Oxygen transfer correlation in high cell density culture of recombinant E. coli

Summary A recombinant E. coli BL21[pET3a-T2M2] was cultivated in fed-batch cultures and cell mass increased to more than 70g/L. The volumetric oxygen transfer coefficient was estimated in a range of various fermentation parameters (agitation speed, oxygen flow rate and cell mass concentration) and finally the oxygen transfer correlation in bioreactor containing the recombinant E. coli cultures was determined as: k_spla = 0.0195 (P_g/V)^0.55 (V_s)^0.64 (1+2.12X+0.20X²)^–0.25.     

An E. coli expression system optimized for DELLA proteins

The DELLA proteins are involved in regulation of plant growth in response to phytohormonal signals such as GA, ethylene, and auxin. They have become one of most challenging and active area of research due to their fundamental roles in plant biology. Here, we describe the first successful expression of the N-terminal domains of DELLA proteins of Arabidopsis thaliana and Malus domestica in Escherichia coli system which will be used to produce monoclonal antibodies for profiling protein micro-arrays. Optimizations of the cloning, expression, and purification using specific tags have been discussed.     

Genetic selection system for improving recombinant membrane protein expression in E. coli

A major barrier to the physical characterization and structure determination of membrane proteins is low yield in recombinant expression. To address this problem, we have designed a selection strategy to isolate mutant strains of Escherichia coli that improve the expression of a targeted membrane protein. In this method, the coding sequence of the membrane protein of interest is fused to a C‐terminal selectable marker, so that the production of the selectable marker and survival on selective media is linked to expression of the targeted membrane protein. Thus, mutant strains with improved expression properties can be directly selected. We also introduce a rapid method for curing isolated strains of the plasmids used during the selection process, in which the plasmids are removed by in vivo digestion with the homing endonuclease I‐CreI. We tested this selection system on a rhomboid family protein from Mycobacterium tuberculosis (Rv1337) and were able to isolate mutants, which we call EXP strains, with up to 75‐fold increased expression. The EXP strains also improve the expression of other membrane proteins that were not the target of selection, in one case roughly 90‐fold.     

重组GM-CSF/IL-3融合蛋白表达菌发酵研究

基因工程菌的发酵技术是基因工程药物大规模生产所必备的关键技术,本文对于重组ＧＭ－ＣＤＦ／ＩＬ－３融合蛋白表达菌株Ｅ．ｃｏｌｉ ＢＬ２１（ＤＥ３）（ｐＦｕ）的生长及产物表达规律进行了探索,在此基础上进行高密度发酵研究,真体最终发酵密度达ＯＤ６００值６０以上,目的产物占菌体总蛋白２５％以上。     

Robust artificial intelligence tool for automatic start-up of the supplementary medium feeding in recombinant E. coli cultivations

One of the most important events in fed-batch fermentations is the definition of the moment to start the feeding. This paper presents a methodology for a rational selection of the architecture of an artificial intelligence (AI) system, based on a neural network committee (NNC), which identifies the end of the batch phase. The AI system was successfully used during high cell density cultivations of recombinant Escherichia coli. The AI algorithm was validated for different systems, expressing three antigens to be used in human and animal vaccines: fragments of surface proteins of Streptococcus pneumoniae (PspA), clades 1 and 3, and of Erysipelothrix rhusiopathiae (SpaA). Standard feed-forward neural networks (NNs), with a single hidden layer, were the basis for the NNC. The NN architecture with best performance had the following inputs: stirrer speed, inlet air, and oxygen flow rates, carbon dioxide evolution rate, and CO₂ molar fraction in the exhaust gas.     

Glucose-limited high cell density cultivations from small to pilot plant scale using an enzyme-controlled glucose delivery system

The enzyme controlled substrate delivery cultivation technology EnBase(?) Flo allows a fed-batch-like growth in batch cultures. It has been previously shown that this technology can be applied in small cultivation vessels such as micro- and deep well plates and also shake flasks. In these scales high cell densities and improved protein production for Escherichia coli cultures were demonstrated. This current study aims to evaluate the scalability of the controlled glucose release technique to pilot scale bioreactors. Throughout all scales, that is, deep well plates, 3 L bioreactor and 150 L bioreactor cultivations, the growth was very similar and the model protein, a recombinant alcohol dehydrogenase (ADH) was produced with a high yield in soluble form. Moreover, EnBase Flo also was successfully used as a controlled starter culture in high cell density fed-batch cultivations with external glucose feeding. Here the external feeding pump was started after overnight cultivation with EnBase Flo. Final optical densities in these cultivations reached 120 (corresponding to about 40 g L(-1) dry cell weight) and a high expression level of ADH was obtained. The EnBase cultivation technology ensures a controlled initial cultivation under fed-batch mode without the need for a feeding pump. Because of the linear cell growth under glucose limitation it provides optimal and robust starting conditions for traditional external feed-based processes.     

Characterization of lycopene-overproducing E. coli strains in high cell density fermentations

Previous work identified two recombinant strains of Escherichia coli capable of significant lycopene overproduction. These strains were constructed by superimposing the deletion of three genes, selected through combinatorial and systematic searches of the metabolic landscape, onto a previously engineered strain over-expressing critical genes in the lycopene biosynthesis pathway. In this paper, we characterize the performance of these two strains in comparison to the parental, pre-engineered strain. Specifically, high cell density fermentations were performed after identifying optimized putative operating parameters. High oxygen levels and increased pH values were found to be critical for increasing both specific and volumetric product titers. Carbon balances suggest linkages between glutamate, NADPH, formate, and alanine levels with lycopene overproduction. Furthermore, lycopene production reached nearly 220 mg/l from approximately 27 g dry cell weight/l in these reactors, which is the highest value reported to date for E. coli.     

Fed-batch production of recombinant beta-galactosidase using the universal stress promoters uspA and uspB in high cell density cultivations

A high-level production system using the universal stress promoters uspA and uspB in a fed-batch cultivation based on minimal medium was designed. In development it was shown that a standard industrial fed-batch protocol could not be used for this purpose since it failed to induce the levels of product as compared to the basal level. Instead, a batch protocol followed by a low constant feed of glucose was shown to give full induction. The levels of the product protein, beta-galactosidase, corresponded to approximately 25% of the total protein. Higher levels were found using the uspA than uspB vectors where uspA showed considerably higher basal level. The data indicate that the sigma(70) regulated promoter, uspA, although affected by the alarmone guanosine tetraphosphate, ppGpp, worked partly in a similar manner to constitutive promoters. An industrial high cell density fed-batch cultivation on the basis of the suggested fed-batch protocol and the uspA promoter gave a final beta-galatosidase concentration of 7 g/L and a final cell concentration of 65 g/L. The heterogeneity in production of the individual cell was measured by fluorescence microscopy. The data show that there is a process time independent heterogeneity in production, which is suggested to be caused by heterogeneity in the substrate uptake rate of the individual cell.     

Effect of oxygen enrichment aeration on penicillin G acylase production in high cell density culture of recombinant E. coli

A strain of E. coli 9633 harboring pGL-5 is employed to develop the process producing penicillin G acylase (PGA). Medium studies show that 0.8% glucose is a proper initial carbon source concentration in the start medium. Whereas, study of nitrogen sources in the production medium exhibits that 2% soybean meat hydrolysate and 0.5% casein hydrolysate give the best result in terms of cell concentration. High cell density culture is carried out through the application of oxygen enrichment aeration (OEA). With the treatment of OEA, the cell concentration and specific PGA activity raise to 2.1 and 1.4 times, respectively, as compared to those without OEA. In a 75 l fermentor, the cell concentration can reach 323 (g wet cell weight/l) with a specific PGA activity of 47 (IU/g w.w.) after 24?h under OEA treatment. This means that the PGA activity of the broth can reach 15 (IU/ml).     

Comparative proteomic analysis of high cell density cultivations with two recombinant Bacillus megaterium strains for the production of a heterologous dextransucrase

High cell density cultivations were performed under identical conditions for two Bacillus megaterium strains (MS941 and WH320), both carrying a heterologous dextransucrase (dsrS) gene under the control of the xylA promoter. At characteristic points of the cultivations (end of batch, initial feeding, before and after induction) the proteome was analyzed based on two dimensional gel electrophoresis and mass spectrometric protein identification using the protein database "bmegMEC.v2" recently made available.     

Fuzzy neural network for the control of high cell density cultivation of recombinant Escherichia coli

A five-layer fuzzy neural network (FNN) was developed for the control of fed-batch cultivation of recombinant Escherichia coli JM103 harboring plasmid pUR 2921. The FNN was believed to represent the membership functions of the fuzzy subsets and to implement fuzzy inference using previous experimental data. This FNN was then used for compensating the exponential feeding rate determined by the feedforward control element. The control system is therefore a feedforward-feedback type. The change in pH of the culture broth and the specific growth rate were used as the inputs to FNN to calculate the glucose feeding rate. A cell density of 84 g DWC/l in the fed-batch cultivation of the recombinant E. coli was obtained with this control strategy. Two different FNNs were then employed before and after induction to enhance plasmid-encoded β-galactosidase production. Before induction the specific growth rate was set as 0.31 h⁻¹, while it was changed to 0.1 h⁻¹ after induction. Compared to when only one FNN was used, the residual glucose concentration could be tightly controlled at an appropriate level by employing two FNNs, resulting in an increase in relative activity of β-galactosidase which was about four times greater. The present investigation demonstrates that a feedforward-feedback control strategy with FNN is a promising control strategy for the control of high cell density cultivation and high expression of a target gene in fed-batch cultivation of a recombinant strain.     

重组铜绿假单胞菌外毒素A工程菌的高密度发酵与表达

高密度培养表达大肠杆菌生产重组铜绿假单胞菌外毒素A(rEPA)。用上海高机公司的30L自控发酵罐,采用分批补料培养技术,维持葡萄糖的浓度始终处于较低的水平,并分批补加氮源,同时溶氧控制在30%～40%,pH自动调控至7.0,培养至对数中期进行诱导。重组菌最终发酵液光密度(A600)未诱导时达到44,诱导时达到36,在上清液中表达的rEPA蛋白的含量占总蛋白的28.1%,在菌体中表达蛋白含量占总蛋白的4.7%。本实验为rE-PA的大规模生产奠定了基础。     

High cell density and high expression of recombinant human ApoA-Imilano in Eschenichia coli by twice temperature-shifted induction

The effect of temperature on the formation of recombinant protein,apolipoprotein A-IMilano was investigated in the present study.The temperature of the initial growth phase was set at 30℃,while temperature variation in induction phase was arranged in three modes.High cell-density culture of Escherichia coli and high expression of recombinant human by twice temperature-shifted induction were carried out.Experimental results showed that ApoA-IMilano reached 4.8 g/L with the final cell density of OD600,150.It was found that twice temperature-shifted induction could successfully avoid the effect of acetic acid on cell density and the expression of the product.The present study provides a basic procedure for the production of recombinant ApoA-IMilano.     

High cell density and high expression of recombinant human ApoA-IMilano in Escherichia coli by twice temperature-shifted induction

The effect of temperature on the formation of recombinant protein, apolipoprotein A-I_Milano was investigated in the present study. The temperature of the initial growth phase was set at 30°C, while temperature variation in induction phase was arranged in three modes. High cell-density culture of Escherichia coli and high expression of recombinant human by twice temperature-shifted induction were carried out. Experimental results showed that ApoA-I_Milano reached 4.8 g/L with the final cell density of OD₆₀₀, 150. It was found that twice temperature-shifted induction could successfully avoid the effect of acetic acid on cell density and the expression of the product. The present study provides a basic procedure for the production of recombinant ApoA-I_Milano.     

Application of dielectric spectroscopy for monitoring high cell density in monoclonal antibody producing CHO cell cultivations

The application of dielectric spectroscopy was frequently investigated as an on-line cell culture monitoring tool; however, it still requires supportive data and experience in order to become a robust technique. In this study, dielectric spectroscopy was used to predict viable cell density (VCD) at industrially relevant high levels in concentrated fed-batch culture of Chinese hamster ovary cells producing a monoclonal antibody for pharmaceutical purposes. For on-line dielectric spectroscopy measurements, capacitance was scanned within a wide range of frequency values (100–19,490 kHz) in six parallel cell cultivation batches. Prior to detailed mathematical analysis of the collected data, principal component analysis (PCA) was applied to compare dielectric behavior of the cultivations. PCA analysis resulted in detecting measurement disturbances. By using the measured spectroscopic data, partial least squares regression (PLS), Cole–Cole, and linear modeling were applied and compared in order to predict VCD. The Cole–Cole and the PLS model provided reliable prediction over the entire cultivation including both the early and decline phases of cell growth, while the linear model failed to estimate VCD in the later, declining cultivation phase. In regards to the measurement error sensitivity, remarkable differences were shown among PLS, Cole–Cole, and linear modeling. VCD prediction accuracy could be improved in the runs with measurement disturbances by first derivative pre-treatment in PLS and by parameter optimization of the Cole–Cole modeling.     

Over-expression of recombinant human interferon-gamma in high cell density fermentation of Escherichia coli

Human interferon-gamma (hIFN-gamma) was expressed in Escherichia coli BL21(DE3) under the control of the T7 promoter. Glucose was used as the sole source of carbon and energy with simple exponential feeding rate in fed-batch process. Cell density of recombinant E. coli was reached to 100 g dry wt l(-1) under both constant (0.12 h(-1)) and variable (0.12-0.52 h(-1)) specific growth rates. In the variable specific growth rate fed-batch process, plasmid stability and specific yield of rhIFN-gamma were greater than constant specific growth rate fed-batch process. The final specific yield and overall productivity of rhIFN-gamma were 0.35 +/- 0.02 g rhIFN-gamma g(-1) dry cell wt and 0.9 +/- 0.05 g rhIFN-gamma l(-1) h(-1) in the variable specific growth rate fed-batch process, respectively.     

Enzyme controlled glucose auto-delivery for high cell density cultivations in microplates and shake flasks

Background

Here we describe a novel cultivation method, called EnBase?, or enzyme-based-substrate-delivery, for the growth of microorganisms in millilitre and sub-millilitre scale which yields 5 to 20 times higher cell densities compared to standard methods. The novel method can be directly applied in microwell plates and shake flasks without any requirements for additional sensors or liquid supply systems. EnBase is therefore readily applicable for many high throughput applications, such as DNA production for genome sequencing, optimisation of protein expression, production of proteins for structural genomics, bioprocess development, and screening of enzyme and metagenomic libraries.

Results

High cell densities with EnBase are obtained by applying the concept of glucose-limited fed-batch cultivation which is commonly used in industrial processes. The major difference of the novel method is that no external glucose feed is required, but glucose is released into the growth medium by enzymatic degradation of starch. To cope with the high levels of starch necessary for high cell density cultivation, starch is supplied to the growing culture suspension by continuous diffusion from a storage gel. Our results show that the controlled enzyme-based supply of glucose allows a glucose-limited growth to high cell densities of OD₆₀₀ = 20 to 30 (corresponding to 6 to 9 g l^-1 cell dry weight) without the external feed of additional compounds in shake flasks and 96-well plates. The final cell density can be further increased by addition of extra nitrogen during the cultivation. Production of a heterologous triosphosphate isomerase in E. coli BL21(DE3) resulted in 10 times higher volumetric product yield and a higher ratio of soluble to insoluble product when compared to the conventional production method.

Conclusion

The novel EnBase method is robust and simple-to-apply for high cell density cultivation in shake flasks and microwell plates. The potential of the system is that the microbial growth rate and oxygen consumption can be simply controlled by the amount (and principally also by the activity) of the starch-degrading enzyme. This solves the problems of uncontrolled growth, oxygen limitation, and severe pH drop in shaken cultures. In parallel the method provides the basis for enhanced cell densities. The feasibility of the new method has been shown for 96-well plates and shake flasks and we believe that it can easily be adapted to different microwell and deepwell plate formats and shake flasks. Therefore EnBase will be a helpful tool especially in high throughput applications.     

Development of an optimized expression system for the screening of antibody libraries displayed on the Escherichia coli surface.

Polypeptide library screening technologies are critically dependent upon the characteristics of the expression system employed. A comparative analysis of the lpp-lac, tet and araBAD promoters was performed to determine the importance of tight regulation and expression level in library screening applications. The surface display of single-chain antibody (scFv) in Escherichia coli as an Lpp-OmpA' fusion was monitored using a fluorescently tagged antigen in conjunction with flow cytometry. In contrast to the lpp-lac promoter, both tet and araBAD promoters could be tightly repressed. Tight regulation was found to be essential for preventing rapid depletion of library clones expressing functional scFv and thus for maintaining the initial library diversity. Induction with subsaturating inducer concentrations yielded mixed populations of uninduced and fully induced cells for both the tet and araBAD expression systems. In contrast, homogeneous expression levels were obtained throughout the population using saturating inducer concentrations and could be adjusted by varying the induction time and plasmid copy number. Under optimal induction conditions for the araBAD system, protein expression did not compromise either cell viability or library diversity. This expression system was used to screen a library of random scFv mutants specific for digoxigenin for clones exhibiting improved hapten dissociation kinetics. Thus, an expression system has been developed which allows library diversity to be preserved and is generally applicable to the screening of E. coli surface displayed libraries.