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Applied and Environmental Microbiology, August 2003, p. 4737-4742, Vol. 69, No. 8
0099-2240/03/$08.00+0 DOI: 10.1128/AEM.69.8.4737-4742.2003
Copyright © 2003, American Society for Microbiology. All Rights Reserved.
Metabolic and Biomolecular Engineering National Research Laboratory, Department of Chemical and Biomolecular Engineering and BioProcess Engineering Research Center,1 Department of BioSystems and Bioinformatics Research Center,3 Center for Ultramicrochemical Process Systems, Korea Advanced Institute of Science and Technology, Yuseong-gu, Daejeon 305-701, Korea2
Received 10 March 2003/ Accepted 10 June 2003
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It has been well known that the overproduction of recombinant proteins acts as a stress on the cells, resulting in induction of stress-responsive genes such as dnaK, groEL, ibpA, ibpB, and ompT (10, 17). Furthermore, the yield and specific productivity of recombinant proteins obtained by high-cell-density culture are generally lower than those obtained by flask cultures (9, 21). Since these problems are caused by unknown complex metabolic events, systematic understanding of the physiology and metabolism altered during the fed-batch culture of recombinant E. coli, especially those altered before and after induction, is essential to develop strategies for solving these problems. Transcriptome analysis employing high-density DNA microarrays is well suited for the elucidation of global physiological and metabolic changes. However, most microarray-based studies of transcriptome profiling in E. coli have been carried out in flask cultures (18, 19). In flask cultures, cells grow to a relatively low density, and the growth environment is continuously changing. Therefore, the results of transcriptome profiling obtained in flask cultures cannot be extended to high-cell-density fed-batch cultures, which are industrially relevant processes.
Recently, combined transcriptome and proteome analysis of E. coli during high-cell-density culture was reported (21). The expression of many genes including those of tricarboxylic acid cycle enzymes, NADH dehydrogenase, and ATPase was up-regulated during the exponential fed-batch period and was down-regulated afterwards. Interestingly, the expression of most amino acid biosynthesis genes was down-regulated as the cell density increased (21).
In this study, we extended our previous work and applied transcriptome profiling to understand physiological changes of recombinant E. coli producing human insulin-like growth factor I fusion protein (IGF-If) during the high-cell-density fed-batch culture. We were able to rationally select two down-regulated genes after induction and subsequently used them to develop engineered strains that were capable of enhanced production of IGF-If.
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TABLE 1. Bacterial strains and plasmids used in this study
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FIG. 1. Schematic drawing of plasmids pJHlacL-prsA (A) and pJHlacL-prsAglpF (B). The plasmids are compatible with IGF-If expression plasmid pYKM-I1. Both the glpF and prsA genes are under the control of the lac promoter, which can be induced by IPTG.
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Analytical methods.
During the fed-batch cultivation, cell growth was monitored by measuring the absorbance at 600 nm (optical density at 600 nm; DU Series 600 spectrophotometer; Beckman, Fullerton, Calif.). DCW (grams per liter) was determined as described previously (1). Protein samples were analyzed by electrophoresis on a sodium dodecyl sulfate-12% (wt/vol) polyacrylamide gel (12). The protein bands were visualized with Coomassie brilliant blue R-250 stain (Bio-Rad Laboratories, Hercules, Calif.). The contents of IGF-If in total protein were quantified with a GS710 calibrated imaging densitometer (Bio-Rad). The total protein concentration was determined with a protein assay kit (Bio-Rad) with bovine serum albumin as a standard.
Microarray experiments.
We used the Panorama E. coli gene array (Sigma-Genosys, Inc., Woodlands, Tex.), which contains all the open reading frames in the E. coli chromosome. To make hybridization probes for the E. coli DNA microarray, total RNA was isolated from the culture by using the Qiagen RNeasy columns (Valencia, Calif.). The purified RNA (1 µg) was mixed with random hexamer primers for cDNA labeling reaction, which was performed using 50 U of avian myeloblastosis virus reverse transcriptase (Roche, Basel, Switzerland) and 20 µCi of [
-33P]dCTP (2,000 to 3,000 Ci/mmol; New England Nuclear, Boston, Mass.) as recommended by Sigma-Genosys, Inc. The cDNA labeling reaction mixture (30 µl) containing 0.5 mM (each) dATP, dGTP, and dTTP and 10 mM dithiothreitol was incubated for 3 h at 42°C. Unincorporated nucleotides were removed by gel filtration through a G-25 Sephadex column (Amersham Biosciences, Piscataway, N.J.).
The Panorama E. coli gene array (Sigma-Genosys) was hybridized with labeled cDNA concentrates plus 0.8 mg of salmon sperm DNA per ml (Amersham Biosciences). Prior to hybridization, the solution was boiled for 10 min and then cooled to room temperature. After hybridization for 18 h at 65°C, the Panorama membrane was washed with 0.5x SSPE solution (0.09 M NaCl, 5 mM NaH2PO4, and 0.5 mM EDTA [pH 7.7]) and subsequently rinsed with 0.5x SSPE at 65°C for 20 min. The Panorama membrane was scanned with a BAS 1500 (Fuji, Tokyo, Japan) instrument with a pixel size of 100 µm. The signal intensities and local background were determined by Array Vision (Imaging Research Inc., St. Catharines, Ontario, Canada). DNA microarray experiments were carried out in duplicate. Also, the Panorama E. coli gene array contains duplicate spots for each gene. Therefore, a total of four measurements were made for each gene. Raw array data from each experimental replicate were exported from Array Vision into MS Excel for further analysis. The raw data values were normalized and selected as described previously (4). We could select 529 genes that were significantly up- or down-regulated by a value greater than 3 standard deviations of the mean of the log ratios for all genes (99.9% confidence) and those that had a P value greater than 0.05% (95% probability that the ratio is significant).
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FIG. 2. Time profiles of cell density (optical density at 600 nm []), DCW (grams per liter [ ]), IGF-If concentration (grams per liter [ ]), and IGF-If content (percentage of total proteins [ ]) during the fed-batch cultures of E. coli W3110 harboring pYKM-I1 (A), E. coli W3110 harboring pYKM-I1 and pJHlacL-prsA (B), and E. coli W3110 harboring pYKM-I1 and pJHlacL-prsAglpF (C). Vertical dashed lines indicate the time point of induction with 1 mM IPTG. The arrows in panel A are the sampling points for transcriptome analyses.
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TABLE 2. Selected genes that are up-regulated after IPTG induction
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TABLE 3. Selected genes that are down-regulated after IPTG induction
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Second, the expression of the genes associated with the biosynthesis of nucleotides and amino acids was down-regulated. For example, the expression of the metL gene was most significantly down-regulated after induction (Table 3). It is interesting that the expression of the metB gene, which forms an operon with the metL gene, was also significantly down-regulated after induction. This suggests the existence of good correlation between the metBL operon structure and the transcript levels of the metB and metL genes. In addition, the expression of the genes in the biosynthetic pathways of serine, cysteine, glutamate, glutamine, arginine, aspartate, threonine, isoleucine, valine, and histidine was slightly down-regulated. It was notable that the expression of the prsA gene was severely down-regulated (>2.7-fold). Ribose-phosphate pyrophosphokinase encoded by the prsA gene is involved in the first step for the biosynthesis of purine, pyrimidine, and nicotinamide nucleotides and for the biosynthesis of histidine and tryptophan. Therefore, it was reasoned that nucleic and amino acid depletion may become a bottleneck in protein production during the high-cell-density fed-batch culture of recombinant E. coli.
Third, in the energy and carbon metabolism, the genes in the tricarboxylic acid cycle showed a relatively constant expression level, while the expression of the genes in the glycolytic pathway, such as gapA, eno, and tpiA, was up-regulated. In this work, glycerol was used as a carbon source, because it allowed production of more IGF-If than glucose did in a previous study (3). The growth rate with glycerol is about 74% of that achievable with glucose (8). It was notable that the expression of the glpF gene encoding a glycerol transporter was significantly down-regulated (>2.2-fold) after induction. Therefore, it was thought that the reduced transport of glycerol might have become a limiting factor for the production of IGF-If.
Among the other genes that showed altered expression levels, but less-than-twofold changes, were stress-responsive genes including dnaK, ibpA, and ibpB. They were up-regulated by 1.6-, 1.6-, and 1.8-fold, respectively, which has been a well-known phenomenon during recombinant protein production (5, 6, 10). However, the expression level of the groEL gene was not changed. Moreover, the expression of the ompT gene was significantly down-regulated (Table 3), coinciding with results previously reported (21).
Effect of prsA coexpression on IGF-If production.
Among the down-regulated genes, we selected the prsA gene as the first candidate for amplification, as its product ribose-phosphate pyrophosphokinase is a key enzyme for the biosynthesis of nucleic acids and amino acids. The 5-phosphoribosyl-1-pyrophosphate (PRPP) produced by PrsA is of importance for the biosynthesis of purine, pyrimidine, and nicotinamide nucleotides and of histidine and tryptophan. Since the expression level of the prsA gene was significantly decreased after induction, PRPP might be limiting. Therefore, it was reasoned that increasing the level of PrsA would result in the sufficient supply of PRPP for synthesis of purine, pyrimidine, and amino acids and consequently increase the protein production during high-cell-density culture. The effect of the prsA gene coexpression on IGF-If production was investigated by carrying out the pH-stat fed-batch culture of E. coli W3110 harboring pYKM-I1 and pJHlacL-prsA (Fig. 2B). The specific growth rate during the exponential phase was 0.16 h-1, which is lower than that of W3110 harboring pYKM-I1 only. The maximum cell concentration of 34.2 ± 2.12 (± standard deviation) g (DCW)/liter was obtained in 24 h. The IGF-If content reached 22% of total protein at 5 h after IPTG induction, which is 2.3 times higher than that obtained without the coexpression of the prsA gene, and then was maintained constantly afterwards. The IGF-If concentration reached a maximum value of 3.6 ± 0.19 g/liter at 12 h after induction. The volumetric productivity of IGF-If was 0.64 ± 0.034 g/liter/h, which is 1.8 times higher than that obtained with W3110 harboring pYKM-I1 only. Therefore, the coexpression of the prsA gene resulted in the increase of recombinant protein production, possibly by increasing the metabolic fluxes towards the biosynthesis of nucleic acids and amino acids. However, the growth rate was lower than that of E. coli W3110 harboring pYKM-I1 only.
Enhancement of volumetric productivity of IGF-If by the coexpression of prsA and glpF genes.
To further enhance the volumetric productivity of IGF-If, we decided to develop a strategy for restoring the growth rate of W3110 harboring pYKM-I1 and pJHlacL-prsA to a value close to that of W3110 harboring pYKM-I1 only. In this study, glycerol was used as a carbon source for the production of recombinant IGF-If. Unlike other carbohydrates, glycerol enters the cytoplasm by facilitated diffusion across the cytoplasmic membrane by use of the facilitator protein GlpF. The expression level of the glpF gene was significantly decreased after induction (Table 3). It means that the cell's ability to transport glycerol is significantly decreased after induction. In order to increase glycerol transport, the E. coli glpF gene was coexpressed in E. coli W3110 harboring pYKM-I1. Both the glpF and prsA genes were coexpressed in E. coli W3110 harboring pYKM-I1. The pH-stat fed-batch culture of E. coli W3110 harboring pYKM-I1 and pJHlacL-prsAglpF was then carried out (Fig. 2C). The specific growth rate was 0.22 h-1, which is similar to that of W3110 harboring pYKM-I1 only. The maximum cell concentration of 46.2 ± 2.53 (± standard deviation) g (DCW)/liter was obtained in 20 h. The IGF-If content reached 19.4% of total protein at 5 h after IPTG induction. The IGF-If concentration increased to 4.3 ± 0.24 g/liter at 8 h after induction. The volumetric productivity of IGF-If of 0.82 ± 0.048 g/liter/h was obtained at 6 h after induction, which is 2.3 and 1.3 times higher than those obtained with W3110 harboring pYKM-I1 only and W3110 harboring pYKM-I1 plus pJHlacL-prsA, respectively. The sodium dodecyl sulfate-polyacrylamide gel electrophoresis analysis clearly shows the improvement of IGF-If production by the coexpression of the prsA and glpF genes (Fig. 3). To examine the effect of GlpF on the productivity of IGF-If, the glpF gene alone was coexpressed in E, coli W3110 harboring pYKM-I1. In this case, the level of IGF-If was not increased, but the specific growth rate was increased (data not shown). Therefore, the increased level of GlpF is responsible for better growth of recombinant E. coli producing IGF-If.
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FIG. 3. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis analysis of total proteins of recombinant E. coli W3110 harboring pYKM-I1 (A) and W3110 harboring pYKM-I1 and pJHlacL-prsAglpF (B). Lanes: M, molecular mass markers; 1, proteins prepared before induction; 2 to 7, 1 to 6 h after IPTG induction, respectively. The arrowsindicate recombinant IGF-If.
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