, semi-continuous), aeration, homogenization, anti-foaming measures, etc., while maintaining a high biomass and metabolite production. Based on the literature data and our experience, the cell cultures often demonstrate cell line- or species-specific responses to parameter changes, with the dissolved oxygen concentration (pO2) and shear stress caused by stirring being frequent growth-limiting factors. The mass transfer coefficient also plays a vital role in upscaling the cultivation process from smaller to larger volumes. The Experimental Biotechnological Facility at the K.A. Timiryazev Institute of Plant Physiology has operated since the 1970s and currently hosts a cascade of bioreactors from the laboratory (20 L) to the pilot (75 L) and a semi-industrial volume (630 L) adapted for the cultivation of plant cells. In this review, we discuss the most appealing cases of the cell cultivation process's adaptation to bioreactor conditions featuring the cell cultures of medicinal plants Dioscorea deltoidea Wall. ex Griseb., Taxus wallichiana Zucc., Stephania glabra (Roxb.) Miers, Panax japonicus (T. Nees) C.A.Mey., Polyscias filicifolia (C. Moore ex E. Fourn.) L.H. Bailey, and P. fruticosa L. Harms. The results of cell cultivation in bioreactors of different types and designs using various cultivation regimes are covered and compared with the literature data. We also discuss the role of the critical factors affecting cell behavior in bioreactors with large volumes.

Multifactorial analysis of terminator performance on heterologous gene expression in Physcomitrella

Key messageCharacterization of Physcomitrella 3′UTRs across different promoters yields endogenous single and double terminators for usage in molecular pharming.The production of recombinant proteins for health applications accounts for a large share of the biopharmaceutical market. While many drugs are produced in microbial and mammalian systems, plants gain more attention as expression hosts to produce eukaryotic proteins. In particular, the good manufacturing practice (GMP)-compliant moss Physcomitrella (Physcomitrium patens) has outstanding features, such as excellent genetic amenability, reproducible bioreactor cultivation, and humanized protein glycosylation patterns. In this study, we selected and characterized novel terminators for their effects on heterologous gene expression. The Physcomitrella genome contains 53,346 unique 3′UTRs (untranslated regions) of which 7964 transcripts contain at least one intron. Over 91% of 3′UTRs exhibit more than one polyadenylation site, indicating the prevalence of alternative polyadenylation in Physcomitrella. Out of all 3′UTRs, 14 terminator candidates were selected and characterized via transient Dual-Luciferase assays, yielding a collection of endogenous terminators performing equally high as established heterologous terminators CaMV35S, AtHSP90, and NOS. High performing candidates were selected for testing as double terminators which impact reporter levels, dependent on terminator identity and positioning. Testing of 3′UTRs among the different promoters NOS, CaMV35S, and PpActin5 showed an increase of more than 1000-fold between promoters PpActin5 and NOS, whereas terminators increased reporter levels by less than tenfold, demonstrating the stronger effect promoters play as compared to terminators. Among selected terminator attributes, the number of polyadenylation sites as well as polyadenylation signals were found to influence terminator performance the most. Our results improve the biotechnology platform Physcomitrella and further our understanding of how terminators influence gene expression in plants in general.

Transitioning from static to suspension culture system for large-scale production of xeno-free extracellular vesicles derived from mesenchymal stromal cells.

Extracellular vesicles (EVs) derived from mesenchymal stromal cells (MSCs) have shown increasing therapeutic potential in the last years. However, large production of EV is required for therapeutic purposes. Thereby, scaling up MSC cultivation in bioreactors is essential to allow culture parameters monitoring. In this study, we reported the establishment of a scalable bioprocess to produce MSC-EV in suspension cultures using spinner flasks and human collagen-coated microcarriers (3D culture system). We compared the EV production in this 3D culture system with the standard static culture using T-flasks (2D culture system). The EV produced in both systems were characterized and quantify by western blotting and nanoparticle tracking analysis. The presence of the typical protein markers CD9, CD63, and CD81 was confirmed by western blotting analyses for EV produced in both culture systems. The cell fold-increase was 5.7-fold for the 3D culture system and 4.6-fold for the 2D culture system, signifying a fold-change of 1.2 (calculated as the ratio of fold-increase 3D to fold-increase 2D). Furthermore, it should be noted that the total cell production in the spinner flask cultures was 4.8 times higher than that in T-flask cultures. The total cell production in the spinner flask cultures was 5.2-fold higher than that in T-flask cultures. While the EV specific production (particles/cell) in T-flask cultures (4.40 ± 1.21 × 108 particles/mL, p < 0.05) was higher compared to spinner flask cultures (2.10 ± 0.04 × 108 particles/mL, p < 0.05), the spinner flask culture system offers scalability, making it capable of producing enough MSC-EV at a large scale for clinical applications. Therefore, we concluded that 3D culture system evaluated here serves as an efficient transitional platform that enables the scaling up of MSC-EV production for therapeutic purposes by utilizing stirred tank bioreactors and maintaining xeno-free conditions.

A new β-galactosidase from Paenibacillus wynnii with potential for industrial applications

Commercial β-galactosidases exhibit undesirable kinetic properties regarding substrate affinity (Michaelis-Menten constant [KM] for lactose) and product inhibition (inhibitor constant [Ki] for galactose). An in silico screening of gene sequences was done and identified a putative β-galactosidase (Paenibacillus wynnii β-galactosidase, BgaPw) from the psychrophilic bacterium Paenibacillus wynnii. The cultivation of the wild-type P. wynnii strain resulted in very low β-galactosidase activities of a maximum of 150 nkat per liter of medium with o-nitrophenyl-β-d-galactopyranoside (oNPGal) as substrate. The recombinant production of BgaPw in Escherichia coli BL21(DE3) increased the yield ∼9,000-fold. Here, a volumetric activity of 1,350.18 ± 11.82 μkatoNPGal/Lculture was achieved in a bioreactor cultivation. The partly purified BgaPw showed a pH optimum at 7.0, a temperature maximum at 40°C, and an excellent stability at 8°C with a half-life of 77 d. Kinetic studies with BgaPw were done in milk or in milk-imitating synthetic buffer (Novo buffer), respectively. Remarkably, the KM value of BgaPw with lactose was as low as 0.63 ± 0.045 mM in milk. It was found that the resulting products of lactose hydrolysis, namely galactose and glucose, did not inhibit the β-galactosidase activity of BgaPw, but instead showed a striking activating effect in both cases (up to 144%). In a comparison study in milk, lactose was completely hydrolyzed by BgaPw in 72 h at 8°C, whereas 2 other known β-galactosidases were less powerful and converted only about 90% of lactose in the same time. Finally, the formation of galactooligosaccharides (GOS) was demonstrated with the new BgaPw, starting with pharma-lactose (400 g/L). A GOS production of about 144 g/L was achieved after 24 h (36.0% yield).

Viable tendon neotissue from adult adipose-derived multipotent stromal cells.

Background: Tendon healing is frequently prolonged, unpredictable, and results in poor tissue quality. Neotissue formed by adult multipotent stromal cells has the potential to guide healthy tendon tissue formation. Objectives: The objective of this study was to characterize tendon neotissue generated by equine adult adipose-derived multipotent stromal cells (ASCs) on collagen type I (COLI) templates under 10% strain in a novel bioreactor. The tested hypothesis was that ASCs assume a tendon progenitor cell-like morphology, express tendon-related genes, and produce more organized extracellular matrix (ECM) in tenogenic versus stromal medium with perfusion and centrifugal fluid motion. Methods: Equine ASCs on COLI sponge cylinders were cultured in stromal or tenogenic medium within bioreactors during combined perfusion and centrifugal fluid motion for 7, 14, or 21days under 10% strain. Viable cell distribution and number, tendon-related gene expression, and micro- and ultra-structure were evaluated with calcein-AM/EthD-1 staining, resazurin reduction, RT-PCR, and light, transmission, and scanning electron microscopy. Fibromodulin was localized with immunohistochemistry. Cell number and gene expression were compared between culture media and among culture periods (p < 0.05). Results: Viable cells were distributed throughout constructs for up to 21days of culture, and cell numbers were higher in tenogenic medium. Individual cells had a round or rhomboid shape with scant ECM in stromal medium in contrast to clusters of parallel, elongated cells surrounded by highly organized ECM in tenogenic medium after 21days of culture. Transcription factor, extracellular matrix, and mature tendon gene expression profiles confirmed ASC differentiation to a tendon progenitor-like cell in tenogenic medium. Construct micro- and ultra-structure were consistent with tendon neotissue and fibromodulin was present in the ECM after culture in tenogenic medium. Conclusion: Long-term culture in custom bioreactors with combined perfusion and centrifugal tenogenic medium circulation supports differentiation of equine adult ASCs into tendon progenitor-like cells capable of neotissue formation.

Production of Xylanase by Trichoderma Species Growing on Olive Mill Pomace and Barley Bran in a Packed-Bed Bioreactor.

Xylanases are hydrolytic enzymes that have tremendous applications in different sectors of life, but the high cost of their production has limited their use. One solution to reduce costs and enhance xylanase production is the use of agro-wastes as a substrate in fungal cultures. In this study, olive mill pomace (OMP) and barley bran (BB) were used as carbon sources and possible inducers of xylanase production by three species of Trichoderma (atroviride, harzianum, and longibrachiatum), one major xylanase producer. The experiments were conducted under a solid-state fermentation system (SSF) in flask cultures and a packed-bed bioreactor. Cultures of OMP and BB were optimized by examining different ratios of OMP and BB, varied particle sizes, and inoculum size for the three species of Trichoderma. The ratio of 8:2 OMP and BB yielded the highest xylanase activity, with a particle size of 1 mm at 29 °C and an inoculum size of 1 × 107 spores/mL. Studying the time profile of the process revealed that xylanase activity was highest after seven days of incubation in flask SSF cultures (1.779 U/mL) and after three days in a packed-bed bioreactor (1.828 U/mL). The maximum percentage of OMP degradation recorded was about 15% in the cultures of T. harzianum flask SSF cultures, compared to about 11% in T. longibrachiatum bioreactor cultures. Ammonium sulfate precipitation and dialysis experiments showed that Xylane enzyme activity ranged from 0.274 U/mL in T. harzianum to 0.837 U/mL in T. atroviride when crude extract was used, with the highest activity (0.628 U/mL) at 60% saturation. Xylose was the main sugar released in all purified fractions, with the G-50 and G-75 fractions showing the maximum units of xylanase.

ВЛИЯНИЕ УРОВНЯ РАСТВОРЕННОГО КИСЛОРОДА НА СПОРООБРАЗОВАНИЕ B. SUBTILIS ПРИ ГЛУБИННОМ КУЛЬТИВИРОВАНИИ В БИОРЕАКТОРЕ

This paper presents research findings on the impact of dissolved oxygen levels on the spore formation of B. subtilis during submerged cultivation in a bioreactor. The experiments analyzed both static and dynamic oxygen levels. The study revealed that oxygenation changes significantly affect the kinetics and yield of B. subtilis spores. When static DO values ranged from 0% to 50%, the process proved economically inefficient, with either non-viable bacteria at the end of the cycle or a spore yield that was not cost-effective. Conversely, DO levels from 50% to 0% resulted in rapid spore formation, followed by a shift from sporulation form back to vegetative form. The research identified the optimal dissolved oxygen range for cultivation as a dynamic cycle between 0% and 50%, where sporulation occurred after 36 hours, with spores comprising 95% of the total bacterial mass. This study broadens our understanding of biotechnological growth factors in bioreactor systems. Microbiological and biotechnological methods were used for submerged cultivation in bioreactors, along with physicochemical monitoring of dissolved oxygen. The practical relevance of this study lies in its potential application in controlling the cultivation of this microorganism for industrial biotechnological processes.

ОСОБЕННОСТИ РАЗЛИЧИЙ БИОРЕАКТОРОВ ДЛЯ КУЛЬТИВИРОВАНИЯ КЛЕТОЧНЫХ КУЛЬТУР ПО СПОСОБУ ПОДВОДА ЭНЕРГИИ

Environment for the cultivation of muscle tissue of farm animals when grown in vitro using the necessary equipment, in particular, biorectors of various types for the cultivation of cell cultures, can become one of the new directions for obtaining animal biomaterial, while observing various parameters of the technology supporting the reproduction of cell cultures during cultivation, including taking into account optimal methods energy supply. (Research purpose) The research purpose is studying the scientifically substantiated parameters of the technological process of energy supply to ensure the optimal mode of cultivation in bioreactors of various technological types of stem and other cells and tissues of farm animals, in particular cattle (Materials and methods) Applied theoretical and experimental methods of energy supply when growing cell mass in vitro with specified cultivation parameters with using mathematical methods. (Results and discussion) It has been found out that all the design features of fermenters (bioreactors) are distinguished by the methods of energy supply: with energy supply to the gas phase; with energy supply to the liquid phase; with combined energy supply. It was determined that the temperature control is carried out by an electric heating plate of 100 watts with a solenoid valve, the gas source is air, O2, CO2, N2; the power supply of the control cabinet is 220 volts, 50 hertz. It has been shown that the presence of an external circulation circuit with heat exchangers, the large height of the apparatus and the length of the tubes create significant hydraulic resistances of the circulation circuits at a speed of 1-2 meters per second of culture fluid in the tubes, which leads to energy losses and the need to have pumps for pumping gas-liquid culture fluids with a pressure not lower than 20-40 meters of water column. (Conclusions) It was found that pumping the medium solution from the growth chamber and back increases the cost of electricity consumed by the bioreactor, therefore it is possible to reduce the pumping speed by increasing the concentration of the components of the enriched medium.

Metabolic engineering of Corynebacterium glutamicum for the production of anthranilate from glucose and xylose.

Anthranilate and its derivatives are important basic chemicals for the synthesis of polyurethanes as well as various dyes and food additives. Today, anthranilate is mainly chemically produced from petroleum-derived xylene, but this shikimate pathway intermediate could be also obtained biotechnologically. In this study, Corynebacterium glutamicum was engineered for the microbial production of anthranilate from a carbon source mixture of glucose and xylose. First, a feedback-resistant 3-deoxy-arabinoheptulosonate-7-phosphate synthase from Escherichia coli, catalysing the first step of the shikimate pathway, was functionally introduced into C. glutamicum to enable anthranilate production. Modulation of the translation efficiency of the genes for the shikimate kinase (aroK) and the anthranilate phosphoribosyltransferase (trpD) improved product formation. Deletion of two genes, one for a putative phosphatase (nagD) and one for a quinate/shikimate dehydrogenase (qsuD), abolished by-product formation of glycerol and quinate. However, the introduction of an engineered anthranilate synthase (TrpEG) unresponsive to feedback inhibition by tryptophan had the most pronounced effect on anthranilate production. Component I of this enzyme (TrpE) was engineered using a biosensor-based invivo screening strategy for identifying variants with increased feedback resistance in a semi-rational library of TrpE muteins. The final strain accumulated up to 5.9 g/L (43 mM) anthranilate in a defined CGXII medium from a mixture of glucose and xylose in bioreactor cultivations. We believe that the constructed C. glutamicum variants are not only limited to anthranilate production but could also be suitable for the synthesis of other biotechnologically interesting shikimate pathway intermediates or any other aromatic compound derived thereof.

Bioreactor Culture to Create Adipose Tissue from Human Mesenchymal Stromal Cells.

Adipose tissue is a complex and multifaceted endocrine organ located throughout the body. The dysfunction of adipose tissue is known to induce a wide variety of comorbidities that can negatively impact one's health and quality of life. In addition to behavioral changes, drugs that target dysfunctional adipose tissue to treat associated diseases are clinically needed. Regarding drug-testing platforms, animal models are the most popular models, limited by known differences from humans in genetics and physiology. Two-dimensional and static three-dimensional (3D) cell cultures are also used. Still, these in vitro models with static culture fail to recapitulate the phenotype and function of adipocytes seen in vivo. To combat this, our lab has developed an adipose tissue microphysiological system. A perfusion bioreactor with dual-flow chambers is 3D printed, which enables individualized top and bottom medium flows after adipose tissues are inserted as a barrier. Human progenitor cells, such as human mesenchymal stem cells, are embedded within a gelatin scaffold and in situ adipogenic differentiation within the bioreactor. Medium flow is established via a syringe pump system, allowing in vivo-like conditions to be maintained. The novel bioreactor-cultured adipose tissues represent a versatile disease modeling and drug-testing system. Here, we present the step-by-step methods to generate the bioreactors and adipose tissues. We also show the process of collecting and analyzing samples. In addition, we highlight the critical steps that require particular attention in notes.

Disposable Bioreactors Used in Process Development and Production Processes with Plant Cell and Tissue Cultures.

The bioreactor is the centerpiece of the upstream processing in any biotechnological production process. Its design, the cultivation parameters, the production cell line, and the culture medium all have a major influence on the efficiency of the process and the result of the cultivation. Disposable bioreactors have been used for the past 20 years, playing a major role in process development and commercial production of high-value substances at medium scales.Our review deals with scalable, disposable bioreactors that have proven to be useful for the cultivation of plant cell and tissue cultures. Based on the definitions of terms and a categorization approach, the most commonly used, commercially available, disposable bioreactor types are presented below. The focus is on wave-mixed, stirred, and orbitally shaken bioreactors. In addition to their instrumentation and bioengineering characteristics, cultivation results are discussed, and emerging trends for the development of disposable bioreactors for plant cell and tissue cultures are also addressed.

Large-Scale Production of Specialized Metabolites In Vitro Cultures.

For centuries plants have been intensively utilized as reliable sources of food, flavoring, and pharmaceutical ingredients. However, plant natural habitats are being rapidly lost due to the climate change and agriculture. Plant biotechnology offers a sustainable approach for the bioproduction of specialized plant metabolites. The unique structural features of plant-derived specialized metabolites, such as their safety profile and multi-target spectrum, have led to the establishment of many plant-derived drugs. However, there are still many challenges to overcome regarding the production of these metabolites from plant in vitro systems and establish a sustainable large-scale biotechnological process. These challenges are due to the peculiarities of plant cell metabolism, the complexity of plant specialized metabolite pathways, and the correct selection of bioreactor systems and bioprocess optimization. In this book chapter, we attempted to focus on the advantages of plant in vitro systems and in particular plant cell suspensions for their cultivation as a source of plant-derived specialized metabolites. A state-of-the-art technological platform for plant cell suspension cultivation from callus induction to lab-scale cultivation, extraction, and purification is presented. Possibilities for bioreactor cultivation of plant cell suspensions in benchtop and large-scale volumes are highlighted, including several examples and patents for industrial production of specialized metabolites.

Protein Expression via Transient Transfection of Mammalian Cells in a WAVE Bioreactor.

Large culture volumes are often required when expression constructs are particularly low-yielding or when end uses require significant amounts of material. In these cases, a single homogeneous culture is usually more convenient, in terms of both consistency of expression and labor/resource requirements, than multiple parallel cultures. Using a WAVE Bioreactor culture, volumes as high as 500L may be achieved in a single vessel. Here, we describe the transfection of Expi293F cells in a disposable 50L Cellbag on a WAVE Bioreactor platform to produce recombinant protein. The methods described herein may be adapted, with suitable optimizations, for other suspension-adapted mammalian cell lines.

PRODUCTION OF MICROSHOOT USING THE TEMPORARY IMMERSION SYSTEM (TIS) IN POTATO CULTIVARS

The Temporary Immersion System (TIS) Bioreactor’s performance in cultivation for several commercial potato cultivars became the prevailing study’s review focus. The experiment in a split-plot design had two factors. The first factor comprised the type of culture system (conventional and TIS Bioreactor) treatment used as main plots. The second factor was the four potato cultivars (Atlantic Malang, Dayang Sumbi, Granola L., and Maglia) used as subplots. The TIS Bioreactor culture has the highest average in all studied variables compared with conventional cultures at the multiplication stage. In the TIS Bioreactor, potato cultivar Dayang Sumbi excelled in the number of axillary branching and number of primary roots. At the same time, genotype Granola L. surpassed the height of the plantlets of other cultivars. Meanwhile, the cultivar Atlantic Malang shone in the number of nodes, with Maglia in the number of leaves. Using the TIS Bioreactor produces microshoots with more nodes and can be beneficial as a propagation organ. The Dayang Sumbi cultivar was superior to all other potato cultivars.

Influence of medium type and culture method on the multiplication efficiency of Chlorophytum comosum (Thunb.) Jacques in in vitro conditions

In response to the challenges posed by modern plant micropropagation techniques, a promising technology for growing shoots temporary immersed in nutrient solution (temporary immersion system, TIS) using SETIS™ bioreactors has been developed. In this experiment, the suitability of this technology for the propagation of Chlorophytum comosum (Thunb.) Jacques was assessed. In vitro culture was carried out using a conventional technique on solid media and liquid media using the SETIS™ bioreactor. In addition, two culture media differing in macro- and micronutrient content (Murashige &amp; Skoog and Rugini OM), while having the same set of phytohormones were evaluated in both systems. Explants obtained from the flower stalk of the plants were used to establish the culture. The effectiveness of the cultures after the first and second subculture was assessed. The study has demonstrated that the efficiency of liquid culture carried out using the SETIS™ bioreactor is higher compared to the conventional culture. The highest multiplication coefficient, fresh weight of regenerants and RGR index value in bioreactor cultures was recorded on Rugini OM medium. No statistically significant differences were found between MS medium and Rugini OM medium in terms of shoot length and vigour with this method of culture. When using the conventional method, better results can be achieved with MS medium. This research can be considered as a first step towards the production of Chlorophytum comosum (Thunb.) Jacques on a larger scale.

Phenomenological-based semi-physical model characterizing the central metabolic response of Escherichia coli to changes in batch culture temperature

This work presents a phenomenological-based semi-physical model characterizing the E. coli response to environmental temperature changes in batch cultures. The proposed model is based on a general description of the mass balance of the central metabolism and an energy balance that focuses on key parameters. This model can represent changes in specific growth rate and alteration to the mass flows of the central metabolism. Moreover, the model can make predictions regarding microorganism growth, respiratory rate, glucose consumption, acetate accumulation, and heat exchange between E. coli and its environment at several different temperatures. The fit and validation of the model was assessed against published data obtained under aerobic growth conditions in agitated tank bioreactor cultures. Our assessment of this model indicates that mass and energy balances can predict global changes in E. coli metabolism that are associated with different temperature conditions and differences in heat flow between bacteria and the environment. This model can be used to correlate environmental conditions with experimental bioreactor parameters and simulate microorganismal response during the design of temperature control systems for bioreactors and can even be used as a base model to represent heat-inducible E. coli strains used in recombinant protein production.

Production of d-glucaric acid with phosphoglucose isomerase-deficient Saccharomyces cerevisiae

d-Glucaric acid is a potential biobased platform chemical. Previously mainly Escherichia coli, but also the yeast Saccharomyces cerevisiae, and Pichia pastoris, have been engineered for conversion of d-glucose to d-glucaric acid via myo-inositol. One reason for low yields from the yeast strains is the strong flux towards glycolysis. Thus, to decrease the flux of d-glucose to biomass, and to increase d-glucaric acid yield, the four step d-glucaric acid pathway was introduced into a phosphoglucose isomerase deficient (Pgi1p-deficient) Saccharomyces cerevisiae strain. High d-glucose concentrations are toxic to the Pgi1p-deficient strains, so various feeding strategies and use of polymeric substrates were studied. Uniformly labelled 13C-glucose confirmed conversion of d-glucose to d-glucaric acid. In batch bioreactor cultures with pulsed d-fructose and ethanol provision 1.3 g d-glucaric acid L−1 was produced. The d-glucaric acid titer (0.71 g d-glucaric acid L−1) was lower in nitrogen limited conditions, but the yield, 0.23 g d-glucaric acid [g d-glucose consumed]−1, was among the highest that has so far been reported from yeast. Accumulation of myo-inositol indicated that myo-inositol oxygenase activity was limiting, and that there would be potential to even higher yield. The Pgi1p-deficiency in S. cerevisiae provides an approach that in combination with other reported modifications and bioprocess strategies would promote the development of high yield d-glucaric acid yeast strains.

γ-Glutamylation of Isopropylamine by Fermentation.

Glutamylation yields N-functionalized amino acids in several natural pathways. γ-Glutamylated amino acids may exhibit improved properties for their industrial application, e. g., as taste enhancers or in peptide drugs. γ-Glutamyl-isopropylamide (GIPA) can be synthesized from isopropylamine (IPA) and l-glutamate. In Pseudomonas sp. strain KIE171, GIPA is an intermediate in the biosynthesis of l-alaninol (2-amino-1-propanol), a precursor of the fluorochinolone antibiotic levofloxacin and of the chloroacetanilide herbicide metolachlor. In this study, fermentative production of GIPA with metabolically engineered Pseudomonas putida KT2440 using γ-glutamylmethylamide synthetase (GMAS) from Methylorubrum extorquens was established. Upon addition of IPA during growth with glycerol as carbon source in shake flasks, the recombinant strain produced up to 21.8 mM GIPA. In fed-batch bioreactor cultivations, GIPA accumulated to a titer of 11 g L-1 with a product yield of 0.11 g g-1 glycerol and a volumetric productivity of 0.24 g L-1 h-1 . To the best of our knowledge, this is the first fermentative production of GIPA.

Sulfate limitation increases specific plasmid DNA yield and productivity in E. coli fed-batch processes

Plasmid DNA (pDNA) is a key biotechnological product whose importance became apparent in the last years due to its role as a raw material in the messenger ribonucleic acid (mRNA) vaccine manufacturing process. In pharmaceutical production processes, cells need to grow in the defined medium in order to guarantee the highest standards of quality and repeatability. However, often these requirements result in low product titer, productivity, and yield. In this study, we used constraint-based metabolic modeling to optimize the average volumetric productivity of pDNA production in a fed-batch process. We identified a set of 13 nutrients in the growth medium that are essential for cell growth but not for pDNA replication. When these nutrients are depleted in the medium, cell growth is stalled and pDNA production is increased, raising the specific and volumetric yield and productivity. To exploit this effect we designed a three-stage process (1. batch, 2. fed-batch with cell growth, 3. fed-batch without cell growth). The transition between stage 2 and 3 is induced by sulfate starvation. Its onset can be easily controlled via the initial concentration of sulfate in the medium. We validated the decoupling behavior of sulfate and assessed pDNA quality attributes (supercoiled pDNA content) in E. coli with lab-scale bioreactor cultivations. The results showed an increase in supercoiled pDNA to biomass yield by 33% and an increase of supercoiled pDNA volumetric productivity by 13 % upon limitation of sulfate. In conclusion, even for routinely manufactured biotechnological products such as pDNA, simple changes in the growth medium can significantly improve the yield and quality.Graphical

Comparison of wild-type KT2440 and genome-reduced EM42 Pseudomonas putida strains for muconate production from aromatic compounds and glucose

Pseudomonas putida KT2440 is a robust, aromatic catabolic bacterium that has been widely engineered to convert bio-based and waste-based feedstocks to target products. Towards industrial domestication of P. putida KT2440, rational genome reduction has been previously conducted, resulting in P. putida strain EM42, which exhibited characteristics that could be advantageous for production strains. Here, we compared P. putida KT2440- and EM42-derived strains for cis,cis-muconic acid production from an aromatic compound, p-coumarate, and in separate strains, from glucose. To our surprise, the EM42-derived strains did not outperform the KT2440-derived strains in muconate production from either substrate. In bioreactor cultivations, KT2440- and EM42-derived strains produced muconate from p-coumarate at titers of 45 g/L and 37 g/L, respectively, and from glucose at 20 g/L and 13 g/L, respectively. To provide additional insights about the differences in the parent strains, we analyzed growth profiles of KT2440 and EM42 on aromatic compounds as the sole carbon and energy sources. In general, the EM42 strain exhibited reduced growth rates but shorter growth lags than KT2440. We also observed that EM42-derived strains resulted in higher growth rates on glucose compared to KT2440-derived strains, but only at the lowest glucose concentrations tested. Transcriptomics revealed that genome reduction in EM42 had global effects on transcript levels and showed that the EM42-derived strains that produce muconate from glucose exhibit reduced modulation of gene expression in response to changes in glucose concentrations. Overall, our results highlight that additional studies are warranted to understand the effects of genome reduction on microbial metabolism and physiology, especially when intended for use in production strains.