Carbon-limited continuous culture was used to study the relationship between the growth of Aspergillus niger and the production of glucoamylase. The result showed that when the specific growth rate was lower than 0.068 h(-1), the production of glucoamylase was growth-associated, when the specific growth rate was higher than 0.068 h(-1), the production of glucoamylase was not growth-associated. Based on the result of continuous culture, the Monod dynamics model of glucose consumption of A. niger was constructed, Combining Herbert-Pirt equation of glucose and oxygen consumption with Luedeking-Piret equation of enzyme production, the black-box model of Aspergillus niger for enzyme production was established. The exponential fed-batch culture was designed to control the specific growth rate at 0.05 h(-1) by using this model and the highest yield for glucoamylase production by A. niger reached 0.127 g glucoamylase/g glucose. The black-box model constructed in this study successfully described the glucoamylase production by A. niger and the result of the model fitted the measured value well. The black-box model could guide the design and optimization of glucoamylase production by A. niger.
Aspergillus niger ; metabolism ; Batch Cell Culture Techniques ; Carbon ; Culture Media ; Glucan 1,4-alpha-Glucosidase ; biosynthesis ; Glucose ; Industrial Microbiology ; methods ; Oxygen

During the production of ε-poly-L-lysine (ε-PL) in fed-batch fermentation, the decline of ε-PL synthesis often occurs at middle or late phase of the fermentation. To solve the problem, we adopted two strategies, namely pH shift and feeding yeast extract, to improve the productivity of ε-PL. ε-PL productivity in fermentation by pH shift and feeding yeast extract achieved 4.62 g/(L x d) and 5.16 g/(L x d), which were increased by 27.3% and 42.2% compared with the control ε-PL fed-batch fermentation, respectively. Meanwhile, ε-PL production enhanced 36.95 g/L and 41.32 g/L in 192 h with these two strategies, increased by 27.4% and 42.48% compared to the control, respectively. ε-PL production could be improved at middle or late phase of fed-batch fermentation by pH shift or feeding yeast extract.
Batch Cell Culture Techniques ; Fermentation ; Industrial Microbiology ; Nitrogen ; chemistry ; Polylysine ; biosynthesis

To enhance the production of ε-poly-L-lysine (ε-PL) by improving dissolved oxygen level of the fermentation system, different oxygen-vectors were added to broth and n-dodecane was screened as the best oxygen-vector. The best amount of n-dodecane was 0.5% (V/V) and the best time was at start of the fermentation. In a fed-batch fermentation in a 5 L bioreactor, ε-PL concentration reached a maximum of (30.8 ± 0.46) g/L and the dry cell weight obtained was (33.8 ± 0.29) g/L, increasing by 31.6% and 20.7% compared with the control group, respectively. This improvement can be related to 0.5% n-dodecane could maintain dissolved oxygen concentration > 32% of air concentration compared with 23.8% in ε-PL production phase, and the production of a main by-product, poly-L-diaminopropionic acid, fell by 31%. These results indicated that the dissolved oxygen level in the broth was improved by adding n-dodecane, which can inhibit the by-product production and improve the biosynthesis of ε-PL.
Alkanes ; chemistry ; Batch Cell Culture Techniques ; Bioreactors ; Fermentation ; Oxygen ; chemistry ; Polylysine ; biosynthesis

A comparative study of batch and repeated batch process was carried out for astaxanthin fermentation of Phaffia rhodozyma to develop a more economical method for astaxanthin industrial production. In shaking flask fermentation, the change of biomass and astaxanthin production was studied to compare the five-day cycle with four-day cycle of repeated batch culture of P. rhodozyma. Astaxanthin production increased at first and then decreased subsequently in seven cycles, yet the yield of astaxanthin in the next six cycles remains higher than that of the first cycle. Comparing the average production of astaxanthin in the seven cycles, four-day cycle performed even better than five-day cycle. Subsequently, a repeated fed-batch process was used in a 5-1 bioreactor. The experimental data showed that biomass and astaxanthin production of the second batch could reach the level of the first batch, no matter that the carbon source was glucose or hydrolysis sugar of starch. This result showed that this strain had good stability, and thus repeated batch and fed-batch process could be applied in astaxanthin fermentation for economical purpose.
Basidiomycota ; genetics ; metabolism ; Batch Cell Culture Techniques ; methods ; Bioreactors ; microbiology ; Fermentation ; Industrial Microbiology ; methods ; Xanthophylls ; biosynthesis

In recent years, the demand of biologics has increased rapidly. Cell culture process with perfusion mode has become more and more popular due to its high productivity, good quality and high efficiency. In this paper, the unique operation and the details of process optimization for perfusion culture mode are discussed by comparing with traditional batch culture process. Meanwhile, the progress and strategies in the development and optimization of perfusion culture process in recent years are summarized to provide reference for the future development of mammalian cell perfusion culture technology.
Animals ; Batch Cell Culture Techniques ; trends ; Bioreactors ; standards ; CHO Cells ; Cricetulus ; Mammals ; Perfusion

With various diseases ravaging internationally, the demands for recombinant adenoviral vector (Adv) vaccines have increased dramatically. To meet the demand for Adv vaccine, development of a new cell culture process is an effective strategy. Applying hyperosmotic stress in cells before virus infection could increase the yield of Adv in batch culture mode. Emerging perfusion culture can significantly increase the yield of Adv as well. Therefore, combining the hyperosmotic stress process with perfusion culture is expected to improve the yield of Adv at high cell density. In this study, a shake flask combined with a semi-perfusion culture was used as a scaled-down model for bioreactor perfusion culture. Media with osmotic pressure ranging from 300 to 405 mOsm were used to study the effect of hyperosmotic stress on cell growth and Adv production. The results showed that using a perfusion culture process with a hyperosmotic pressure medium (370 mOsm) during the cell growth phase and an isosmotic pressure medium (300 mOsm) during the virus production phase effectively increased the yield of Adv. This might be due to the increased expression of HSP70 protein during the late phases of virus replication. The Adv titer in a bioreactor with such a process reached 3.2×10¹⁰ IFU/mL, three times higher than that of the traditional perfusion culture process. More importantly, this is the first time that a strategy of combining the hyperosmotic stress process with perfusion culture is applied to the production of Adv in HEK 293 cells. It also reveals the reason why the hyperosmotic stress process increased the yield of Adv, which may facilitate the process optimization of for producing other Adv in HEK 293 cells.
Humans ; HEK293 Cells ; Genetic Vectors/genetics* ; Batch Cell Culture Techniques ; Bioreactors ; Perfusion

No abstract available.
Cell Culture Techniques*

Background: In recent years, the rotavirus diarrhea increased significantly in Vietnam, an estimated 50%-70% of children\u2019s hospitalization for diarrhea in 2005. The virus subtype causing disease mainly in Vietnam today was not only G1, G2, G4, like other countries in the world but also the rare strain was G9. Objectives: to isolate G9 rotavirus strains on MA104 cell culture; to selecting G9 rotavirus which developing well on MA104 cells. Subjectives and Method: an experimental research in the laboratory. 20 stool samples derived from 20 children with acute diarrhea caused by rotavirus G9P8 (using RT-PCR method). The samples were processed according to standards of the Centers for disease control and prevention (CDC), Atlanta, USA. Results: eight out of 20 human rotavirus strains G9P8 were positive on Ma104 cell suspension after 3 consecutive cultures (OD indexes of these sample were over 0.100,sample No 2 had the highest OD (1.347)). Sample No 2 was chosen for the first time cloning (25 clones, 17/25 with OD>0.100). And clone No 16 was selected for the second purifying (25 clones, 24/25 with OD>0.100). Ten out of 25 clones in the second time were adapted on monolayer Ma104 cell culture and only clone No 14 and No 18 with highest OD (2.648 and 2.644, respectively) will be used for next studies. Conclusions: cloning method was a basic method for adapting rotavirus clone on cell cultured. Rate of G9P8 rotavirus strain which isolated on Ma104 cells\ufffd?suspension was relatively high. Among the second time clones, 2/10 samples adapted on Ma104 cells with high OD.
Cell Culture Techniques ; Rotavirus ;

Using human rotavirus strain VNHR203-027 to inoculate and passage 11 consecutive times on Africa green monkey kidney (Vero) cells with inoculum medium at different trypsine concentrations, their results are VNHR203-027 have been adapting and growing on Vero cells with trypsin concentration of 30g/ml. Using human rotavirus strain VNHR203-037 to multiply on 4 lots of primary monkey kidney cells and 6 lots of Vero cells gave very high titre on both kinds of cell, the average titre on primary monkey kidney cells was 8,47 Iog10 FFU/ml and of Vero cells was 8.65 Iog10 FFU/ml. No significant difference in potency is found among Vero cells and primary monkey kidney cells (T=10-2 < t=1.86 with =0.05).
Rotavirus ; Cell Culture Techniques

No abstract available.
Cell Culture Techniques*