西洋参悬浮细胞发酵工艺研究

探讨了西洋参悬浮细胞分步培养与稀土、D-半乳糖和甘露醇等诱导子对悬浮细胞生长及皂甙产量的影响。发现继代4d后换液一次再继续培养获得的培养物,在皂甙产率和糖利用率等方面优于连续培养;D-半乳糖作为诱导子,对悬浮培养的西洋参细胞生长、皂甙产率及皂甙的分泌等方面都有非常明显的促进作用。     

Enhanced taxol production and release in Taxus chinensis cell suspension cultures with selected organic solvents and sucrose feeding

Suspension culture of Taxus chinensis cells was carried out in aqueous-organic two-phase systems for the production and in situ solvent extraction of taxol (paclitaxel). Three organic solvents, hexadecane, decanol, and dibutylphthalate, were tested at 5-20% (v/v) in the culture liquid. All of these solvents stimulated taxol release and the yield per cell, though decanol and higher concentrations of the other two solvents depressed biomass growth significantly. Ten percent dibutylphthalate was the optimal solvent for improving taxol production and release with minimal cell growth inhibition. The time of solvent addition to the culture also affected taxol production, with the addition during the late-log growth phase being most favorable. By feeding sucrose to the culture near the stationary growth phase, the cell growth and taxol production period was extended from 27 to 42 days. The combining of the two-phase culture and sucrose feeding increased the taxol yield by about 6-fold compared with the single-phase batch culture, to 36.0 +/- 3.5 mg/L, with up to 63% taxol released. This study shows that in situ solvent extraction combined with nutrient feeding is an effective process strategy for production and recovery of secondary metabolites in plant cell suspension culture.     

Antibody production and growth of mouse hybridoma cells in Nutridoma media supplements

Traditionally, cell culturists have relied upon the addition of serum to culture medium for the growth and maintenance of cell lines. However, many aspects of the use of serum in tissue culture are problematic. Cell culture supplements that circumvent the need for serum are readily available and provide a consistent protein composition. This defined environment allows the antibody to be more easily purified from culture supernatants. Nutridoma media supplements were formulated to support the growth of lymphoblastoid cells in a defined culture environment. In this study, Nutridoma media supplements were tested in parallel with serum-containing cultures to determine if Nutridoma supplemented medium is effective in supporting hybridoma cell growth and antibody production in three hybridoma cell lines. Data, based on cell growth and antibody production, show the importance of basal media selection when serum is replaced with Nutridoma media supplements. SDS-PAGE results show that cell supernatants from Nutridoma supplemented cultures contain very few contaminating proteins.     

Intensification of β-poly(l-malic acid) production by Aureobasidium pullulans ipe-1 in the late exponential growth phase

β-Poly(malic acid) (PMLA) has attracted industrial interest because this polyester can be used as a prodrug or for drug delivery systems. In PMLA production by Aureobasidium pullulans ipe-1, it was found that PLMA production was associated with cell growth in the early exponential growth phase and dissociated from cell growth in the late exponential growth phase. To enhance PMLA production in the late phase, different fermentation modes and strategies for controlling culture redox potential (CRP) were studied. The results showed that high concentrations of produced PMLA (above 40 g/l) not only inhibited PMLA production, but also was detrimental to cell growth. Moreover, when CRP increased from 57 to 100 mV in the late exponential growth phase, the lack of reducing power in the broth also decreased PMLA productivity. PMLA productivity could be enhanced by repeated-batch culture to maintain cell growth in the exponential growth phase, or by cell-recycle culture with membrane to remove the produced PMLA, or by maintaining CRP below 70 mV no matter which kind of fermentation mode was adopted. Repeated-batch culture afforded a high PMLA concentration (up to 63.2 g/l) with a productivity of 1.15 g l(-1) h(-1). Cell-recycle culture also confirmed that PMLA production by the strain ipe-1 was associated with cell growth.     

Enhanced hyaluronic acid production by a two-stage culture strategy based on the modeling of batch and fed-batch cultivation of Streptococcus zooepidemicus

This study aimed to enhance hyaluronic acid (HA) production by a two-stage culture strategy based on the modeling of batch and fed-batch culture of Streptococcus zooepidemicus. Batch culture had higher specific HA synthesis rate while fed-batch culture had higher specific cell growth rate. The lower specific HA synthesis rate in fed-batch culture resulted from the competition of cell growth for the common precursors at a low substrate concentration. Based on the modeling of batch and fed-batch culture of S. zooepidemicus, a two-stage culture strategy was proposed to enhance HA production. S. zooepidemicus were cultured in a fed-batch mode with sucrose concentration maintained at 1.0+/-0.2g/L during 0-8h and then batch culture was performed during 8-20h with an initial sucrose concentration of 15g/L. With the proposed two-stage culture strategy, HA production was increased to 6.6g/L compared with 5.0g/L in batch culture with the same total sucrose. The enhanced HA production by the proposed two-stage culture strategy resulted from the decreased inhibition of cell growth and the increased transformation rate of sucrose to HA.     

On-line determination of optimum time for switching from growth phase to production phase in tissue plasminogen activator production in a microcarrier cell culture

To maximize the productivity of tissue plasminogen activator (TPA) by a mammalian cell culture, on-line determination of the optimum time to switch from the cell growth phase to the TPA production phase was investigated. By measuring the TPA production activity of the cells during the cell growth culture, it was shown that this optimum time was not necessarily the same as the time at which the cell concentration was maximized, and that the optimum time varied with growth culture batch. The TPA production activity of the cells during the growth culture could be estimated by on-line regression analysis using physiological data of the current state, including the oxygen consumption rate (Io₂) and cell concentration, as well as data from past batches. Applying this on-line estimation, the optimum switching time was determined to be the time at which the TPA production activity of the cells in the growth culture became highest, or higher than a certain value according to determined criteria.     

微囊化重组CHO细胞制备和培养条件的优化

微囊化重组基因细胞移植治疗肿瘤是一种新兴的肿瘤基因治疗方法,然而由于目前微囊化细胞规模化制备和培养技术还不成熟,阻碍了其在临床治疗中的推广与应用。以重组CHO细胞为模型,考察了不同的微囊制备和培养条件对微囊化细胞生长和内皮抑素表达的影响。实验表明,种子细胞所处的生长阶段和细胞接种密度对微囊化细胞生长和内皮抑素表达的影响较大,对数生长期的细胞进行包囊并且细胞接种密度为1×106~2×106cells/mL微囊时微囊内细胞生长良好、内皮抑素表达量高。微囊制备时间对细胞活性和内皮抑素表达也有较大的影响,制备时间延长对细胞的损伤增大,因此制备时间应控制在5h以内。生物微胶囊在制备过程中会造成细胞损伤,而体外培养是恢复细胞活性的良好方法,在培养过程中微囊接种量为5%时对细胞生长和内皮抑素表达有利。     

Metabolic profiling of Chinese hamster ovary cell cultures at different working volumes and agitation speeds using spin tube reactors

Culture systems based on spin tube reactors have been consolidated in the development of manufacturing processes based on Chinese hamster ovary (CHO) cells. Despite their widespread use, there is little information about the consequences of varying operational setting parameters on the culture performance of recombinant CHO cell lines. Here, we investigated the effect of varying working volumes and agitation speeds on cell growth, protein production, and cell metabolism of two clonally derived CHO cell lines (expressing an IgG1 and a “difficult-to-express” fusion protein). Interestingly, low culture volumes increased recombinant protein production and decreased cell growth, while high culture volumes had the opposite effect. Altering agitation speeds exacerbated or moderated the differences observed due to culture volume changes. Combining low agitation rates with high culture volumes suppressed growth and recombinant protein production in CHO cells. Meanwhile, high agitation rates narrowed the differences in culture performance between low and high working volumes. These differences were also reflected in cell metabolism, where low culture volumes enhanced oxidative metabolism (linked to a productive phenotype) and high culture volume generated a metabolic profile that was predominately glycolytic (linked to a proliferative phenotype). Our findings indicate that the culture volume influence on metabolism modulates the balance between cell growth and protein production, a key feature that may be useful to adjust CHO cells toward a more productive phenotype.     

Cellulase production by a solid state culture system

Production of cellulase using solid culture systems of Trichoderma reesei QM9414 and Sporotrichum cellulophilum on wheat bran was studied. By using moisture-controlled solid culture equipment, the effect of water content of wheat bran on cell growth and cellulase production was investigated. Cellular biomass grown on solid substrate was estimated by measuring oxygen consumption rate and glucosamine content of the cells. These parameters were shown to have a good linear correlation with the specific growth rate. This reliable method of estimating the cell growth rate enabled us to simulate the enzyme production in a solid culture system by means of multiple linear regression analysis which takes into account of the water content, cell mass, and the oxygen consumption rate as variables. The cell growth and cellulase production were maximized at different water content of the medium. A high water content, 57% for T. reesei and 70% for S. cellulophilum, favored mycelial growth, while the maximum cellulase activity was obtained at a lower water content such as 50% for both fungi. It was observed that cellulase production by T. reesei depended on the culture conditions that support the optimal growth rate for the maximum enzyme production.     

A kinetic analysis of hybridoma growth and metabolism in continuous suspension culture on serum-free medium

The steady-state metabolic parameters for a murine hybridoma cell line have been determined in continuous suspension culture over a wide range of dilution rates. Long-term adaption occurred over seven months in culture and resulted in lower glucose consumption rates, reduced lactate production, higher cell viability, and, consequently, growth rates more nearly matching the dilution rate. Antibody production rates decreased over the first two months and then remained stable for at least 75 days. The antibody production rate was not found to be growth associated. Steadystate amino acid uptake rates are presented for a wide range of growth rates.     

Comparison of the optimal culture conditions for cell growth and tissue plasminogen activator production by human embryo lung cells on microcarriers

Optimization of culture conditions such as the dissolved O₂ (DO) concentration, temperature and pH was attempted regarding both cell growth and the production of tissue plasminogen activator (TPA) in a microcarrier cell culture of human embryo lung cells. The growth rate was suppressed at a DO concentration below 30% saturation. From the pH range 7.2–7.6, both the specific growth rate and maximal cell concentration decreased. At a lower temperature than 37°C, although both the specific growth rate and the maximal cell concentration decreased, the cell concentration was maintained for a longer time during the production period, high TPA productivity being maintained. As the optimal conditions for culture growth, a DO concentration of 30% saturation or over, temperature of 37°C and pH of 7.4 are recommended. However, for TPA production after cell culture growth, the DO concentration should be in the range 20–30% O₂ saturation, and the temperature and pH should be lowered to 33°C and 6.8, respectively.     

Expression of a human anti-rabies virus monoclonal antibody in tobacco cell culture

A Nicotiana tabacum cv. Xanthi cell culture was initiated from a transgenic plant expressing a human anti-rabies virus monoclonal antibody. Within 3 months, plant cell suspension cultures were established and recombinant protein expression was examined. The antibody was stably produced during culture growth. ELISA, protein G purification, Western blotting, and neutralization assay confirmed that the antibody was fully processed, with association of light and heavy-chains, and that it was able to bind and neutralize rabies virus. Quantification of antibody production in plant cell suspension culture revealed 30 microg/g of cell dry weight for the highest-producing culture (0.5 mg/L), 3 times higher than from the original transgenic plant. The same production level was observed 3 months after cell culture initiation. Plant cell suspension cultures were successfully grown in a new disposable plastic bioreactor, with a growth rate and production level similar to that of cultures in Erlenmeyer flasks.     

Optimization of Vi capsular polysaccharide production during growth of Salmonella enterica serotype Typhi Ty2 in a bioreactor

Vi capsular polysaccharide is synthesized during growth of Salmonella typhi Ty2 and is spontaneously released from the bacterial cells into the culture medium during culture. Vi production was dependent on cell growth and the greater the cell mass the greater the production of Vi. Using fed batch culture to optimize bacterial growth resulted is an increase in cell mass and consequently Vi production. The yield of Vi obtained in fed batch culture was 415 mg l⁻¹, which was over three times that, obtained in batch culture. A proportion of the Vi remained cell associated in the form of a capsule and at least part of this was released from the bacterial surface by sonication. The size of the Vi polysaccharide produced was consistently high and did not change during the different phases of bacterial growth. The synthesis of Vi was also dependent upon the media components and the fermentation conditions. The presence of high concentrations of glucose at the beginning of growth inhibited the production of Vi, particularly during the stationary phase. At a concentration of 400 mM sodium phosphate the synthesis of Vi was strongly inhibited.     

Production of a secreted glycoprotein from an inducible promoter system in a perfusion bioreactor

The primary advantage of an inducible promoter expression system is that production of the recombinant protein can be biochemically controlled, allowing for the separation of unique growth and production phases of the culture. During the growth phase, the culture is rapidly grown to high cell density prior to induction without the extra metabolic burden of exogenous protein production, thus minimizing the nonproductive period of the culture. Induction of the culture at high cell density ensures that the volumetric production will be maximized. In this work, we have demonstrated the feasibility of overexpressing a reporter glycoprotein from the inducible MMTV promoter in recombinant Chinese hamster ovary (CHO) cells cultured in a high cell density perfusion bioreactor system. Retention of suspension-adapted CHO cells was achieved by inclined sedimentation. To maximize volumetric production of the culture, we have demonstrated that high cell density must be achieved prior to induction. This operating scheme resulted in a 10-fold increase in volumetric titer over the low density induction culture, corresponding directly to a 10-fold increase in viable cell density during the highly productive period of the culture. The amount of glycoprotein produced in this high cell density induction culture during 26 days was 84-fold greater than that produced in a week long batch bioreactor. Long-term perfusion cultures of the recombinant cell line showed a production instability, a phenomenon that is currently being investigated.     

单克隆抗体Mab-A生产细胞Sp2/0缩小模型培养优化研究

Sp2/0是一种生产单克隆抗体的常用细胞株。本研究首先在批次培养模式中对适合Sp2/0细胞生长的5种基础培养基、摇床转速、培养温度、二氧化碳浓度、微量元素和GlutaMAX ^TM替换谷氨酰胺等影响因素进行了筛选研究。结果显示Sp2/0细胞在批次培养中细胞密度最高值达到13.12×10 ⁶ cells/ml,培养时间为7天。除培养温度会导致不同的细胞生长密度和活率、进而影响培养时间外,其它因素不能导致明显的细胞生长差异。随后在流加培养模式下就14种补料组合进行了筛选,Sp2/0在流加培养模式下细胞的峰值密度可达20~30×10 ⁶ cells/ml,培养时间9天,单克隆抗体Mab-A日产量最高达到27.20mg/L。最后应用批次-反复流加培养模式培养Sp2/0细胞,该条件下峰值细胞数为50.42×10 ⁶ cells/ml,培养时间14天,每天单抗产量(141.10mg/L)是流加培养的5.19倍。这些研究结果为Sp2/0细胞规模化生产单克隆抗体奠定了一定基础。     

A comparison of oxygenation methods fro high-density perfusion culture of animal cells

A perfusion culture system was developed to investigate the oxygenation of high-density hybridoma cell cultures. The culture system was composed of a stirred-tank bioreactor and an external microfiltration hollow fiber cartridge for medium perfusion. Cell growth and antibody production were examined with large bubble ( approximately 5 mm in diameter), micron-sized bubble ( approximately 80 mum in diameter), and silicone tubing oxygenation techniques. Comparable cell growth and monoclonal antibody (MAb) production were found for both the micron-sized and large oxygenation methods, provided that large bubbles were enriched with pure oxygen. Relatively low cell growth and MAb production were attained with the bubble-free silicone tubing oxygenation. It is concluded that direct bubble oxygenation can be applied successfully in high-density animal cell cultures, provided that the culture medium is supplemented with Pluronic F-68. The accumulation of ammonia in the culture medium rather than oxygen limitation was found to be one of the possible problems that eventually inhibited cell growth. This and the fouling of the filtration cartridge during long-term cultivation were found to be more problematic than simple bubble oxygenation of high-density cell culture. The micron-sized bubble oxygenation method is highly recommended for high-density animal cell cultures, provided that Pluronic F-68 is supplemented into the culture medium. (c) 1993 John Wiley & Sons, Inc.     

Enhancement of paclitaxel production by temperature shift in suspension culture of Taxus chinensis

Effect of temperature shift during culture period on cell growth and paclitaxel was investigated to optimize paclitaxel production in suspension culture of Taxus chinensis. Cell growth showed the optimum at 24 degrees C while paclitaxel synthesis showed the maximum at 29 degrees C. To minimize the inhibitory effect of higher temperature on cell growth, temperature was shifted after a certain period of culture time at 24 degrees C. Paclitaxel synthesis in plant cell culture increased dramatically during day 14 to day 21 regardless of treatment, reaching the maximum production of 137.5 mg paclitaxel/L. When the temperature was maintained at 29 degrees C after day 21, the specific productivity of paclitaxel was sustained for prolonged period of 42 days. The possible relationship between temperature and paclitaxel synthetic pathway was also suggested.     

Serum-free suspension cultivation of PER.C6(R) cells and recombinant adenovirus production under different pH conditions

PER.C6(R) cell growth, metabolism, and adenovirus production were studied in head-to-head comparisons in stirred bioreactors under different pH conditions. Cell growth rate was found to be similar in the pH range of 7.1-7.6, while a long lag phase and a slower growth rate were observed at pH 6.8. The specific consumption rates of glucose and glutamine decreased rapidly over time during batch cell growth, as did the specific lactate and ammonium production rates. Cell metabolism in both infected and uninfected cultures was very sensitive to culture pH, resulting in dramatic differences in glucose/glutamine consumption and lactate/ammonium production under different pH conditions. It appeared that glucose metabolism was suppressed at low pH but the efficiency of energy production from glucose was enhanced. Adenovirus infection resulted in profound changes in cell growth and metabolism. Cell growth was largely arrested under all pH conditions, while glucose consumption and lactate production were elevated post virus infection. Virus infection induced a reduction in glutamine consumption at low pH but an increase at high pH. The optimal pH for adenovirus production was found to be 7.3 under the experimental conditions used in the study. Deviations from this optimum resulted in significant reductions of virus productivity. The results indicate that culture pH is a very critical process parameter in PER.C6(R) cell culture and adenovirus production.     

Evaluation of growth hormone production from GH1 cells in vitro: Effect of culture media and time in culture

Summary Growth hormone production by a rat pituitary tumor cell line (GH1) was measured during lag, exponential, and plateau phases of growth in different culture media. Growth hormone secretion was low during lag and early exponential phase; it increased late in the exponential phase and continued to increase during the plateau phase. This biphasic pattern of growth hormone production was observed in all media and sera utilized. Both the doubling time and growth hormone production were influenced by the choice of media and sera. In addition, the length of time in culture affected the growth fraction with passage level 40 GH1 cells having a 79% growth fraction, whereas the growth fraction of passage level 100 cells was 95%. Using the population doubling time as a criterion for a choice of medium, F-10 medium supplemented with 20% fetal bovine serum consistently yielded the most rapid doubling time (32 hr), whereas Dulbecco's MEM supplemented with 15% horse serum and 2.5% fetal bovine serum yielded the greatest plateau cell density. Growth hormone secretion and the population doubling times were directly related to culture conditions including length of time in culture, choice of tissue culture media, choice of sera, and the phase of cell growth (lag, exponential or plateau).     

Improved paclitaxel and baccatin III production in suspension cultures of Taxus media

A cell suspension culture of Taxus media was established from a stable callus line of this species. The growth rate and production of paclitaxel and baccatin III of this cell suspension were significantly increased during the shake flask culture in its respective optimum media for cell growth and product formation, which were selected after assaying 24 different culture media. The highest yields of paclitaxel (2.09 mg L(-1)) and baccatin III (2.56 mg L(-1)) in the production medium rose (factors of 7.0 and 3.0, respectively) in the presence of methyljasmonate (220 microg g(-1) FW). When the elicitor was added together with mevalonate (0.38 mM) and N-benzoylglycine (0.2 mM), the increase in the yields of paclitaxel and baccatin III was even higher (factors of 8.3 and 4.0, respectively). Thereafter, a two-stage culture for cell suspension was carried out using a 5-l stirred bioreactor running for 36 days, the first stage being in the cell growth medium until cells entered their stationary growth phase (12 days) and the second stage being in the production medium supplemented with the elicitor and two putative precursors in the concentrations indicated above. Under these conditions, 21.12 mg L(-1) of paclitaxel and 56.03 mg L(-1) of baccatin III were obtained after 8 days of culture in the production medium.