High cell density cultivation of E. coli in shake flasks for the production of recombinant proteins.
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ABSTRACT:
SUBMITTER: Ganjave SD
PROVIDER: S-EPMC8718739 | biostudies-literature |
REPOSITORIES: biostudies-literature
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Project description:BackgroundPoly(?-glutamic acid) (?-PGA) is a biopolymer with many useful properties making it applicable for instance in food and skin care industries, in wastewater treatment, in biodegradable plastics or in the pharmaceutical industry. ?-PGA is usually produced microbially by different Bacillus spp. The produced ?-PGA increases the viscosity of the fermentation broth. In case of shake flask fermentations, this results in an increase of the volumetric power input. The power input in shake flasks can be determined by measuring the torque of an orbitally rotating lab shaker. The online measurement of the volumetric power input enables to continuously monitor the formation or degradation of viscous products like ?-PGA. Combined with the online measurement of the oxygen transfer rate (OTR), the respiration activity of the organisms can be observed at the same time.ResultsTwo different Bacillus licheniformis strains and three medium compositions were investigated using online volumetric power input and OTR measurements as well as thorough offline analysis. The online volumetric power input measurement clearly depicted changes in ?-PGA formation due to different medium compositions as well as differences in the production behavior of the two investigated strains. A higher citric acid concentration and the addition of trace elements to the standard medium showed a positive influence on ?-PGA production. The online power input signal was used to derive an online viscosity signal which was validated with offline determined viscosity values. The online measurement of the OTR proved to be a valuable tool to follow the respiration activity of the cultivated strains and to determine its reproducibility under different cultivation conditions.ConclusionsThe combination of the volumetric power input and the OTR allows for an easy and reliable investigation of new strains, cultivation conditions and medium compositions for their potential in ?-PGA production. The power input signal and the derived online viscosity directly reflect changes in ?-PGA molecular weight and concentration, respectively, due to different cultivation conditions or production strains.
| S-EPMC5506581 | biostudies-literature
Project description:The transcriptome profiles for wild-type (plasmid-free) and recombinant (plasmid-bearing) Escherichia coli during well-controlled synchronized high-cell-density fed-batch cultures were analyzed by DNA microarrays. It was observed that the growth phase significantly affected the transcriptome profiles, and the transcriptome profiles were significantly different for the recombinant and wild-type cultures. The response of the wild-type and recombinant cultures to an isopropyl-1-thio-β-D-galactopyranoside- (IPTG-) addition was examined, where IPTG induced recombinant protein production in the plasmid-bearing cultures. The IPTG-addition significantly altered the transcriptome response of the wild-type cultures entering the stationary phase. The IPTG-induced recombinant protein production resulted in a significant down-regulation of many energy synthesis genes (atp, nuo, cyo), as well as nearly all transcription- and translation-related genes (rpo, rpl, rpm, rps, rrf, rrl, rrs). Numerous phage (psp, hfl) and transposon-related genes (tra, ins) were significantly regulated in the recombinant cultures due to the IPTG-induction. These results indicate that the signaling mechanism, associated with the recombinant protein production, may induce a metabolic burden in the form of a phage defense mechanism. Taken together, these results indicated that recombinant protein production initiated a cascade of transcriptome responses that down-regulated the very genes needed to sustain productivity. In this study, the transcriptome profiles for recombinant and wild-type E. coli cultures were compared. The recombinant and wild-type cultures were monitored during the exponential growth phase and as the cultures entered the stationary phase. Well-controlled fed-batch fermenters were used to synchronize the high-cell density cultures. E. coli MG1655 [pPROEx-CAT] and E. coli MG1655 (plasmid-free) were exposed to IPTG in the exponential phase, where chloramphenicol acetyltransferase (CAT) expression was induced in the plasmid-bearing cultures. Control cultures, not exposed to IPTG, were also examined. The gene expression profiles were determined using DNA microarrays. Recombinant protein production was shown to result in a metabolic burden due to significant down-regulation of the transcription, translation, and energy synthesis genes. This was the first comprehensive study that has examined the transcriptome of wild-type and recombinant cultures under the same set of conditions. This data indicated that one cannot merely extrapolate the behavior of recombinant cultures from wild-type culture data.
2009-08-07 | GSE17505 | GEO
Project description:Kinetic growth models are a useful tool for a better understanding of microalgal cultivation and for optimizing cultivation conditions. The evaluation of such models requires experimental data that is laborious to generate in bioreactor settings. The experimental shake flask setting used in this study allows to run 12 experiments at the same time, with 6 individual light intensities and light durations. This way, 54 biomass data sets were generated for the cultivation of the microalgae Chlorella vulgaris. To identify the model parameters, a stepwise parameter estimation procedure was applied. First, light-associated model parameters were estimated using additional measurements of local light intensities at differ heights within medium at different biomass concentrations. Next, substrate related model parameters were estimated, using experiments for which biomass and nitrate data were provided. Afterwards, growth-related model parameters were estimated by application of an extensive cross validation procedure.
| S-EPMC8732984 | biostudies-literature
Project description:For over 30 years, serine hydroxamate has been used to chemically stimulate a stringent response in Escherichia coli and other bacteria. These studies have elucidated numerous characteristics of the classical stringent response beyond the simple cellular response to an amino acid shortage, including phospholipid synthesis and protease up-regulation. In this study, the effects of a serine hydroxamate addition on high cell density recombinant E. coli were examined and compared to the effects of recombinant protein production to determine overlaps, as recombinant protein production stress has often been attributed to amino acid shortages. Both the transcriptome and growth characteristics were evaluated and compared. The serine hydroxamate addition profoundly decreased the culture growth rate, whereas, recombinant protein production did not. Conversely, the transcriptome profile of the recombinant E. coli cultures were relatively unaffected by the serine hydroxamate addition, yet recombinant protein production dramatically changed the transcriptome profile. A subset of the classical stringent response genes were effected by the serine hydroxamate addition, whereas, recombinant protein production regulated numerous classical stringent response genes; however, not all. The genes that were regulated by the serine hydroxamate addition include numerous fatty acid synthesis genes, in agreement with altered phospholipids synthesis reports. These results indicate that recombinant protein production and the stringent response have many overlapping responses; however, are far from identical. It was hypothesized that recombinant protein production leads to a stringent response due to the high amino acid synthesis demands related to recombinant protein synthesis. A comparison of the transcriptomes during recombinant protein production and a chemical imposed stringent response would assist with determining what portion of the “metabolic burden” associated with recombinant protein production is due to amino acid shortages. In this study, the transcriptome profiles of recombinant E. coli were examined and compared for the three culture conditions: 1) Normal growth, no external stress; 2) L-serine hydroxamate addition (to mediate a stringent response); and 3) IPTG-induction to produce the recombinant protein chloramphenicol acetyltransferase (CAT). The transcriptome profiles from these three conditions were analyzed using Affymetrix Anti-sense E. coli GeneChip® microarrays.
2009-08-07 | GSE17506 | GEO
Project description:The transcriptome profiles for wild-type (plasmid-free) and recombinant (plasmid-bearing) Escherichia coli during well-controlled synchronized high-cell-density fed-batch cultures were analyzed by DNA microarrays. It was observed that the growth phase significantly affected the transcriptome profiles, and the transcriptome profiles were significantly different for the recombinant and wild-type cultures. The response of the wild-type and recombinant cultures to an isopropyl-1-thio-β-D-galactopyranoside- (IPTG-) addition was examined, where IPTG induced recombinant protein production in the plasmid-bearing cultures. The IPTG-addition significantly altered the transcriptome response of the wild-type cultures entering the stationary phase. The IPTG-induced recombinant protein production resulted in a significant down-regulation of many energy synthesis genes (atp, nuo, cyo), as well as nearly all transcription- and translation-related genes (rpo, rpl, rpm, rps, rrf, rrl, rrs). Numerous phage (psp, hfl) and transposon-related genes (tra, ins) were significantly regulated in the recombinant cultures due to the IPTG-induction. These results indicate that the signaling mechanism, associated with the recombinant protein production, may induce a metabolic burden in the form of a phage defense mechanism. Taken together, these results indicated that recombinant protein production initiated a cascade of transcriptome responses that down-regulated the very genes needed to sustain productivity. In this study, the transcriptome profiles for recombinant and wild-type E. coli cultures were compared. The recombinant and wild-type cultures were monitored during the exponential growth phase and as the cultures entered the stationary phase. Well-controlled fed-batch fermenters were used to synchronize the high-cell density cultures. E. coli MG1655 [pPROEx-CAT] and E. coli MG1655 (plasmid-free) were exposed to IPTG in the exponential phase, where chloramphenicol acetyltransferase (CAT) expression was induced in the plasmid-bearing cultures. Control cultures, not exposed to IPTG, were also examined. The gene expression profiles were determined using DNA microarrays. Recombinant protein production was shown to result in a metabolic burden due to significant down-regulation of the transcription, translation, and energy synthesis genes. This was the first comprehensive study that has examined the transcriptome of wild-type and recombinant cultures under the same set of conditions. This data indicated that one cannot merely extrapolate the behavior of recombinant cultures from wild-type culture data. Experiment Overall Design: All fermentations were synchronized in time to the time at which the cell density reached approximately 11.5 OD, or roughly 70% of the fermenter’s maximum cell density. IPTG (5 mM) was added when the cell density reached the targeted OD for the cultures to be induced. Cells were harvested at 0, 1, 2, 3, 4, and 5 hours relative to the synchronization time point (identified as Time S0, S1, etc). Each fermentation condition was conducted in duplicate. For the recombinant Control Time S0 sample, triplicate samples were available since prior to the IPTG-addition, all fermentations within a strain were replicates. All fermentation conditions were repeated twice (two biological replicates). RNA from each biological replicate was purified and processed independently. Three biological replicates were obtained from for the recombinant Control sample (Time S0) since the cultures prior to the IPTG-addition were replicates. Prior to hybridization, where only two biological replicates existed, one of the RNA samples was divided into two technical replicates, resulting in three separate hybridized chips. The wild-type Time S0 samples and all Time S1 and S4 samples contained data from three DNA microarrays obtained from two biological duplicates (30 DNA microarrays total).
2009-08-25 | E-GEOD-17505 | biostudies-arrayexpress
Project description:BackgroundIn Streptomyces, understanding the switch from primary to secondary metabolism is important for maximizing the production of secondary metabolites such as antibiotics, as well as for optimizing recombinant glycoprotein production. Differences in Streptomyces lividans bacterial aggregation as well as recombinant glycoprotein production and O-mannosylation have been reported due to modifications in the shake flask design. We hypothetized that such differences are related to the metabolic switch that occurs under oxygen-limiting conditions in the cultures.ResultsShake flask design was found to affect undecylprodigiosin (RED, a marker of secondary metabolism) production; the RED yield was 12 and 385 times greater in conventional normal Erlenmeyer flasks (NF) than in baffled flasks (BF) and coiled flasks (CF), respectively. In addition, oxygen transfer rates (OTR) and carbon dioxide transfer rates were almost 15 times greater in cultures in CF and BF as compared with those in NF. Based on these data, we obtained respiration quotients (RQ) consistent with aerobic metabolism for CF and BF, but an RQ suggestive of anaerobic metabolism for NF.ConclusionAlthough the metabolic switch is usually related to limitations in phosphate and nitrogen in Streptomyces sp., our results reveal that it can also be activated by low OTR, dramatically affecting recombinant glycoprotein production and O-mannosylation and increasing RED synthesis in the process.
| S-EPMC6260694 | biostudies-literature
Project description:Chinese Hamster Ovary cell lines are currently the primary host for production of therapeutic glycoproteins. Fast process development resulting in robust and scalable processes is a critical success factor in the highly competitive market for biosimilars. In process development screening of hundreds of clones and selection of process conditions are routinely performed in uncontrolled cultivation systems like shake flasks. A handful of potential candidate clones is nominated to be evaluated more intensively in well controlled small-scale bioreactors. Cell performance in the uncontrolled systems and to a lesser extent in the small-scale bioreactors may, however, be different from that in the final production reactor, which may result in failures during scale-up and thus extra development time. In this work, the focus is on better understanding the differences in cell performance between controlled and uncontrolled systems, which can be used to make process development faster and more robust in terms of scale-up. For this, we evaluated differences in gene expression profiles between shake flask and bioreactor cultures at three different time points during the exponential and stationary phase of a batch culture using commercially available Affymetrix GeneChip CHO Gene 2.1 ST arrays and multivariate data analysis on the outcomes. The outcomes were correlated with differences in glycosylation patterns and other culture parameters. Results showed large differences in gene expression over time and much smaller differences between the two cultivation systems. Furthermore, our study identified differentially expressed genes and corresponding metabolic and mechanistic pathways between the two systems, which were directly related to the degree of the control of the systems.
2023-11-04 | GSE104787 | GEO
Project description:High cell density cultivation is a promising approach to reduce capital and operating costs of poly (3-hydroxybutyrate) (PHB) production. To achieve high cell concentration, it is necessary that the cultivation conditions are adjusted and controlled to support the best growth of the PHB producer. In the present study, carbon to nitrogen (C/N) ratio of a sugarcane juice (SJ)-based medium, initial sugar concentration, and dissolved oxygen (DO) set point, were optimized for batch cultivation of Paracoccus sp. KKU01. A maximum biomass concentration of 55.5 g/L was attained using the C/N ratio of 10, initial sugar concentration of 100 g/L, and 20% DO set point. Fed-batch cultivation conducted under these optimum conditions, with two feedings of SJ-based medium, gave the final cell concentration of 87.9 g/L, with a PHB content, concentration, and yield of 36.2%, 32.1 g/L, and 0.13 g/g-sugar, respectively. A medium-based economic analysis showed that the economic yield of PHB on nutrients was 0.14. These results reveal the possibility of using SJ for high cell density cultivation of Paracoccus sp. KKU01 for PHB production. However, further optimization of the process is necessary to make it more efficient and cost-effective.
| S-EPMC9133739 | biostudies-literature
Project description:BackgroundLipopolysaccharide (LPS), also referred to as endotoxin, is the major constituent of the outer leaflet of the outer membrane of virtually all Gram-negative bacteria. The lipid A moiety, which anchors the LPS molecule to the outer membrane, acts as a potent agonist for Toll-like receptor 4/myeloid differentiation factor 2-mediated pro-inflammatory activity in mammals and, thus, represents the endotoxic principle of LPS. Recombinant proteins, commonly manufactured in Escherichia coli, are generally contaminated with endotoxin. Removal of bacterial endotoxin from recombinant therapeutic proteins is a challenging and expensive process that has been necessary to ensure the safety of the final product.ResultsAs an alternative strategy for common endotoxin removal methods, we have developed a series of E. coli strains that are able to grow and express recombinant proteins with the endotoxin precursor lipid IVA as the only LPS-related molecule in their outer membranes. Lipid IVA does not trigger an endotoxic response in humans typical of bacterial LPS chemotypes. Hence the engineered cells themselves, and the purified proteins expressed within these cells display extremely low endotoxin levels.ConclusionsThis paper describes the preparation and characterization of endotoxin-free E. coli strains, and demonstrates the direct production of recombinant proteins with negligible endotoxin contamination.
| S-EPMC4404585 | biostudies-literature
Project description:BackgroundThe fungal ribotoxin hirsutellin A (HtA) exhibits strong insecticidal activity; however, efficient systems for expressing recombinant HtA (rHtA) are lacking. Here, we established an efficient heterologous expression system to produce large amounts of rHtA.ResultsRecombinant Pichia pastoris transformants with high levels of secretory rHtA were screened, and in a fed-batch reactor, rHtA was secreted at levels up to 80 mg/l following methanol induction, which was more than sixfold higher than that in shake flasks. Approximately 7 mg of highly pure rHtA was obtained from 300 ml of fed-batch culture supernatant by Ni+-nitriloacetic acid affinity chromatography and CM Sepharose ion-exchange chromatography. Mass spectrometry results revealed rHtA as a native N-terminal non-glycosylated monomeric protein with a molecular weight of 15.3 kDa. Purified rHtA exhibited excellent thermal and protease stability and dose-dependent cytotoxicity to Sf9 insect cells and insecticidal activity against Galleria mellonella larvae.ConclusionsThis is the first report of rHtA expression in P. pastoris. The rHtA was expressed at a high level under high-cell-density fed-batch fermentation and was efficiently purified using a two-step purification method. Purified rHtA exhibited thermal and protease stability, as well as appropriate bioactivities. Our results indicate that fed-batch production by P. pastoris is an efficient method to produce functional rHtA.
| S-EPMC6195745 | biostudies-literature