• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 추계학술발표대회 및 bio-venture fair
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• pp.676-679
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• 2000

• Journal of Microbiology and Biotechnology
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• 제1권2호
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• pp.126-129
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• 1991

In order to produce ${\gamma}-linolenic$ acid by Mucor sp. KCTC 8405P. the fungus was cultivated in fed-batch culture with two phases. i.e., growth in yeast-like form and induction to hyphal growth by pH shift of the culture medium during cultivation. The synchronous growth of the fungus into the appropriate sizes was important for the high density cell culture of this dimorphic fungus. Dissolved oxygen concentration in the medium did not affect degree of unsaturation of fatty acids and ${\gamma}-linolenic$ acid content. Under the culture conditions applied in this experiment. the fungus was found to produce 100 g/l dry mycelia containing 40% of the lipids, where ${\gamma}-linolenic$ acid comprised about 9% of the total extractable fatty acids.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2001년도 추계학술발표대회
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• pp.845-848
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• 2001

For understanding physiology and metabolism under various culture conditions, combined analysis of transcriptome and proteome is attractable way. We have manufactured DNA microarray containing 2,850 genes including all functionally known and putative ones. In this study, we report analysis of transcriptome and proteome during the high cell density culture of E. coli by using DNA microarray and 2-DE. Fed-batch fermentation of E. coli was carried out by exponential feeding of nutrients until the maximum cell density reached 74 g dry cell weight/L (g DCW/L). Changes in transcriptome and proteome during the HCDC are analyzed qualitatively and quantitatively to provide their physiological and metabolic meanings.

• Journal of Microbiology and Biotechnology
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• 제19권12호
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• pp.1603-1611
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• 2009

High-cell-density cultivation of yeast was investigated using the agricultural waste products corn steep liquor (CSL) and molasses. The Saccharomyces cerevisiae KV-25 cell mass was significantly dependent on the ratio between C and N sources. The concentrations of molasses and CSL in the culture medium were statistically optimized at 10.25% (v/v) and 16.87% (v/v), respectively, by response surface methodology (RSM). Batch culture in a 5-l stirred tank reactor using the optimized medium resulted in a cell mass production of 36.5 g/l. In the fed-batch culture, the feed phase was preceded by a batch phase using the optimized medium, and a very high dried-cell-mass yield of 187.63 g/l was successfully attained by feeding a mixture of 20% (v/v) molasses and 80% (v/v) CSL at a rate of 22 ml/h. In this system, the production of cell mass depended mainly on the agitation speed, the composition of the feed medium, and the glucose level in the medium, but only slightly on the aeration rate.

• 미생물학회지
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• 제35권4호
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• pp.302-306
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• 1999

정장용 효모로 알려져 있는 Saccharomyces cerevisiae Hansen CBS5926의 생균제 제조를 목적으로 생균수 증대를 위한 배양조건과 배양 후 얻은 균체의 효과적인 동결건조 보존법에 관하여 조사하였다. 포도당을 탄소원으로 하는 회분식과 유가식 배양에 비해 에탄올을 탄소원으로 하는 유가식 배양이 장점이 많은 것으로 나타났으며, 배양 72시간 후 2.2${\times}$10^9 cfu/ml의 생균수와 38g/l의 건조 균체량을 얻을 수 있었다. 에탄올을 탄소원으로 하는 유가식 배양으로부터 얻은 균체의 동결보존을 위한 보호제의 효능을 비교한 결과, 20% 백당(w/v)과 30% 유당(w/v)에서의 생존율이 16.3%로서 비교된 다른 종류의 동결보호제보다 효과적인 것으로 나타났다. 그러나, 백당, 유당 및 탈지분유의 혼합에 의한 동해방지 보호 효과를 비교한 결과 생존율이 12.4~16.5%로서 보호제의 혼합에 따른 생존율의 상승효과는 나타나지 않았다.

• KSBB Journal
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• 제6권3호
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• pp.231-240
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• 1991

Recently, developments of large scale and high density cell culture methods have been the objects of many researches, because the demand of various pharmaceutical products produced by animal cell culture has been rapidly increasing. The cell culture equipment should have the requirements such as sufficient oxygen transfer and mixing, low shear stress and surface tension, and small foaming. In order to develop a proper bioreactor meeting these requirements simultaneously, a perfluorocarbon having high solubility of oxygen was sprayed into the medium as an oxygen carrier instead of air. Also, a new impeller was developed and combined together with the perfluorocarbon spraying system so as to design a new bioreartor for cell cultivation. The new impeller had better characteristics of mixing and oxygen transfer than the paddle and cell-lift impellers based on the same, shear rate. But, it was observed that the volumetric oxygen transfer coefficient of the new bioreactor decreased with increasing cell density during E. coli fermentation.

• Biotechnology and Bioprocess Engineering:BBE
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• 제4권1호
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• pp.21-25
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• 1999

Two low-salt complex media, bactopeptone and desalted yeast extract, were used for high density cultivation of the hyperthermophilic archaeon Sulfolobus solfataricus (DSM 1617). Bactopeptone, which has low mineral ion content among various complex media, was good for cell growth in batch cultures; the maximal cell density in bactopeptone was comparable to that in yeast extract. However, cell growth was rather poor when bactopeptone was added by the fed-batch procedure. Since several vitamins are deficient in abctopeptone, the effect of vitamins on cell growth was examined. Among the vitamins tested, pyridoxine was found to improve the growth rate of S. solfataricus. To reduce the growth inhibition caused by mineral ions, yeast extract was dialyzed against distilled water and then fed-batch cultures were carried out using a fed medium containing desalted yeast extract. Although the concentrations of mineral ions in yeast extract were significantly lowered by the dialysis whether low molecular weight solutes in yest extract are crucial for cell growth, we investigated the effect of trehalose, a most abundant compatible solute in yeast extract, on the growth pattern. Cell densities were increased and the length of the lag phase was markedly shortened by the presence of trehalose, indicating that trehalose plays an important role in the growth of S. solfataricus.

• Biotechnology and Bioprocess Engineering:BBE
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• 제1권1호
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• pp.32-35
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• 1996

Amoving aeration-membrane (MAM) bioreactor was employed for the production of 2$\mu$g/mL of tissue type Plasminogen Activator (tPA)in serum free medium from normal human fibroblast cells. This system could maintain high cell density for long periods of steady state conditions in perfusion cultivation. Under normal operating condition, shear stress was as low as 0.65 dynes/$\textrm{cm}^2$ at the agitation speed of 80 rpm. Even though cell density gradually decreased with increasing agitation speed, tPA production increased linearly with increasing shear stress within a moderate range. This culture system allowed production of 2$\mu$g tPA/mL while maintaining a high cell denisty of 1.0$\times$107 viable cell/mL.

• KSBB Journal
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• 제14권2호
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• pp.160-166
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• 1999

본 연구에서는 ($\beta$-carotene 생산균주인 미세조류 Dunaliella bardawil을 사용하여 batch flask에서 미세조류의 고농도세포에 관한 최적배양조건(미량원소, pH, agitation speed, nitrate, phosphate, carbon source)을 확립하고자 하였다. 미량원소는 5X 배지에서 교반하였을 때 비생장속도는 $0.0l3hr^{-l}$와 세포농도는 $4.9{\times}10^6$ cells/mL로서 IX. 3X, lOX 배지에서 배양한 것보다. 약 46%, 18%, 69% 높은 세포수율을 얻었으며 세포배양시 교반한 경우, pH는 80에서 최대 세포농도를 얻었다. 초기 nitrate ($KNO_3$)와 phosphate($KH_2PO_4$)의 영향을 조사한 결과 미세조류 생장에 중요한 영양분으로서 질소원의 주입은 매우 효과적임을 확인하였다. 또힌 탄소원으로서 250mM의 $NaHCO_3$와 $CO_2$ 가스를 동시에 사용한 배양조건이 500mM $NaHCO_3$만을 탄소원으로 사용한 실험에 비하여 32% 증가된 세포농도를 나타내었다. light는 white light의 경우 blue light보다 세포생장에 적합하였다. 질소원을 이용한 유기배양시 2회의 nitrate주입만으로써 배양 198hr에 $8.955{\times}10^6$cell/mL의 고농도의 세포를 얻었다.

• Biotechnology and Bioprocess Engineering:BBE
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• 제8권6호
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• pp.349-353
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• 2003

The physiological characteristics of cultures of very high cell mass (e.g. 10g cell mass/L), termed“ultrahigh cell density cultures”is reviewed. A close relationship was found between the length of the optical path (OP) in flat-plate reactors and the optimal cell density of the culture as well as its areal (g m$\^$-2/ day$\^$-1/) productivity. Cell-growth inhibition (GI) unfolds as culture density surpasses a certain threshold. If it is constantly relieved, a 1.0cm OP reactor could produce ca. 50% more than reactors with longer OP, e.g. 5 or 10cm. This unique effect, discovered by Hu et al. [3], is explained in terms of the relationships between the frequency of the light-dark cycle (L-D cycle), cells undergo in their travel between the light and dark volumes in the reactor, and the turnover time of the photosynthetic center (PC). In long OP reactors (5cm and above) the L-D cycle time may be orders of magnitude longer than the PC turnover time, resulting in a light regime in which the cells are exposed along the L-D cycle, to long, wasteful dark periods. In contrast, in reactors with an OP of ca. 1.0 cm, the L-D cycle frequency approaches the PC turnover time resulting in a significant reduction of the wasteful dark exposure time, thereby inducing a surge in photosynthetic efficiency. Presently, the major difficulty in mass cultivation of ultrahigh-density culture (UHDC) concerns cell growth inhibition in the culture, the exact nature of which is awaiting detailed investigation.