The use of multi-parameter flow cytometry to compare the physiological response of Escherichia coli W3110 to glucose limitation during batch, fed-batch and continuous culture cultivations.

Multi-parameter flow cytometric techniques have been developed for the 'at-line' study of bacterial cultivations. Using a mixture of specific fluorescent stains it is possible to resolve an individual cells physiological state beyond culturability, based on the presence or absence of an intact polarised cytoplasmic membrane, enabling assessment of population heterogeneity. It has been shown that during the latter stages of small-scale (5 l), well mixed fed-batch cultivations there is a considerable drop in cell viability, about 17%, as characterised by cytoplasmic membrane depolarisation and permeability. These phenomena are thought to be due to the severe and steadily increasing stress associated with glucose limitation at high cell densities, during the fed-batch process. Such effects were not found in either batch or continuous culture cultivations. The possibility of using these findings for improved process control using 'on-line' flow cytometry are discussed.     

Recombinant trypsin production in high cell density fed-batch cultures in Escherichia coli

Fed-batch techniques were employed to obtain high cell density cultures (92-100 g DCW/L) of Escherichia coli strain X90 producing a recombinant serine protease, rat anionic trypsin, secreted to the periplasm. The specific growth rate was controlled to minimize growth-inhibiting acetate formation by utilizing an exponential feeding profile determined from mass balance equation. The volumetric yield of recombinant rat anionic trypsin was 56 mg/L, and the final cell density was 92 g DCW/L when the culture was induced in the late logarithmic phase. However, when the culture was induced in the early logarithmic phase, the volumetric yield was 13 mg/L and the final cell density was 14 g DCW/L. Thus, the induction timing is shown to have a significant effect on the final cell density as well as the overall volumetric yield of the recombinant protease. (c) 1993 Wiley & Sons, Inc.     

The use of flow cytometry to detect nucleic acids attached to the surface of Escherichia coli in high cell density fed-batch processes

E. coli was grown in an aerobic fed-batch process for the production of a recombinant protein (rhGH). The cells were examined by flow cytometry and PI (propidium iodide) staining. The fluorescence of the PI-stained cells increased with increasing concentrations of DNA in the medium. Furthermore, DNA and RNA attached to the cell could partly be degraded with DNase/RNase and the fluorescence decreased. Formate excretion during the aerobic processes may be due to DNA and possibly also RNA attached to the cell surface, so creating diffusion resistance.     

Evidencing the role of lactose permease in IPTG uptake by Escherichia coli in fed-batch high cell density cultures

The lac-operon and its components have been studied for decades and it is widely used as one of the common systems for recombinant protein production in Escherichia coli. However, the role of the lactose permease, encoded by the lacY gene, when using the gratuitous inducer IPTG for the overexpression of heterologous proteins, is still a matter of discussion. A lactose permease deficient strain was successfully constructed. Growing profiles and acetate production were compared with its parent strain at shake flask scale. Our results show that the lac-permease deficient strain grows slower than the parent in defined medium at shake flask scale, probably due to a downregulation of the phosphotransferase system (PTS). The distributions of IPTG in the medium and inside the cells, as well as recombinant protein production were measured by HPLC-MS and compared in substrate limiting fed-batch fermentations at different inducer concentrations. For the mutant strain, IPTG concentration in the medium depletes slower, reaching at the end of the culture higher concentration values compared with the parent strain. Final intracellular and medium concentrations of IPTG were similar for the mutant strain, while higher intracellular concentrations than in medium were found for the parent strain. Comparison of the distribution profiles of IPTG of both strains in fed-batch fermentations showed that lac-permease is crucially involved in IPTG uptake. In the absence of the transporter, apparently IPTG only diffuses, while in the presence of lac-permease, the inducer accumulates in the cytoplasm at higher rates emphasizing the significant contribution of the permease-mediated transport.     

Use of a stress-minimisation paradigm in high cell density fed-batch Escherichia coli fermentations to optimise recombinant protein production

Production of recombinant proteins is an industrially important technique in the biopharmaceutical sector. Many recombinant proteins are problematic to generate in a soluble form in bacteria as they readily form insoluble inclusion bodies. Recombinant protein solubility can be enhanced by minimising stress imposed on bacteria through decreasing growth temperature and the rate of recombinant protein production. In this study, we determined whether these stress-minimisation techniques can be successfully applied to industrially relevant high cell density Escherichia coli fermentations generating a recombinant protein prone to forming inclusion bodies, CheY–GFP. Flow cytometry was used as a routine technique to rapidly determine bacterial productivity and physiology at the single cell level, enabling determination of culture heterogeneity. We show that stress minimisation can be applied to high cell density fermentations (up to a dry cell weight of >70 g L^?1) using semi-defined media and glucose or glycerol as carbon sources, and using early or late induction of recombinant protein production, to produce high yields (up to 6 g L^?1) of aggregation-prone recombinant protein in a soluble form. These results clearly demonstrate that stress minimisation is a viable option for the optimisation of high cell density industrial fermentations for the production of high yields of difficult-to-produce recombinant proteins, and present a workflow for the application of stress-minimisation techniques in a variety of fermentation protocols.     

Simple fed-batch technique for high cell density cultivation of Escherichia coli

A simple fed-batch process for high cell density cultivation of Escherichia coli TG1 was developed. A pre-determined feeding strategy was chosen to maintain carbon-limited growth using a defined medium. Feeding was carried out to increase the cell mass concentration exponentially in the bioreactor controlling biomass accumulation at growth rates which do not cause the formation of acetic acid (μ < μ_crit). Cell concentrations of 128 and 148 g per 1 dry cell weight (g 1⁻¹ DCW) were obtained using glucose or glycerol as carbon source, respectively.     

The use of flow cytometry to study the impact of fluid mechanical stress on Escherichia coli W3110 during continuous cultivation in an agitated bioreactor

Continuous culture fermentations of Escherichia coli W3110 have been carried out at controlled dissolved oxygen levels of 40% and 10% of saturation. Satisfactory and reproducible results were obtained. Agitation speeds of 400 and 1200 rpm at an aeration rate of 1 vvm have been used as well as an aeration rate of 3 vvm at 400 rpm. The upper levels of these variables represent much higher agitation and aeration intensities than those normally used in practical fermentations. The fermentations were monitored by mass spectrometry and optical density, and cell samples were studied by flow cytometry, SEM, and TEM. Protocols were developed so the state of both cell membranes and cell size could be measured by flow cytometry. Under all the conditions of agitation and aeration, flow cytometric analysis indicated that both cell membranes were intact and that a cytoplasmic membrane potential existed; also the cell size did not change, results confirmed by SEM and TEM. There were no detectable changes in off-gas analysis or optical density during the continuous fermentation nor in the cell structure as revealed by SEM or TEM, except at the highest agitation intensity. Under the latter conditions, after 7 h, the outer polysaccharide layer on the cell was stripped away. It is concluded that any changes in biological performance of this E. coli cell line due to variations in agitation or aeration intensity or scale of operation cannot be attributed to fluid dynamic stresses associated with the turbulence generated by impellers or with bursting bubbles.     

Proteomic profiling of Escherichia coli proteins under high cell density fed-batch cultivation with overexpression of phosphogluconolactonase

In this study, we used proteomics to better understand the growth on glucose of Escherichia coli in high cell density, fed-batch cultures and the response to overexpression of plasmid-encoded 6-phosphogluconolactonase (PGL). Using liquid chromatography coupled to electrospray mass spectrometry, at least 300 proteins were identified in the cytosolic fraction of the six time points used to monitor the fermentation. The relative abundance changes of selected proteins were obtained by comparing the peak area of the corresponding peptides at a particular m/z (mass over charge ratio) value. During the time course of samples collected during the rapid growth achieved under batch and fed-batch conditions, both the control and recombinant E. coli strains showed up-regulation of proteins participating in the tricarboxylic acid (TCA) cycle, particularly acetyl-CoA synthetase (AcCoAS), malate dehydrogenase (MDH), and succinyl-CoA synthetase (SuccCoAS). In the recombinant strain culture, fumarase was up-regulated until 35 h after inoculation but was not in the control strain culture. In addition, the proteomic measurement detected up-regulation of three well-characterized binding transport proteins in both control and recombinant strains. The up-regulation of TCA cycle enzymes is consistent with the increase in growth rate observed in the cell culture. In addition, up-regulation of these proteins demonstrated the importance of both the pentose-phosphate shunt and TCA cycle to the increased biosynthetic activity required by a high level protein synthesis. This study shows the potential of proteomics using shotgun sequencing (LC/MS of tryptic digests) to measure global changes in protein abundance during a fermentation process and will facilitate the development of robust manufacturing systems.     

Enhanced production of the nonribosomal peptide antibiotic valinomycin in Escherichia coli through small-scale high cell density fed-batch cultivation

Nonribosomal peptides (NRPs), a large family of natural products, possess numerous pharmaceutically significant bioactivities. However, many native microbial producers of NRPs are not cultivable or have low production yields making mass production infeasible. The recombinant production of natural products in a surrogate host has emerged as a strategy to overcome these limitations. De novo recombinant production of the NRP antibiotic valinomycin in an engineered Escherichia coli host strain was established with the necessary biosynthetic pathway constituents from Streptomyces tsusimaensis. In the present study, the initially modest valinomycin yields could be significantly increased from 0.3 up to 2.4 mg L^?1 by switching from a batch to an enzyme-based fed-batch mode in shake flasks. A subsequent design of experiment-driven optimization of parallel fed-batch cultivations in 24-well plates with online monitoring of dissolved oxygen and pH led to valinomycin yields up to 6.4 mg L^?1. Finally, repeated glucose polymer feeding to enzyme-based high cell density cultivations in shake flasks resulted in cell densities of OD₆₀₀ >50 and a valinomycin titer of appr. 10 mg L^?1. This represents a 33-fold improvement compared to the initial batch cultivations and is the highest concentration of a nonribosomal peptide which has been produced in E. coli without feeding of specific precursors so far to our knowledge. Also, such a small-scale optimization under fed-batch conditions may be generally applicable for the development and scale-up of natural product production processes in E. coli.     

Control of endotoxin release in Escherichia coli fed-batch cultures

High amounts of outer membrane (OM) components were released in glucose-limited fed-batch (GLFB) cultures at 37 °C at specific growth rates approaching 0.05 h⁻¹. Endotoxin analyses from a 20 °C GLFB culture gave similar results. An alternative fermentation technique, the temperature-limited fed-batch (TLFB) technique, reduced the endotoxin concentration in a culture with a biomass concentration of 30 g l⁻¹ from the 850 mg l⁻¹ in traditional GLFB cultures to about 20 mg l⁻¹. The TLFB technique uses the temperature to regulate the dissolved oxygen tension, while all substrate components are unregulated. It appears to be severe glucose limitation that triggers the extensive release of endotoxins rather than a low growth rate. Furthermore, it is not the low temperature that stabilizes the OM when using the TLFB technique. Simulations and experimental data show that this technique results in the same biomass productivity as the GLFB technique.     

Co-expression of bacterial hemoglobin overrides high glucose-induced repression of foreign protein expression in Escherichia coli W3110

Co-expression of Vitreoscilla hemoglobin (VHb) can enhance production of foreign proteins in several microorganisms, including Escherichia coli. Production of foreign proteins [green fluorescent protein (GFP) and organophosphorous hydrolase (OPH)] has been examined in two typical industrial E. coli strains, W3110 (a K12 derivative) and BL21 (a B derivative). In particular, we investigated the effects of VHb co-expression and media glucose concentration on target protein production. We employed the nar O(2)-dependent promoter for self-tuning of VHb expression based on the natural changes in dissolved O(2) levels over the duration of culture. Foreign protein production in strain BL21 was decreased by a high glucose concentration but co-expression of VHb had no effect on this. In contrast, co-expression of VHb in strain W3110 overrode the glucose-induced repression and resulted in steady expression of foreign proteins.     

Analysis of Escherichia coli cell state by flow cytometry during whole cell catalyzed biotransformation for l-carnitine production

Flow cytometry was used to monitor Escherichia coli cellular state during the biotransformation of crotonobetaine into l-carnitine using growing and resting cells in batch and high-cell-recycle continuous membrane reactors. The cell physiological state and the DNA, RNA and protein cell content were analyzed during the bioprocess. The cell growth cycle was followed by reference to cellular DNA concentration and the entry in the stationary phase resulted in an increase in intracellular protein. The biochemical activity of resting cells was assessed for the first time at the molecular level, protein synthesis being observed despite the absence of nutrients. Freely suspended growing, both in batch and continuous cultures, and, more importantly, resting E. coli cells were seen to be made up of subpopulations differing in reproductive ability, metabolic activity and membrane integrity. In the case of growing cells, biotransformation was mostly performed by fully viable cells (68–75%), while in a resting cell system, also dead cells (1–5%) and cells with doubtful viability (60–70%) appeared to be involved in the process; in later stages, a population made up of phantom cells, containing little or no cellular DNA, was detected. In cell-recycle continuous reactors, the recording of DNA (40 to 60 fg), RNA (50 to 120 fg) and protein (100 to 220 fg) levels per unit of cell, and the evolution of cell population heterogeneity (three different populations of cells) threw light on the stress conditions imposed by high cell densities. The use of FCM allowed to follow the recovery of cell catalytic activity for resting biotransformation batch processes, thus showing its potential for the optimization of bioprocesses.     

Death of the Escherichia coli K-12 strain W3110 in soil and water.

Whether Escherichia coli K-12 strain W3110 can enter the "viable but nonculturable" state was studied with sterile and nonsterile water and soil at various temperatures. In nonsterile river water, the plate counts of added E. coli cells dropped to less than 10 CFU/ml in less than 10 days. Acridine orange direct counts, direct viable counts, most-probable-number estimates, and PCR analyses indicated that the added E. coli cells were disappearing from the water in parallel with the number of CFU. Similar results were obtained with nonsterile soil, although the decline of the added E. coli was slower. In sterile water or soil, the added E. coli persisted for much longer, often without any decline in the plate counts even after 50 days. In sterile river water at 37 degrees C and sterile artificial seawater at 20 and 37 degrees C, the plate counts declined by 3 to 5 orders of magnitude, while the acridine orange direct counts remained unchanged. However, direct viable counts and various resuscitation studies all indicated that the nonculturable cells were nonviable. Thus, in either sterile or nonsterile water and soil, the decline in plate counts of E. coli K-12 strain W3110 is not due to the cells entering the viable but nonculturable state, but is simply due to their death.     

Use of high density cultures of Escherichia coli for high level production of recombinant Pseudomonas aeruginosa exotoxin A

Summary An efficient fermentation method for the production of two modified recombinant Pseudomonas aeruginosa exotoxin As cloned in Escherichia coli BL21(DE3) was developed. Cell densities of 16–30 g dry weight/l were found to be most suitable for the induction of protein synthesis, which was under the isopropyl \-d-thiogalactopyranoside (IPTG)-inducible T7 expression system. A concentration of 0.6 mm IPTG and induction time of 90 min were found to give the best results for production of the modified toxins. Using this procedure, gram amounts of the proteins were obtained in a 3-1 bench-top fermentor. The high density growth of the bacteria did not impair the integrity of the proteins and did not interfere with the purification procedure. Offsprint requests to: J. Shiloach     

Kinetics of inclusion body production in batch and high cell density fed-batch culture of Escherichia coli expressing ovine growth hormone.

A process for maximizing the volumetric productivity of recombinant ovine growth hormone (r-oGH) expressed in Escherichia coli during high cell density fermentation process has been devised. Kinetics of r-oGH expression as inclusion bodies and its effect on specific growth rates of E. coli cells were monitored during batch fermentation process. It was observed that during r-oGH expression in E. coli, the specific growth rate of the culture became an intrinsic property of the cells which reduced in a programmed manner upon induction. Nutrient feeding during protein expression phase of the fed-batch process was designed according to the reduction in specific growth rate of the culture. By feeding yeast extract along with glucose during fed-batch operation, high cell growth with very little accumulation of acetic acid was observed. Use of yeast extract helped in maintaining high specific cellular protein yield which resulted in high volumetric productivity of r-oGH. In 16 h of fed-batch fermentation, 3.2 g l-1 of r-oGH were produced at a cell OD of 124. This is the highest concentration of r-oGH reported to date using E. coli expression system. The volumetric productivity of r-oGH was 0.2 g l-1 h-1, which is also the highest value reported for any therapeutic protein using IPTG inducible expression system in a single stage fed-batch process.     

Production of tilapia insulin-like growth factor-2 in high cell density cultures of recombinant Escherichia coli

An improved expression plasmid pET-insulin-like growth factor-2 (IGF2) was constructed and transferred into Escherichia coli BL21(DE3) for the expression of tilapia insulin-like growth factor-2. The recombinant insulin-like growth factor-2 was produced as inclusion bodies, and the recombinant insulin-like growth factor-2 content was as high as 10.3% of the total protein content. For production of recombinant insulin-like growth factor-2 in E. coli, pH-stat fed-batch cultures were used to achieve a high cell density culture. A cell concentration 183gl(-1) dry cell weight (DCW) was obtained after 30h cultivation and plasmid stability was maintained at high levels. Expression of insulin-like growth factor-2 was induced at three different cell concentrations, 50, 78.5, and 114.5gl(-1) dry cell weight. When cells were induced at a cell concentration of 114.5gl(-1) dry cell weight, the amount of insulin-like growth factor-2 produced was 9.69gl(-1) (11.3% of the total protein). Using a simple purification process including inclusion body isolation, denaturation, refolding and Ni-NTA affinity chromatography, 19.51mg of insulin-like growth factor-2 was obtained from a 22.5ml of culture, and the recovery yield was 20.5%. The biological activity of the purified IGF-2 was demonstrated as promoting the growth of four different cell lines by the colorimetric bioassay and the best growth stimulation ratio was obtained for the Balb/3T3 clone 31A cell line.     

Quantitative modeling of inducer transport in fed-batch cultures of Escherichia coli

An unsteady, unstructured, unsegregated and based on first principles mathematical model has been proposed to describe IPTG (isopropyl-β-d-tiogalactopiranoside) transport in induced fed-batch cultures of E. coli M15 ΔglyA [pQEαβrham] [pREP4] producing rhamnulose 1-phosphate aldolase (RhuA). The model predicts extracellular and intracellular IPTG concentration. Experimental extracellular IPTG concentrations under different operational conditions were obtained by HPLC–MS analysis. These experimental data were used to fit the parameters of the model. The model was also able to predict the experimental behavior of two different E. coli strains producing fuculose 1-phosphate aldolase (FucA). IPTG transport to cells was the contribution of three processes: a diffusion process, and two active processes (one non-specific and another specific).