• KSBB Journal
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• 제8권5호
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• pp.457-464
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• 1993

회분식 배양을 통해 탄소원으로 초기 glucose 농도를 5g/$\ell$, lOg/$\ell$, 20g/$\ell$, 30g/$\ell$ 로 변화시키고, 초기 glucose 농도 20g/$\ell$ 에 저해제의 초기 acetIcacid 농도를 19/$\ell$, 2g/$\ell$, 3g/$\ell$, 4g/$\ell$, 5g/$\ell$ 로 변화시키면서 Bacillus amyloliquefacieηs 23350 균주를 이용하여 최적의 세포성장과 생성물 생산을 얻기 위한 배양을 시도하였다. 최대 건조세포밀도는 초기 glucose 농도가 증가할수록 증가하였고, 저해제로 acetic acid를 첨가하면 세포의 성장이 감소하였다. 탄소원 중 최대 $\alpha$-amylase의 생산은 초기 glucose 농도 lOgje 일 때 225unit/ml이었으며, 배양 기질 중 초기 acetic acid 농도가 2g/$\ell$ 일 때가 376unit/ml이었고, 최대 비세포성장속도와 최대 $\alpha$-amylase 의 비생성속도는 초기 glucose 농도가 109/E 일 때 $0.1239(hr^{-1})$ 과 2.34930unit/mg-hr로 최적이었다. 최적의 $\alpha$-amylase 생산 및 비생성속도를 얻기 위해서는 저해제로서 초기 acetic acid 농도를 2-4g/$\ell$ 정도 첨가하여 배양을 행하여야 한다.

• 한국미생물·생명공학회지
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• 제26권2호
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• pp.89-95
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• 1998

R. sphaereides K7 및 E15-1은 혐기적 광합성조건에서 glucose를 탄소원으로 하여 배양초기 24시간 동안은 수소가스를 계속 생산하였으나, 그 이후에는 배양액에 축적된 acetic acid및 formic acid가 배양액의 pH를 4.2-4.8로 저하시켜 수소를 거의 생산하지 못하였다. 또한 배양 6일 후에도 R. sphaeroides K7 및 E15-1의 glucose의 이용율은 각각 43% 및 74%에 불과하였다. 그러나 배양액의 pH를 6.8-7.0으로 유지하면서 배양한 결과 R. sphaeroides K7및 E15-1 두 균주 모두의 수소생산율과 glucose의 이용율이 증가되어, 수소생산은 배양 10일까지도 계속 증가되었으며, glucose도 두 균주 각각 배양후 2.5일 및 4.5일 후에 완전 소비하였다. 뿐만 아니라 균체 배양액의 pH를 중성으로 유지하면서 R. sphaeroides K7 및 E15-1을 배양할 경우 균체의 표백현상이 제거되어 배양 7일 후에는 각각 균체의 bacteriochlorophyll 함량이 약 44배 및 9배 증가되었으며, 이때 균체의 농도는 각각 약 10배 및 2.4배 증가되었다. R. sphaeroides K7 및 E15-1은 혐기적 광합성조건에서 acetic, lactic, butyric 및 malic acid로 부터도, 비록 그 양이 glucose로 부터보다는 적으나, 수소를 생산하였다. 본 실험 결과로 미루어 혐기적 광합성 조건에서 R. sphaeroides K7 및 E15-1은 glucose로부터 수소를 생성할 때 NADH 산화 및 hydrogenase가 관여한 대사가 우선적으로 일어나고, 2차적으로는 이때 생성된 유기산을 전자 공여체로 광합성 작용에 의해 질소원이 존재하지 않을 때 nirogenase에 의해서 양성자(H$^{+}$)가 환원되어 수소(H$_2$)가 생성되는 것으로 생각된다.

• Journal of Microbiology and Biotechnology
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• 제8권5호
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• pp.543-546
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• 1998

The effect of glucose concentration on the production of erythritol by Trichosporon sp. was mainly studied. The specific growth rate and production rate of erythritol gave the highest values of $0.23 h^{-1}\; and\; 4.2 g/\ell/h,\; respectively,\; on\; 100 g \; glucose/\ell$ of medium. The conversion yield of erythritol during the exponential phase and the stationary phase was constantly maintained at 19% and 51 %, respectively, while the glucose concentration in the medium varied from 100 g/$\ell$ to 400 g/$\ell$. The maximum overall erythritol conversion yield of 47% was obtained when the glucose concentration in the medium was 400 g/$\ell$. It corresponded to a 74% increase compared with the 100 g/$\ell$ glucose medium. The diauxy growth of this microbe was also observed. It grew exponentially consuming glucose, then after the second lag phase, biomass slowly increased using glycerol and erythritol.

• Asian-Australasian Journal of Animal Sciences
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• 제15권7호
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• pp.982-985
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• 2002

A study was carried out to determine glucose kinetics, nutrient balance and milk production of lactating Etawah crossbred goats. The animals (27.2 to 29.1 kg BW) were randomly divided into four levels of dietary treatment groups: the first group R1 received 100% (3 kg) fresh king grass (Penisetum purpuroides), the second group R2 received 75% king grass and 25% king grass silage prepared with chicken manure, the third group R3 received 50% king grass and 50% silage, and the fourth group R4 received 100% silage. In addition to the roughage, each group received 800 g of concentrate (CP 14.77% of DM; 17.26 MJ/kg). Animals fed king grass silage made with chicken manure were found to be superior to the group fed king grass alone. Glucose kinetics and retained energy were significantly affected. Calculations showed that glucose requirements for maintenance and milk production can be met for the groups with high levels of silage (R3 and R4). The values of glucose flux were in the range of 2.52 to 4.50 mg/min.kg $BW^{0.807}$ which are lower, but close to, the values for the temperate lactating dairy cow. The present glucose flux value for the lactating Etawah crossbred goat is higher than the previous value published from this laboratory.

• Journal of Microbiology and Biotechnology
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• 제29권6호
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• pp.905-912
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• 2019

Bioethanol has attracted much attention in recent decades as a sustainable and environmentally friendly alternative energy source. In this study, we compared the production of bioethanol by Candida molischiana and Saccharomyces cerevisiae at different initial concentrations of cellobiose and glucose. The results showed that C. molischiana can utilize both glucose and cellobiose, whereas S. cerevisiae can only utilize glucose. The ethanol yields were 43-51% from different initial concentrations of carbon source. In addition, different concentrations of microcrystalline cellulose (Avicel) were directly converted to ethanol by a combination of Trichoderma reesei and two yeasts. Cellulose was first hydrolyzed by a fully enzymatic saccharification process using T. reesei cellulases, and the reducing sugars and glucose produced during the process were further used as carbon source for bioethanol production by C. molischiana or S. cerevisiae. Sequential culture of T. reesei and two yeasts revealed that C. molischiana was more efficient for bioconversion of sugars to ethanol than S. cerevisiae. When 20 g/l Avicel was used as a carbon source, the maximum reducing sugar, glucose, and ethanol yields were 42%, 26%, and 20%, respectively. The maximum concentrations of reducing sugar, glucose, and ethanol were 10.9, 8.57, and 5.95 g/l, respectively, at 120 h by the combination of T. reesei and C. molischiana from 50 g/l Avicel.

• Journal of Plant Biology
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• 제12권2호
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• pp.7-14
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• 1969

Dunaliella tertiolecta did not show any increase in respiration rate when supplied with glucose, glycerol, sucrose, L-alanine, acetate, pyruvate and succinate. This was in contrast to Chlorella pyrenoidosa, which, under identical conditions, showed significant increase when supplied with glucose or acetate but not with the other compounds. Production of 14CO2 from added 14C-glucose in D. tertiolecta was lower than the other 14C-labelled substrates: L-alinine, glycerol, succinate, but higher than 14C-sucrose addition. And it was also lower than C. pyrenoidosa experiments which was added 14C-glucose as a substrate. Light reduced amounts of labelled carbon dioxide from 14C-glucose or 14C-acetate and increased incorporation of 14C from the substrates to cell materials in either D. tertiolecta or C. pyrenoidosa. The contribution of 14C from 14C-glucose to 14CO2 in cell-free system of D. tertiolecta were much higher than in whole cell suspension. It was contrast to C. pyrenoidosa which were showed reduction of 14CO2 production in cell-free systems than whole cell suspensions. When cell-free systems of D. tertiolecta and C. pyrenoidosa were supplied with ATP, NAD, NADP or/and hexokinase, it was remarkably increased production of 14CO2 from the substrates than the control. It was concluded that the low ability of D. tertiolecta to metabolize glucose were caused by the impermeability of the cell membrane to glucose and were not due to deficiencies of enzyme systems concerning glucose metabolism. In the cell-free systems, it seemed to be more active pentose phosphate pathway than glycolytic pathway in D. tertiolecta.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 추계학술발표대회 및 bio-venture fair
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• pp.352-355
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• 2000

Production of pullulan by Aureobasidium pullulans HP-2001 with agro-industrial byproducts was investigated. Agro-industrial byproducts from the rice processing industry for the traditional Korean food (AIB-A), apple juice production (AIB-B), and soybean sauce production (AIB-C) were used for carbon and nitrogen source for production of pullulan. Major components of AIB-A were glucose, maltose, maltotriose, and dextran. AIB-A and B were found to be good substitute to glucose as carbon source. Productivity of pullulan with AIB-A and B as carbon source was similar to that glucose. Molecular weight of pullulan produced with AIB-A and B was higher than that with glucose. Major components of AIB-B and C were carbohydrate, protein, fat and ash. AIB-C was also a good substitute to yeast extract as nitrogen source. Some of physiological conditions were examined for the large scale production of pullulan.

• Biomolecules & Therapeutics
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• 제26권1호
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• pp.39-44
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• 2018

In 1923, Dr. Warburg had observed that tumors acidified the Ringer solution when 13 mM glucose was added, which was identified as being due to lactate. When glucose is the only source of nutrient, it can serve for both biosynthesis and energy production. However, a series of studies revealed that the cancer cell consumes glucose for biosynthesis through fermentation, not for energy supply, under physiological conditions. Recently, a new observation was made that there is a metabolic symbiosis in which glycolytic and oxidative tumor cells mutually regulate their energy metabolism. Hypoxic cancer cells use glucose for glycolytic metabolism and release lactate which is used by oxygenated cancer cells. This study challenged the Warburg effect, because Warburg claimed that fermentation by irreversible damaging of mitochondria is a fundamental cause of cancer. However, recent studies revealed that mitochondria in cancer cell show active function of oxidative phosphorylation although TCA cycle is stalled. It was also shown that blocking cytosolic NADH production by aldehyde dehydrogenase inhibition, combined with oxidative phosphorylation inhibition, resulted in up to 80% decrease of ATP production, which resulted in a significant regression of tumor growth in the NSCLC model. This suggests a new theory that NADH production in the cytosol plays a key role of ATP production through the mitochondrial electron transport chain in cancer cells, while NADH production is mostly occupied inside mitochondria in normal cells.

• KSBB Journal
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• 제6권1호
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• pp.69-77
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• 1991

When S. fradiae was cultured in S medium, it stavted to produce neomycin in the middle of stationary phase of growth. Antibitoic production is regulated not only by glucose but also by metabolites formed from glucose. A chemically defined minimal salt broth was developen for the study of metabolites activating produition of antibiotic in a neomycin producer. When growth and production or antibiotic in minimal salt broth was examined with a full grown or a vefctativc mycelium, the medium was found not to be good for the growth, but to be good enough for the production of antibiotic with a full grown mycelium. When many carbotlydrates, organic acids, or alcohol were supplmented with instead of glucose in the medium suspcndcn with a full grown mycelium, the amount of antibiotic produced in the medium containing fumaratc was 5 times more than that in the medium with glucose. Further study indicated that the medium is not good also for the growth but good for the production of antibiotic. The antibiotic produced in this medium was identified to be neomycin. The activation of the production of neomycin by fumarate was further confirmed in a complex medium. Fuinarate is suspected to initiate and to activate the biosynthesis of neomycin at the gene level.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2003년도 생물공학의 동향(XIII)
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• pp.268-272
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• 2003

LSW는 유기질소원으로 가격이 가장 저렴하면서도 43.3 mL/L를 이용할 경우에 250 g/L의 glucose로부터 erythritol을 53%의 수율과 0.52 g/L-hr의 생산성 및 132 g/L의 농도로 생산이 가능하였다. 따라서 산업용 쓰이기에 충분한 가능성을 보였다. Erythritol의 생산성 향상을 위한 발효 조건의 최적화에 대한 실험을 수행한 결과 기본 발효배지에 65 mL/L의 농도로 LSW를 이용할 경우에 250 g/L의 glucose로부터 erythritol의 수율은 44% 약간 낮아졌지만, 생산성은 0.66 g/L-hr로 1.3배 증가하였다. Growth stage에서 고농도 균체를 얻기 위하여 glucose를 feeding 방법에 관한 연구에서는 glucose 100 g/L와 LSW 500 mL/L를 같이 넣고 배양하는 회분식 배양 방법을 통해 23시간만에 77.6 g/L의 균체를 얻을 수 있었다. Erythritol의 수율 향상을 위하여 production stage에서 최적의 glucose 농도에 대한 연구를 수행한 결과 발효조 내에서 glucose의 농도가 450 g/L 가 되도록 할 경우에 185.5 g/L의 erythritol을 37.3%의 생성 수율과 1.66 g/L-hr의 생산성으로 얻을 수 있었다. 따라서 산업용 질소원으로 선정된 LSW를 가지고 2단계 유가식 배양을 통하여 회분식 배양과 비교해 볼 때 수율은 1.1배정도 감소되었지만 erythritol의 생산성은 2.5 배 정도 향상시킬 수 있었다.