Production of recombinant human granulocyte-colony-stimulating factor in high cell density yeast cultures

The recombinant human granulocyte-colony-stimulating factor (rhG-CSF) was synthesized in a fusion protein using a GAL1-10 UAS in recombinant Saccharomyces cerevisiae and the intracellular KEX2 cleavage led excretion of mature rhG-CSF into the extracellular culture broth. The recombinant yeast growth in fed-batch cultures was controlled by precise computer-aided medium feed. The optimal C/N ratio in preinduction (glucose/Casamino acids) and post-induction (galactose/yeast extract) feed media was determined at 3 and 2, respectively. The final rhG-CSF and cell concentration was more than 60 mg/L and 70 g/L, respectively, with around 90% plasmid stability and negligible ethanol accumulation. Comparing the cell growth between the hG-CSF + and hG-CSF - recombinant strains shows that the cloned gene product does not hamper the host cell growth.     

Plasmid stability and alpha-amylase production in batch and continuous cultures of Bacillus subtilis TN106[pAT5

Cell growth and enzyme (alpha-amylase) production characteristics of Bacillus subtilis TN106 containing the recombinant plasmid pAT5 are investigated in batch and continuous cultures using a defined medium with glucose as the limiting nutrient. The batch culture studies demonstrate that the recombinant plasmid, reported earlier(1) to be stably maintained in the host, suffers from segregational and structural instabilities. The structural instability of this strain occurred during culture storage and can be eliminated in bioreactor experiments by using a modified inoculum preparation procedure. Such elimination allows an unbiased investigation of segregational instability via continuous culture studies. Such studies conducted with this fast growing microorganism, in the absence of antibiotic selection pressure, indicate a very efficient glucose utilization (very low residual glucose concentrations) over a wide range of dilution rates (0.16 h(-1) - 0.94 h(-1)). The nearly time-invariant and low residual glucose concentrations at each such dilution rate enable convenient estimation of growth parameters of the host and recombinant cells and frequency of segregational instability from transients in the resulting mixed cultures. The specific alpha-amylase activity exhibits an inverse relationship to the specific growth rate of recombinant cells. The growth of recombinant cells is not affected by the presence of antibiotic (kanamycin). The growth advantage of host cells over recombinant cells diminishes with increasing dilution rate.     

Growth-rate-independent production of recombinant glucoamylase by Fusarium venenatum JeRS 325

Most recombinant proteins generated in filamentous fungi are produced in fed-batch cultures, in which specific growth rate normally decreases progressively with time. Because of this, such cultures are more suited to the production of products that are produced efficiently at low-growth rates (e.g., penicillin) than to products which are produced more efficiently at high-growth rates (e. g., glucoamylase). Fusarium venenatum A3/5 has been transformed (JeRS 325) to produce Aspergillus niger glucoamylase (GAM) under the control of the Fusarium oxysporum trypsin-like protease promoter. No glucoamylase was detected in the culture supernatant during exponential growth of F. venenatum JeRS 325 in batch culture. In glucose-limited chemostat cultures, GAM concentration increased with decrease in dilution rate, but the specific production rate of GAM (g GAM [g biomass](-1) h(-1)) remained approximately constant over the dilution-rate range 0.05 h to 0.19 h(-1), i.e., the recombinant protein was produced in a growth-rate-independent manner. The specific production rate decreased at dilution rates of 0.04 h(-1) and below. Specific production rates of 5.8 mg and 4.0 mg GAM [g biomass](-1) h(-1) were observed in glucose-limited chemostat cultures in the presence and absence of 1 g mycological peptone L(-1). Compared to production in batch culture, and for the same final volume of medium, there was no increase in glucoamylase production when cultures were grown in fed-batch culture. The results suggested that a chemostat operated at a slow dilution rate would be the most productive culture system for enzyme production under this trypsin-like promoter.     

High-level production of recombinant human IFN-α2a with co-expression of tRNAArg(AGG/AGA) in high-cell-density cultures ofEscherichia coli

The co-expression of theargU gene in a double-vector expression system of recombinantEscherichia coli BL21(DE3)[pET-IFN2a+pAC-argU] significantly enhanced the production level of recombinant human interferon-α2a (rhIFN-α2a) in high cell density cultures compared to a recombinantE coli culture containing only the single expression vector, pET-IFN2a. The dry cell mass concentration increased to almost 100 g/L, and more than 4 g/L of rhIFN-α2a was accumulated in the culture broth. Evidently, the synthesis of rhIFN-α2a was strongly dependent on the pre-induction growth rate and more efficient at a higher specific growth rate. The additional supply of tRNA^Arg(AGG/AGA) enhanced the expression level of the rhIFN-α2a gene in the early stage of the post-induction phase, yet thereafter the specific production rate of rhIFN-α2a rapidly decreased due to severe segregational instability of plasmid vector pET-IFN2a. It would appear that the plasmid instability, which only occurred to pET-IFN2a in the double vector system, was related to the effect of translational stress due to the overexpression of rhIFN-α2a.     

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.     

Production of heterologous thermostable glycoside hydrolases and the presence of host-cell proteases in substrate limited fed-batch cultures of Escherichia coli BL21(DE3)

Metabolic stress is a phenomenon often discussed in conjunction with recombinant protein production in Escherichia coli. This investigation shows how heterologous protein production and the presence of host cell proteases is related to: (1) Isopropyl-beta- D-thiogalactopyranoside (IPTG) induction, (2) cell-mass concentration at the time of induction, and (3) the presence of metabolites (glutamic acid or those from tryptone soy broth) during the post-induction phase of high cell density fed-batch cultivations. Two thermostable xylanase variants and one thermostable cellulase, all originating from Rhodothermus marinus, were expressed in E. coli strain BL21 (DE3). A three-fold difference in the specific activity of both xylanase variants [between 7,000 and 21,000 U/(g cell dry weight)], was observed under the different conditions tested. Upon induction at high cell-mass concentrations employing a nutrient feed devoid of the metabolites above, the specific activity of the xylanase variants, was initially higher but decreased 2-3 h into the post-induction phase and simultaneously protease activity was detected. Furthermore, protease activity was detected in all induced cultivations employing this nutrient feed, but was undetected in uninduced control cultivations (final cell-mass concentration of 40 g/l(-1)), as well as in induced cultivations employing metabolite-supplemented nutrient feeds. By contrast, maximum specific cellulase activity [between 700 and 900 U/(g cell dry weight)] remained relatively unaffected in all cases. The results demonstrate that detectable host cell proteases was not the primary reason for the decrease in post-induction activity observed under certain conditions, and possible causes for the differing production levels of heterologous proteins are discussed.     

Induction of interleukin-3 by interleukin-1 in the absence of other exogenous stimuli

We have previously reported that lipopolysaccharide (LPS) could induce the production of interleukin-3 (IL-3) by mouse spleen cells. In the present study, we show that recombinant human interleukin-1, in the absence of other stimuli, is able to induce the production of IL-3. IL-3 was detected in the supernatants of adult, although neither in young nor in nude mouse splenocytes and was assessed by its capacity to support the growth of the IL-3-dependent FDC-P2 cell line. The presence of IL-3 was antigenically confirmed with a monoclonal anti-IL-3 antibody. Both recombinant IL-1 alpha and IL-1 beta had similar potential for inducing IL-3 production. IL-3 activity was detected in the supernatants of cells cultured in the presence of 100 pg/ml IL-1; maximal IL-3 levels were obtained with 10-30 ng/ml IL-1. Kinetic studies of IL-1-induced IL-3 production indicated that 4-6 days of culture were required for optimal production, whereas 1-2 days were sufficient in cultures stimulated with concanavalin A. Recombinant IL-6 failed to induce significant amounts of IL-3, and TNF alpha induced only weak IL-3 production. GM-CSF but not M-CSF could lead to the appearance of IL-3 in spleen cell culture supernatants. Removal of macrophages decreased the production of IL-3 induced by LPS and GMF-CSF though did not affect the IL-3 production induced by IL-1. This observation suggests that IL-1 production might be an intermediate event in IL-3 production induced by LPS and GM-CSF through the activation of macrophages. IL-3 was detected in culture supernatants of B-cell-depleted splenocytes indicating that T-cells were the source of IL-3. Surprisingly T-cell-depleted populations could also produce IL-3 upon IL-1 stimulation. Preliminary experiments with an autoreactive CD4- CD8- V beta 8+ clone suggested that these cells might also be involved in the described IL-3 production.     

Large-scale production of endotoxin-free plasmids for transient expression in mammalian cell culture

Transient expression of recombinant proteins in mammalian cell culture in a 100-L scale requires a large quantity of plasmid that is very labour intensive to achieve with shake flask cultures and commercially available plasmid purification kits. In this paper we describe a process for plasmid production in 100-mg scale. The fermentation is carried out in a 4-L fed-batch culture with a minimal medium. The detection of the end of batch and triggering the exponential (0.1 h(-1)) feed profile was unattended and controlled by Multi-fermenter Control System. A restricted specific growth rate in fed-batch culture increased the specific plasmid yield compared to batch cultures with minimal and rich media. This together with high biomass concentration (68-107 g L(-1) wet weight) achieves high volumetric yields of plasmid (95-277 mg L(-1) depending on the construct). The purification process consisted of alkaline lysis, lysate clarification and ultrafiltration, two-phase extraction with Triton X-114 for endotoxin removal, anion-exchange chromatography as a polishing step, ultrafiltration and sterile filtration. Both fermentation and purification processes were used without optimisation for production of four plasmids yielding from 39 to 163 mg of plasmids with endotoxin content of 2.5 EU mg(-1) or less.     

Influence of plasmid origin and promoter strength in fermentations of recombinant yeast

The effects of plasmid promoter strength and origin of replication on cloned gene expression in recombinant Saccharomyces cerevisiae have been studied in batch and continuous culture. The plasmids employed contain the Escherichia coli lacZ gene under the control of yeast promoters regulated by the galactose regulatory circuit. The synthesis of beta-galactosidase was therefore induced by the addition of galactose. The initial induction transients in batch culture were compared for strains containing plasmids with 2mu and ARS1 origins. As expected, cloned gene product synthesis was much lower with the ARS1 plasmid: average beta-galactosidase specific activity was an order of magnitude below that with the 2mu-based plasmid. This was primarily due to the low plasmid stability of 7.5% when the plasmid origin of replication was the ARS1 element. The influence of plasmid promoter strength was studied using the yeast GAL1, GAL10, and hybrid GAL10-CYC1 promoters. The rate of increase in beta-galactosidase specific activity after induction in batch culture was 3-5 times higher with the GAL1 promoter. Growth rate under induced conditions, however, was 15% lower than in the absence of lacZ expression for this promoter system. The influence of plasmid promoter strength on induction behavior and cloned gene expression was also studied in continuous fermentations. Higher beta-galactosidase production and lower biomass concentration and plasmid stability were observed for the strain bearing the plasmid with the stronger GAL1 promoter. Despite the decrease in biomass concentration and plasmid stability, overall productivity in continuous culture using the GAL1 promoter was three times that obtained with the GAL10-CYC1 promoter.     

补料速度对工程菌生长和产物表达的影响研究

通过研究各培养阶段补料速度对温敏启动子控制的rIL-2工程菌E.coliK802(pLY-4)培养密度和rIL-2表达的影响,发现在各培养阶段控制不同的补料速度有利于提高菌密度和rIL-2表达,缩短培养周期。确定了rIL-2工程菌高密度培养方案,三批重复实验,平均菌密度为58OD_(600);菌干重18.0g/L,rIL-2表达水平为42.4％。     

Temperature control of growth and productivity in mutant Chinese hamster ovary cells synthesizing a recombinant protein

The use of a temperature switch to control the growth and productivity of temperature-sensitive (ts) mutants was investigated to extend the productive life span of recombinant Chinese hamster ovary (CHO) cells in batch culture. Bromodeoxyuridine was used at 39 degrees C to select mutagenized CHO-K1 cells, which resulted in the isolation of 31 temperature-sensitive mutants that were growth inhibited at 39 degrees C. Two of these mutants were successfully transfected with the gene for tissue inhibitor of metalloproteinases (TIMP) using glutamine synthetase amplification, and a permanent recombinant cell line established (5G1-B1) that maintains the ts phenotype.Continuous exposure to the nonpermissive temperature (npt) of 39 degrees C led to a rapid decline in cell viability. However, a temperature regime using alternating incubations at 34 degrees C and 39 degrees C arrested the 5G1-B1 cells while retaining a high cell viability for up to 170 h in culture. The specific production rate of the growth-arrested cells was 3-4 times that of control cultures maintained at a constant 34 degrees C over the crucial 72-130-h period of culture, which resulted in a 35% increase in the maximum product yield. Glucose uptake and lactate production both decreased in arrested cells. Flow cytometric analysis indicated that 5G1-B1 cells arrested in the G(1) or G(0) phase of the cell cycle, and no major structural damage was caused to these cells by the alternating temperature regime.These results demonstrate that growth-arrested ts CHO cells have increased productivity compared to growing cultures and maintain viability for longer periods. The system offers the prospect of enhancing the productivity of recombinant mammalian cells grown in simple batch fermentors. (c) 1993 John Wiley & Sons, Inc.     

Effect of phenylacetic acid on the growth and production of penicillin G acylase of recombinant and host strains derived from Escherichia coli W

The industrial production strain Escherichia coli RE3(pKA18) for penicillin G acylase (PGA) bears simultaneously the pga gene on the chromosome as an inducible gene pgaⁱ, (the inductor is phenylacetic acid, PAA) and on the recombinant plasmid pKA18 as a constitutively expressed gene pga^c. Under non-selective conditions, plasmid-less strains (P⁻) appeared in 17th successive batch culture. However, the population was over taken by P⁻ cells already in fourth culture if the medium was supplemented with PAA. The rate of plasmid loss from the culture depends on the PAA concentration and on the expression of pgaⁱ, not on PGA overproduction from pga^c. PAA at inducing concentration has a negative effect on PGA expression and plasmid stability in the high-expression self-cloning system RE3(pKA18) which results in the reduction of: (1) the specific growth rate of a culture and biomass concentration, (2) the synthesis of PGA (e.g. the specific activity of the strain) and (3) the copy number of the recombinant plasmid and promotion of the plasmid loss from the culture. Segregational stability of pKA18 increases in P⁺ persisting clones and in re-transformed P⁻ clones segregated during the selection in the presence of PAA.     

Influence of dilution rate and induction of cloned gene expression in continuous fermentations of recombinant yeast

The effects of growth rate on cloned gene product synthesis in recombinant Saccharomyces cerevisiae have been studied in continuous culture. The plasmid employed contains a yeast GAL10-CYC1 hybrid promoter directing expression of the E. coli lacZ gene. beta-Galactosidase production was therefore controlled by the yeast galactose regulatory circuit, and the induction process and its effects were studied at the various dilution rates. At all dilution rates plasmid stability decreased with induction of lacZ gene expression. In some instances, two induced "steady states" were observed, the first 10-15 residence times after induction and the second after 40-50 residence times. The second induced steady state was characterized by greater biomass concentration and lower beta-galactosidase specific activity relative to the first induced "steady-state." beta-Galactosidase specific activity and biomass concentration increased as dilution rate was reduced, and despite lower flow rate and plasmid stability, overall productivity (activity/L/hr) was substantially higher at low dilution rate. Important factors influencing all of the trends were the glucose and galactose (inducer) concentrations in the vessel and inducer metabolism.     

Overproduction of alkaline polygalacturonate lyase in recombinant Escherichia coli by a two-stage glycerol feeding approach

This work aims to achieve the overproduction of alkaline polygalacturonate lyase (PGL) with recombinant Escherichia coli by a two-stage glycerol feeding approach. First, the PGL coding gene from Bacillus subtilis WSHB04-02 was expressed in E. coli BL21 (DE3) under the strong inducible T7 promoter of the pET20b (+) vector. And then the influence of media composition, induction temperature, and inducer isopropyl β-D-1-thiogalactopyranoside (IPTG) concentration on cell growth and PGL production was investigated. Finally, a two-stage glycerol feeding strategy was proposed and applied in a 3-L fermenter, where cultivation was conducted at a controlled specific growth rate (μset=0.2) during pre-induction phase, followed by a constant glycerol feeding rate of 12 ml h(-1) at post-induction phase. The total PGL yield reached 371.86 U mL(-1), which is the highest PGL production by recombinant E. coli expression system.     

Control of culture environment for improved polyethylenimine-mediated transient production of recombinant monoclonal antibodies by CHO cells

In this study we describe optimization of polyethylenimine (PEI)-mediated transient production of recombinant protein by CHO cells by facile manipulation of a chemically defined culture environment to limit accumulation of nonproductive cell biomass, increase the duration of recombinant protein production from transfected plasmid DNA, and increase cell-specific production. The optimal conditions for transient transfection of suspension-adapted CHO cells using branched, 25 kDa PEI as a gene delivery vehicle were experimentally determined by production of secreted alkaline phosphatase reporter in static cultures and recombinant IgG4 monoclonal antibody (Mab) production in agitated shake flask cultures to be a DNA concentration of 1.25 microg 10(6) cells(-1) mL(-1) at a PEI nitrogen:DNA phosphate ratio of 20:1. These conditions represented the optimal compromise between PEI cytotoxicity and product yield with most efficient recombinant DNA utilization. Separately, both addition of recombinant insulin-like growth factor (LR3-IGF) and a reduction in culture temperature to 32 degrees C were found to increase product titer 2- and 3-fold, respectively. However, mild hypothermia and LR3-IGF acted synergistically to increase product titer 11-fold. Although increased product titer in the presence of LR3-IGF alone was solely a consequence of increased culture duration, a reduction in culture temperature post-transfection increased both the integral of viable cell concentration (IVC) and cell-specific Mab production rate. For cultures maintained at 32 degrees C in the presence of LR3-IGF, IVC and qMab were increased 4- and 2.5-fold, respectively. To further increase product yield from transfected DNA, the duration of transgene expression in cell populations maintained at 32 degrees C in the presence of LR3-IGF was doubled by periodic resuspension of transfected cells in fresh media, leading to a 3-fold increase in accumulated Mab titer from approximately 13 to approximately 39 mg L(-1). Under these conditions, Mab glycosylation at Asn297 remained essentially constant and similar to that of the same Mab produced by stably transfected GS-CHO cells. From these data we suggest that the efficiency of transient production processes (protein output per rDNA input) can be significantly improved using a combination of mild hypothermia and growth factor(s) to yield an extended "activated hypothermic synthesis".     

Kinetic study of instability of recombinant plasmid pPLc23trpAl in E. coli using two-stage continuous culture system

Derepression of the phage lambda p(L) promoter on recombinant plasmid pPLc 23-trpAl caused a rapid increase of plasmid free segregants in the population. In continuous culture, increased production of trpA protein follwing derepression was accompanied by a continuous deceleration of specific growth rate. In the repressed condition, plasmid loss per generation in continuous culture decreased as dilution rate increased from 0.06 to 1.08 h(-1). Over this range, the concentration of plasmid DNA within the cell decreased eightfold corresponding to a decrease in plasmid number from 74 to 32 molecules/cell. The use of a two-stage continuous culture system coupled with a temperature sensitive expression system allows a high trpA productivity from the derepressed plasmid for more than 48 h and also offers a possibility of minimizing the instability problem of high expression recombinants. Such a system also permits the critical study of the effects of fermentation and other regulatory parameters on expression under better controlled conditions than is possible in a batch culture or single-stage continous culture.     

Comparison of three different promoter systems for secretory alpha-amylase production in fed-batch cultures of recombinant Saccharomyces cerevisiae

Cloned gene expression in recombinant Saccharomyces cerevisiae 20B-12 containing three different plasmids was compared in batch and fed-batch cultures. The plasmids pNA3, pNA7, and pNA9 contain the alpha-amylase gene under the control of SUC2, PGK, and GAL7 Promoters, respectively. The synthesis of alpha-amylase was therefore induced by low glucose concentration for the SUC2 and PGK promoters, and by galactose for GAL7 promoter. The specific cell growth rates were similar among cells harboring the three different plasmids; they decreased from 0.35 to 0.38 h(-1) during the cell growth phase to 0.03 to 0.06h(-1) during the production phase. The secretory alpha-amylase activity of cells harboring plasmid pNA7 was 129 U/mL in fed-batch culture, which was 1.4 and 2 times as high as the activities of cells harboring plasmids pNA3 and pNA9, respectively. The secretion ratios (amount of extracellular alpha-amylase activity/amounts of total alpha-amylase activity) of cells harboring plasmids pNA3, pNA7, and pNA9 were 91.4%, 94.5%, and 95.3%, respectively. (c) 1993 Wiley & Sons, Inc.     

A chemostat culture as a tool for the improvement of a recombinant E. coli strain over-producing penicillin G acylase

The recombinant strain RE3(pKA18) of Escherichia coli constitutively overproduces penicillin G acylase (PGA) from plasmid-borne gene pga. The host strain RE3 bears the same pga gene on its chromosome, the expression of which is controlled by the natural mechanism of induction with phenylacetic acid (PA). To evaluate the maximum biosynthetic capacity for PGA, induction of the chromosomal pga by PA was studied in a culture of the recombinant strain. PGA production by batch cultures of RE3(pKA18) and RE3 showed a different response to the addition of PA to the medium: while an addition of PA induces PGA in a culture of strain RE3 as expected, in recombinant cells it lowers the specific activity of PGA and a large amount of PGA is released into the culture medium. To improve the PGA production, the strain RE3(pKA18) was cultured in a carbon-limited chemostat and subjected to selection pressure in a medium supplemented with phenylacetic acid amide (PAA). Phenylacetic acid amide served as a source of nitrogen, an inducer of PGA and a factor exerting positive selection pressure on the maintenance of the recombinant plasmid. After 130 generations of growth in the presence of the inducer, no recombinant strain with constitutive expression of the chromosomal gene pga was detected in the prevailing P(+) subpopulation in the chemostat. Shake-flask experiments with the parent recombinant strain RE3(pKA18), host strain RE3, chemostat evolvant ERE3(epKA18), the cured host ERE3 alone, and its derivative after retransformation with ancestral plasmid ERE3(pKA18) showed that inactivation of the plasmid-borne pga by a frame-shift mutation (plasmid epKA18) occurred in the plasmid-bearing subpopulation accumulated in the chemostat. Marked adaptive changes evolved in the host ERE3 during a 130 generation culture: (1) the specific growth rate of the host increased by 30% in a medium without PA, (2) the copy number of plasmids pKA18 and epKA18 in the host cultured in PA-free medium dropped by about 40%, and (3) the leakage of PGA from the cell in the presence of PA found in strain RE3(pKA18) was not observed in strain ERE3(pKA18). This new recombinant strain with modified traits was constructed by means of retransformation of the evolved host ERE3 with ancestral plasmid pKA18.     

High-level expression of recombinant human soluble thrombomodulin in serum-free medium by CHO-K1 cells

Cultivation of gene-engineered Chinese hamster ovary (CHO-K1) cells that produce recombinant human soluble thrombomodulin (rsTM) was investigated to optimize conditions for high-level expression of the protein in a serum-free medium. For economic protein production, oxygenation of cultures with pure O₂ permitted sufficient cell growth for high rsTM production with only 1 g/l of microcarriers and a low foetal bovine serum concentration. A longer growth phase (over 5 days) with serum was important to establish sufficient growth of this cell line on the microcarriers for subsequent serum-free culture, and to support a long-term production phase (about 2 months). In the production phase, a high glucose concentration (6.15 g/l) in the serum-free medium was very effective for prolonging the harvest cycle interval. Under these conditions, up to 100 mg/l rsTM was expressed in the conditioned medium. The rates of glucose consumption (G) and lactae production (L) were measured periodically and their ratio (L/G ratio) correlated with rsTM productivity. When the average L/G ratio was lower, reflecting a lower lactate production rate due to appropriate oxygenation of the culture, the specific rsTM production rate increased. Thus it may be possible to estimate protein productivity from L/G ratios calculated from the glucose and lactate measurements. Correspondence to: M. Ogata     

Effect of cell growth rate on the performance of a two-stage continuous culture system in a recombinant Escherichia coli fermentation

As part of the process optimization of a two-stage continuous culture system, the effect of growth rate mu(2) (app) on the performance of the second stage (production stage) was studied in a recombinant Escherichia coli K12 (DeltaH1Deltatrp/pPLc23trpA1). Important parameters considered were specific gene expression rate, plasmid content, and plasmid stability, all of which were closely related to the cell growth rate and the production rate of the cloned gene product (trpalpha). When operating conditions were maintained constant (T(1) = 35 degrees C, D(1) = 0.9 h(-1), T(2) = 40 degrees C, and D(2) = 0.7 h(-1)) and mu(2) (app) was varied, plasmid content in the second stage showed its maximum at mu(2) (app) = 0.4 h(-1) and decreased thereafter. Specific gene expression rate linearly increased with increasing mu(2) (app), while plasmid stability decreased. Optimum cell growth rate giving the maximum value in overall productivity was observed at around mu(2) (app) = 0.4 h(-1). The contribution or role of the three parameters, specific gene expression rate, plasmid content, and plasmid stability in exhibiting the maximum productivity at the optimal mu(2) (app) is discussed.