• KSBB Journal
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• 제13권6호
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• pp.730-734
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• 1998

An이ew식과 Aiba삭을 조합하여 에탄올 생산단주인 Saccharomyces cerevisiae ATCC 24858의 비성장속도를 당농도와 에탄올 농도의 함수로 표현하였다. 기침의 저해영향을 받지 않는 최대 당농도 $S_m$은 150 g/L이며 기질의 저해영향은 기질농도 S와 $S-S_{max}$항의 함수로 표현되었다. 최대 비성장 속도 ${\mu}max 는 0.49 hr^{-1}, Monod상수 K_s$는 19 g/L, Andrew식의 기질저해상수 $K_1$는 139 g/L이였다. 또한 비성장속도에 영향을 마치지 앓는 최대알콜농도 Pm이 존재하였으며 그 값은 2 g/L 이였다. 따라서 Aiba식에서 비성장속도에 영향을 미치는 에탄올 농도항은 P-Pm으보 표현되었다. 본 연구의 알코올생산균주에 대한 비성장속도의 완성된 수식은 디음과 같으며 이 수식에 위한 계산값은 평균오차 6% 내외의 범위에서 실험값과 일치하였다.

• 한국물환경학회지
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• 제33권4호
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• pp.441-448
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• 2017

Microcystis aeruginosa (M. aeruginosa) is a cyanobacterium species that can form harmful algal blooms in freshwater bodies worldwide. The use of Artemisia asiatica extracts to control M. aeruginosa inhibition will be environmentally friendly and promising. Artemisia asiatica extracts removed successfully upto 88% of M. aeruginosa pH 8 at $25^{\circ}C$ of temperature. These results was indicated that the amount of 2.24 g/L Artemisia asiatica extracts was removed 1g dryweight/L of M. aeruginosa. The kinetic data showed substrate inhibition kinetics and maximum growth rate was obtained when the M. aeruginosa was grown in medium containing 2.5 g/L of initial concentration of Artemisia asiatica extracts. In the various growth control models, Luong model showed the highest correlation coefficient of 0.9916. Therefore, the Luong model was the most suitable control model for the growth control of M. aruginosa using Artemisia asiatica extracts. In conclusion, the growth control of M. aruginosa using Artemisia asiatica extracts can be applied in the field without controlling the temperature and pH of rivers and streams, and it is possible to control the growth of M. aruginosa efficiently in a short time. The natural extract, Artemisia asiatica extracts, can be a promising inhibition due to its high efficiency and low dose requirements.

• Journal of Microbiology and Biotechnology
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• 제22권12호
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• pp.1758-1766
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• 2012

An extensive investigation was carried out to describe the kinetics of cell growth, substrate consumption, and product formation in the batch fermentation using starch as substrate. Evaluation of intrinsic kinetic parameters was carried out using a best-fit unstructured model. A nonlinear regression technique was applied for computational purpose. The Andrew's model showed a comparatively better $R^2$ value among all tested models. The values of specific growth rate (${\mu}_{max}$), saturation constant ($K_S$), inhibition constant ($K_I$), and $Y_{X/S}$ were found to be 0.109 $h^{-1}$, 11.1 g/l, 0.012 g/l, and 1.003, respectively. The Leudeking-Piret model was used to study the product formation kinetics and the process was found to be growth-associated. The growth-associated constant (${\alpha}$) for protease production was sensitive to substrate concentration. Its value was fairly constant up to a substrate concentration of 30.8 g/l, and then decreased.

• Journal of Microbiology and Biotechnology
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• 제15권2호
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• pp.368-375
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• 2005

Batch cultures were carried out to optimize the exo-polysaccharide production by liquid cultures of Pleurotus ferulae. Among the various carbon sources, when $5\%$ of glucose was used, the maximum mycelial growth and exo-polysaccharide concentration reached were 8.78 g/l and 3.59 g/l, respectively. Yeast extract and polypeptone were identified as the most suitable nitrogen sources. In particular, when a mixture of $1\%$ of polypeptone and $0.8\%$ of yeast extract was used, 9.52 g/l of mycelial growth and 4.09 g/l of exo-polysaccharide were obtained. In the case of mineral sources, K$_2$HPO$_4$ and MgSO$_4$$\codt$7H$_2$0 were found to be the best mineral sources for mycelial growth and exo-polysaccharide production. Under the optimized culture conditions, the agitation speed and aeration were investigated for mycelial growth and exo­polysaccharide production in a jar fermentor. The maximum mycelial growth and exo-polysaccharide concentration at 1.5 vvm and 200 rpm obtained were 13.2 g/l and 4.95 g/l, respectively, after 10 days of culture, which were $76\%$ and $79\%$ higher than those of the basal medium. The specific growth rate was decreased with the increase of mycelial growth. However, the specific production rate of the exo-polysaccharide was proportionally increased with the specific growth rate. The proposed model profiles showed good agreement with the experimental results for the mycelial growth and exo-polysaccharide production. The specific production rate using the optimized medium was higher than that of basal medium.

• Biotechnology and Bioprocess Engineering:BBE
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• 제11권1호
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• pp.72-79
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• 2006

Kojic acid production by Aspergillus flavus strain S44-1 using sucrose as a carbon source was carried out in a 250-mL shake flask and a 2-L stirred tank fermenter. For comparison, production of kojic acid using glucose, fructose and its mixture was also carried out. Kojic acid production in shake flask fermentation was 25.8 g/L using glucose as the sole carbon source, 23.6 g/L with sucrose, and 6.4 g/L from fructose. Reduced kojic acid production (13.5 g/L) was observed when a combination of glucose and fructose was used as a carbon source. The highest production of kojic acid (40.2 g/L) was obtained from 150 g/L sucrose in a 2 L fermenter, while the lowest kojic acid production (10.3 g/L) was seen in fermentation using fructose as the sole carbon source. The experimental data from batch fermentation and resuspended cell system was analysed in order to form the basis for a kinetic model of the process. An unstructured model based on logistic and Luedeking-Piret equations was found suitable to describe the growth, substrate consumption, and efficiency of kojic acid production by A. flavus in batch fermentation using sucrose. From this model, it was found that kojic acid production by A. flavus was not a growth-associated process. Fermentation without pH control (from an initial culture pH of 3.0) showed higher kojic acid production than single-phase pH-controlled fermentation (pH 2.5, 2.75, and 3.0).

• 생명과학회지
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• 제15권1호
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• pp.15-20
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• 2005

동충하초 Paecilomyces tenuipes C240의 균사체 배양과정에서 균사체 성장, 세포외 다당체 생산, 기질감소 속도를 표현할 수 있는 동력학적 모델을 제시하였다. 균사체 성장은 Logistic식을, 세포외 다당체 생산은 Luedeking-Piret 식을, 기질소모는 Luedeking-Piret 유사식을 각각 적용함으로써, 전체 균사체 배양과정을 예측할 수 있었다. 모델식에서 사용된 주요 kineti, constant들은 다음과 같다: 균사체의 최대 비성장속도${\mu}m,\;0.7281\;h^{-1};$; 다당체 생산에서의 growth-associated constant $(\alpha),\;0.1743g(g\;cells)^{-1}$; non-growth-associated constant $(\beta),\;0.0019g(g\;cells)^{-1}\;;$ maintenance coefficient ($(m_s),\;0.0572g\;(g\;cells)^{-1}$·5L 발효조에서 얻은 균사체 성장, 세포외 다당체 생산, 기질감소 속도자료들을 모델에서 예측한 결과와 비교한 결과 서로 잘 일치하는 것으로 보아, 본 연구에서 제안된 모델식은 이 동충하초 균사체 배양공정의 scale-up등의 프로세스 설계에 응용가능 할 것이며, 다른 종류의 동충하초 균사체 배양공정에도 적용가능 할 것으로 판단된다.

• 생약학회지
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• 제44권3호
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• pp.275-280
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• 2013

This study was carried out to investigate the effect of Origanum vulgare extracts on cell proliferation of human hair dermal papilla cell (HHDPC) using sulforhodamine B (SRB) assay, antioxidant activity by 1,1-diphenyl-2-picryl hydrazyl (DPPH) method, expression of insulin-like growth factor-1 (IGF-1) by analyzing reverse transcriptase polymerase chain reaction (RT-PCR) and hair growth in a shaving animal model of C57BL/6 mice topically applying with an amount of 0.1 mL once a day for 3 weeks. The mice were divided into 4 groups including normal group (saline, N), negative control group (dimethyl sulfoxide, NC), positive control group (5 mg/mL minoxidil, PC), and experimental group (Origanum vulgare extracts, OV). Treatment of OV didn't show cytotoxicity in HHDPC up to 10 ${\mu}g/mL$ and exhibited antioxidant activity with $IC_{50}$ of 31.0 ${\mu}g/mL$. IGF-1 expression in the skin was significantly (p<0.05) increased in the PC and OV compared to the N or NC. PC and OV also showed a prominently promoted hair regrowth compared to the N or NC in hair growth observation. The hair regrowth of OV was significantly higher than that of PC (p<0.05). Therefore, these results indicate that O. vulgare extracts effectively stimulated hair growth in an animal model.

• Journal of Microbiology and Biotechnology
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• 제9권6호
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• pp.716-721
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• 1999

It has been known that continuous cultivation of hairy root is difficult to maintain for a long period of time compared to the microbial and callus cultures. Chemostat cultivation was successfully carried out in order to economically produce a plant-based colorant, betacyanin, from red beet hairy root for more than 85 days in a 14-1 fermentor. The result from the chemostat cultivation was compared to those of the batch and fed-batch cultivations of red beet hairy roots. It was shown that hairy root reached its steady state within 50 days of the cultivation, and then maintained for about 25-30 days in a wide range of dilution rates. Total betacyanin production from the continuous process was also calculated to be 2.65g at 0.28(l/d) of dilution rate, compared to 0.196g from fed-batch cultivation. It was found that betacyanin production was a partially growth related process, yielding 0.376 mg/g-fresh wt. cell and $1.89{\times}10^{-5}$ mg/g-fresh wt. cell/d, with 0.92 of correlation factor in a partial growth-product model. It was also shown that the cell growth required was relatively large for maintenance amount of energy at a low dilution rate. The growth of hairy root was inhibited by high light intensity in following a photo-inhibition model. The growth parameters were estimated to be 0.3(l/d), $10.56kcal/\textrm{m}^2/h$,{\;}and{\;}35.81kcal/\textrm{m}^2/h$ for the maximum specific growth rate, half saturation light intensity, and inhibition light intensity, respectively.

• 한국미생물·생명공학회지
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• 제26권5호
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• pp.435-441
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• 1998

Red beet(Beta vulagris L.) 모상근의 회분배양을 이용한 천연색소인 betacyanin 생산 최적화를 위해 광도, C/N ratio, 인산의 농도를 각각 변화시켜 세포생육과 색소 생산성에 관한 동력학적 분석을 실시했다. 광도변화에 따른 배양 결과 3 klux의 경우 0.3(1/day)의 최대 비 생육속도와 0.11(mg/g-dry cell/day)의 최대 비 생산속도 그리고 14 k1ux에서 0.242(1/day)의 최대 비 생육속도와 0.125(mg/g-dry cell/day)의 최대 비 생산속도를 나타냈다. 광도와 균체의 생육관계를 검토한 결과 광도에 따른 세포 생육은 photoinhibition model이 적용됨이 확인되었다. Red beet 모상근으로부터 betacyanin의 생산은 partially growth related process임이 입증됐다. 이에 따른 세포당 최대 betacyanin 생산을 나타내는 $\alpha$는 0.3756 (mg/cell)이며, 최대 생산속도를 나타내는 $\beta$는 0.001 (mg/g-cel1/day)로 측정됐다. C/N ratio에 따른 실험결과 42.1(w/w)에서 0.26(1/day)의 최대 비생육 속도를 나타내었으나 최대 비 생산속도는 31.6(w/w)에서 0.075(mg/g-cell/day)를 나타냈다. 인 농도에 대한 균체의 생육 및 물질 생산성의 관계를 검토한 결과 1.25mM에서 0.31(1/day)의 비생육 속도와 0.134(mg/g-dry cell/day) 비생산 속도를 나타내었다. 최적 조건을 결정하기 위한 response surface methodology(RSM)결과 세포 생육과 betacyanin의 최대 생산을 위한 최적 광도는 5.5 (klux),최적 C/N ratio와 인의 농도는 27(w/w), 1.25 (mM)로 결정됐다. 그리고 0.1 $\mu$M kinetin 첨가시 대조구에 비해 비생산성이 0.085(mg/g-dry cell/day)로 증가함이 입증됐다. Normal조건과 optimum조건의 비교결과 세포의 농도인 X(g-dry wt./L)가 8와 16, betacyanin의 생산량인 P(mg/L)가 4.48과 12.5, 그리고 optimum 조건에서 최대비 생육속도인 $\mu$$_{max}$ 가 0.375와 그리고 최대비 생산속도인 q$^{max}$ $_{p}$ 는 0.134로 약 2배로서 최적화가 되었다.

• KSBB Journal
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• 제4권3호
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• pp.259-265
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• 1989

당근세포의 현탁배양에서 배지중 제한영양소인 인산염과 글루코우즈 농도에 대한 당근세포 배양특성에 관한 실험으로부터 다음의 결론을 얻었다. 1) 배지중의 글로코우즈와 인산염을 제한영양소로 하였을 때, 현탁배양 중의 글루코우즈의 농도 1.49g/l - 3.01g /l, 인산염의 농도 0.08mM - 1.06mM의 범위에서 세포성장 정체기에 도달하는 시간은 13.2hr-66.4hr였고 제한영양소의 전환율은 초기 글루코우즈와 인산염의 농도의 5~30% 범위내에 분포되었다. 2) 제한 영양소의 저농도범위에서의 농도변화에 따른 세포의 비성장속도, $\mu$는 $0.15day^{-1}$와 $0.3day^{-1}$사이의 값으로 일정한 경향을 보이지 않았는데, 이것은 제한요소가 저농도로 존재할 때 세포의 비성장속도에 미치는 영향이 적음을 알 수 있다. 3) 제한 영양소의 소모량과 세포증가량 사이에는 선형적 관계를 나타내며, 제한 영양소 글루코우즈에 대한 세포수율($Y_{x/sG}$)은 인산염 0.32mM, 글루코우즈 2.67g/l에서 $98.71{\times}10^{10}개\;/\;g로$ 최대값을 나타내었다. 4) 제한 영양소의 비($s_G/s_P$)에 대한 비성장속도, $\mu$ 및 세포수율($Y_{x/s_G}$는 두 농도의 비($s_G/s_P$)가 20mM/mM-120mM/mM 사이에서 임의적으로 분포하였다.