• KSBB Journal
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• v.11 no.5
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• pp.600-605
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• 1996

Optimum inoculum concentration for the production of taxol was determined in Taxus brevifolia and Taxus cuspidata cell suspension cultures. By fresh weight, 2.5, 5, 7.5, 10 g/flask of cells were inoculated and cell growth as well as taxol production were examined. In both Taxus cell cultures, the higher the inoculum concentration, the shorter the length of the lag period. The optimum inoculum concentration for taxol production was found to be 5 g/flask. To produce taxol in large quantity, utilization of proper medium was thought to be important. In case of using a production medium with 6% sucrose, taxol production was noticed. Its level reached the maximum at the 9th day of culture and decreased afterwards. However, taxol was not detected from cell cultures in growth medium.

• KSBB Journal
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• v.24 no.1
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• pp.70-74
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• 2009

For continuous culture of cellulolytic enzymes production to saccharify food wastes, refill concentration of Mandel's medium for continuous culture was 0.5%, and refill intervals were determined to 12 hours by analysis of COD and total nitrogen concentration after 4-days batch culture in flask level. As a result, amylase and FPase productivities were 3.5 and 1.0 U/L.hr, respectively. In 10 L bioreactor, the batch culture mode was compared with fed-batch, fill-and-draw for continuous production of cellulolytic enzyme. Enzyme productivities were most high at batch culture and followed by fed-batch culture. Amylase and FPase activities were 42.3 and 5.6 U/L.hr at batch culture, and 23.0, 2.8 U/L.hr at fed-batch culture, respectively. As a result, in continuous cultivation of cellulolytic enzymes by T. inhamatum KSJ1, the mode of fed-batch was most effective in 10 L bioreactor.

• 한국생물공학회:학술대회논문집
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• 2001.11a
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• pp.758-761
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• 2001

In this study, the nar promoter of E. coli was characterized to see whether the nar promoter cloned onto pBBR122 can be used as an expression promoter of gram negative microbes. For this purpose, a plasmid with lacZ gene expressing ${\beta}-galactosidase$ instead of the structural genes of nar operon in a gram negative host strain(Agrobacterium.tumefaciens) was used to simplify an assay of induction of the nar promoter. The following effects were investigated to find optimal conditions: methods of inducing the nar promoter, optimal nitrate concentration, maximally inducing the nar promoter, the amount of expressed ${\beta}-galactosidase$ and induction ratio(specific ${\beta}-galactosidase$ activity after maximal induction/specific ${\beta}-galactosidase$ activity before induction). The following results were obtained from the experiments: the growth of Agrobacterium with E.coli nar promoter was not much affected by nitrate concentration in the shake-flask; induction of nar promoter was optimal when Agrobacterium was grown in the presence of 1% nitrate ion at the beginning of culture and when overnight culture was completely grown in the shake-flask before being transferred to other shake-flask; the amount of ${\beta}-galactosidase$ per cell and per medium volume was maximal when Agrobacterium was grown under aerobic condition to $OD_{600}$ of 1.7; then the nar promoter was induced under microaerobic and anaerobic condition made by lowering dissolved oxygen level(DO). After 2-3h of induction in the YEP medium selected as a main culture medium, the specific ${\beta}-galactosidase$ activity became about 17,000 Miller units in the fermentor cluture.

• Biotechnology and Bioprocess Engineering:BBE
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• v.11 no.1
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• pp.43-47
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• 2006

Ginseng (Panax ginseng CA. Meyer) hairy root cultures, which are established via the infection of ginseng root discs with Rhizobium rhizogenes, have been used to construct profiles of both biomass growth and nutrient consumption in flask cultures. In a 250 mL shake flask culture, the maximum biomass was observed on the 59th day of the culture period, at 216.8 g (fresh wt) per liter or 11.4 g (dry wt) per liter. The hairy roots were determined to have a growth rate of 0.355 g-DW/g cells/day during the exponential growth phase and a maximum specific growth rate on day 7. Total ginseng saponin and phenolic compound contents were noted to have increased within the latter portion of the culture period. Linear correlations between increases in biomass weight and nutrient uptake were used to imply the conductivity yield $2.60g-DW/(L{\cdot}mS)$ and carbon yield 0.45 g-DW/(g sugar) in the 250 mL flask cultures. The biomass yield when two different nitrogen sources were used (ammonia and nitrate) was shown to remain approximately constant. at $0.47g-DW/(L{\cdot}mM\;NH_4$) and $0.33g-DW/(L{\cdot}mM\;NO_3$); it remained at these levels for 16 days with the ammonia. and for 24 days with the nitrate. The biomass yield when a phosphate source was used was also shown to remain approximately constant for 9 days, at $3.17g-DW/(L{\cdot}mM\;PO_4$), with an $R^2$ of 0.99.

• Journal of Life Science
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• v.18 no.7
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• pp.980-985
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• 2008

This study was carried out to develope an alcoholic drink by fermentation of onion extract using Saccharomyces cerevisiae. The optimal conditions for ethanol production were obtained by standing culture at $25^{\circ}C$ for 5 days with 5% inoculum volume. At the results by flask culture, the growth curve of used S. cerevisiae reached to the stantionary phase at 48 hr and the death phase at 90 hr, whereas ethanol production reached maximum at 114 hr. Under the above conditions, a large scale production was carried out. A standing culture in 5 l fermenter showed the similar results to its flask culture, but progressed 24 hr rapidly more than that of the flask culture. A fed-batch culture was performed by addition of the onionic medium supplemented with 10% (v/v) sucrose after 72 hr from the fermenting start. The fed-batch culture could prevent S. cerevisiae from entering into the death phase and maintain constant level of alcohol production. A continuous culture was able to carry out by adding per every 24 hr the onionic medium supplemented with 10% (v/v) sucrose after 72 hr from the fermenting start. Although S. cerevisiae used showed a little decreased growth, alcohol production maintained roughly the constant level at the maximum yield. To enhance the quality of this alcoholic drink, $2-O-{\alpha}-D-glucopyranosyl$ L-ascorbic acid (AA-2G) was supplemented into the onion extract of the substrate for fermentation. As resulted at this study, this alcoholic drink containing AA-2G should be used as a functional fermented alcohol drink strengthened with vitamin C.

• KSBB Journal
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• v.13 no.1
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• pp.83-89
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• 1998

Using a cellulose macroporous microcarrier, HeLa cells were cultivated in 100mL spinner flask(Bellco Co., USA) and confluent cell laden microcarriers were subcultured by bead-to-bead cell transfer method. In macroporous mcirocarrier-HeLa system viable suspended cells played an important role in bead-to-bead cell transfer and that could be increased by use of RPMI-1640, a calcium-ion-reduced-media and high speed agitation. Successful bead-to-bead cell transfers were performed continuously three time in spinner flask. We applied this technique to produce recombinant Vaccinia virus which express $\beta$-galactosidase. Recombinant protein yield of bead-to-bead transferred culture was comparable to conventional microcarrier cultures that were inoculated by cells detached from T-flask. Although trypsinization is a useful method for subculturing microcarriers in some cases, that process adds quality control problem and handling steps to large scale cell production. There fore, bead-to-bead cell transfer technique offers another convenient and efficient scale-up method for continuous microcarrier cultures.

• Journal of Plant Biotechnology
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• v.35 no.2
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• pp.155-161
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• 2008

This paper reported the establishment of mass production system of adventitious roots of Codonopsis lanceolata through shake flask and bioreactor culture. Induction of adventitious roots was started from the explants of leaf, stem and root on 1/2 strength Murashing and Skoog (MS) solid medium. Stem segments were the best explants for induction of adventitious roots compared to leaf and root segments. Among the different auxins tested (NAA, IBA and IAA), number of adventitious root per explant was highest on solid medium with 1.0 mg/L IBA, and produced $9.9{\pm}1.2$ roots per explant. However, growth of adventitious roots was fast in the presence of IBA at low concentration (0.1 mg/L). In shake flask culture, maximum production of adventitious roots (fresh weight) was obtained in half-strength MS medium compared to full-strength and one-third MS medium. When the adventitious roots produced in shake-flask culture were transferred to 5 L air-lift bioreactor, 16 times of fresh weight increase was gained after one month of culture. These results indicate that this protocol for the production of C. lanceolata adventitious roots can be applied to large scale culture for practical application.

• Journal of Biosystems Engineering
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• v.24 no.1
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• pp.9-18
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• 1999

This study was performed to investigate the optimum microalgal culture conditions using flask culture and to find the feasibility of using the flue gas of the rice husk incinerator for cultivating the microalgae. The optimum initial pH of media was 4.5 for the microalgae culture, and the intermittently illuminated culture was more effective than the continuous illuminated culture. Thus, the balance between photosynthesis and formative metabolism must be considered thoroughly to cultivate microalgal cells. The optimum CO2 concentrations were in the range of 7 to 10%, and the optimum temperature was about 35$^{\circ}C$ in both the daytime and the nighttime for the culture. When flue gas of the rice husk incinerator was applied to the microalgae culture using stirred photobioreactor, the dry cell weight was 0.026 g dry biomass/hr$.$l. The results obtained in experiments indicated that the flue gas was effective for microalgae culture without any limitations.

• KSBB Journal
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• v.10 no.1
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• pp.78-88
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• 1995

The encapsulatpd A. niger grew up inside the capsule and mycelia penetrated through the pore of the capsule membrane. The mycelia on the capsule wall became loose when the carbon source and oxygen were deficient in the medium. On the contrary, the production rate increased and mycelia made a lump tightly when the carbon source and oxygen were sufficient. Namely, number of proper capsule of unit volume in the medium was existed. The phenomenon which was swelled of capsule membrane in cultivation could prevented by adding CaCl2 into the medium. According to the time adding CaCl2 into the medium, the production rate of citric acid was influenced. In case of adding CaCl2 into the medium at 7th day cultivation, the production yield of citric acid was increased about 40 percent higher than that of adding CaCl2 initially. The production yield of citric acid using encapsulated A. niger of flask culture was influenced with oxygen supply. The production yield of citric acid ($\Delta$p/$\Delta$s) of the flask culture was increased 3.88 time by using T-flask instead of parafilm sealed flask. Therefore, the productivity and consumption rate concerning production which was taken carbon source were increased when oxygen supply was sufficient. The production of citric acid using encapsulated A. niger was increased average 30 percent higher than that of bead in between 6th and 13th day cultivation.

• Journal of Microbiology and Biotechnology
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• v.12 no.4
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• pp.617-621
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• 2002

In order to optimize the carrot hairy root culture for SOD production, a fed-batch culture of hairy roots was performed in a bioreactor. Maximum SOD activity was obtained when the hairy roots were transferred to the MS medium containing 110 g/1 concentration of sucrose. By controlling the sucrose concentration (70 g/1 sucrose for growth and 110 g/1 sucrose far production, respectively) In a two-stage fed-batch culture, 29 g/1 of the hairy roots was obtained based on the final dry mass. The volumetrically determined SOD activity and productivity in the fed-batch culture were about 6 times higher than those from the flask culture containing sucrose at 30 g/1 concentration.