• 한국수소및신에너지학회논문집
• /
• 제23권4호
• /
• pp.397-403
• /
• 2012

Galactose, an isomer of glucose with an opposite hydroxyl group at the 4-carbon, is a major fermentable sugar in various promising feedstock for hydrogen production including red algal biomass. In this study, hydrogen production characteristics of galactose-glucose mixture were investigated using batch fermentation experiments with heat-treated digester sludge as inoclua. Galactose showed a hydogen yield compatible with glucose. However, more complicated metabolic steps for galactose utilization caused a slower hydrogen production rate. The existence of glucose aggravated the hydrogen production rate, which would result from the regulation of galactose-utilizing enzymes by glucose. Hydrogen produciton rate at galactose to glucose ratio of 8:2 or 6:4 was 67% of the production rate for galactose and 33% for glucose, which could need approximately 1.5 and 3 times longer hydraulic retention time than galacgtose only condition and glucose only condition, respectively, in continuous fermentation. Hydrogen production rate, Hydrogen yield, and organic acid production at galactose to glucose ratio of 8:2 or 6:4 were 0.14 mL H2/mL/hr, 0.78 mol $H_2$/mol sugar, and 11.89 g COD/L, respectively. Galactose-rich biomass could be usable for hydogen fermenation, however, the fermentation time should be allowed enough.

• 한국미생물·생명공학회지
• /
• 제24권2호
• /
• pp.149-154
• /
• 1996

Effect of glucose addition to xylose medium on xylitol production was investigated by using Candida parapsilosis ATCC 21019 mutant. With increasing the ratio of glucose to xylose in total amount of 50 g/l as glucose and/or xylose, xylitol production was decreased but ethanol and glycerol production were increased. Ethanol and glycerol concentration were maxmum in 10 g/l of xylose and 40 g/l of glucose medium as 21.5 g/l and 3.6 g/l, respecti- vely. No xylitol was formed in glucose medium without xylose because xylitol could be not produced from glucose. With increasing the ratio of glucose to xylose, the activity of xylose reductase which converted xylose to xylitol were decreased. The activities of xylitol dehydrogeiiase which converted xylitol to xylulose and then cell materials were found to be constant regardless of the ratio of glucose to xylose. This results indicated that glucose addition to xylose medium on cell growth was not affected. In order to prevent the inhibitory effect of glucose on xylitol production, glucose in a fermentor was fed with low concentration and then ethanol and glycerol was critically decreased and the xylitol yield from xylose of the culture with glucose feeding was recovered the almost same as that with only 50 g/l of xylose. However, the xylitol yield from total sugars (xylose and glucose) was decreased and glucose was not contributed to xylitol production. Therefore, the fermentation at high concentration of xylose without glucose was carried out. A final xylitol concentration of 242 g/l which corresponding 80.7% of xylitol yield was obtained from 300 g/l of xylose for 273 hours.

• 한국미생물·생명공학회지
• /
• 제25권5호
• /
• pp.495-500
• /
• 1997

Xylitol production from xylose and glucose was investigated using Candida tropicalis KFCC-10960. As glucose concentration in xylose medium was increased, ethanol production increased. However, xylitol production was maximum at glucose concentration of 10 g/l. The concentrated cells grown on xylose or glucose were inoculated in xylose medium. The specific activities of xylose reductase and xylitol dehydrogenase, and xylitol production in concentrated cells grown on glucose were the same as those in concentrated cells grown on xylose. The results suggested that cells grown on glucose had the same xylitol producing activity as those grown on xylose. By feeding glucose in xylose medium, cell growth was achieved from glucose and xylitol production was obtained from xylose. By using this technique, a final xylitol concentration of 261 g/l was achieved from 300 g/l xylose in 41 hours which corresponded to a xylitol yield from xylose of 87% and a xylitol productivity of 6.37 g/1-h.

• KSBB Journal
• /
• 제10권3호
• /
• pp.323-334
• /
• 1995

Hybridoma 세포의 세포 성장 속도, monoclo nal antibody의 생산성 및 세포 대사에 미치는 glucose의 영향이 조사되었다. IgG2,를 생산하는 m mouse-mouse hybridona VIII H-8 세포가 모델로 이용되었다. Glucose 농도에 따른 바성장속도의 변화는 기질저해형식 (substrate inhibition type) 의 성장모델로 나타낼 수 있었다. 초기 glucose 농도 4g/f까지는 최대 세포밀도의 증가를 보여 주었다. Glucose는 세포사망속도에 큰 영향을 나타내었고 glucose 농도와 비사망속도 간에는 반비례의 관계가 성립됨을 보였다. Glucose 농도가 증가될수록 세포의 생존율과 monoclonal an tibody의 생산이 증가되었다. Glucose 놓도가 증가될수록 glucose의 비소비속도가 증가되 었고, 초기 glucose 농도의 증가는 lactate의 총괄 비 생산속도의 증대를 가져왔다. 암모늄 이온의 총괄비 생산속도는 초기 Glucose의 농도에 의존하 였지만 암모늄 이온의 전반적인 생성속도는 초기 glucose 농도에 거 의 무관함을 보여 주었다.

• 한국미생물·생명공학회지
• /
• 제24권4호
• /
• pp.404-407
• /
• 1996

The effects of carbon sources on vancomycin production were investigated using Nocardia orientalis CSVC 3300. Among carbon sources tested, glucose, maltose and fructose were effective for the production of vancomycin. Glucose was favored for growth, but decrease the production of vancomycin at the concentration above 7.5%. In comparison, maltose did not decrease the production of vancomycin up to the concentration of 20%. When the mixture of glucose and maltose was used in the ratio 1:3 to 1:4, the highest production of vancomycin was achieved. When glucose concentration was set at 3.0%, catabolite repression could not be observed up to total sugar concentration of 16.0%. Fermentation was carried out using commercial hydrolyzed starch composed of glucose, maltose, maltotriose and maltotetraose, The initial glucose concentration was set at 3.0% and subsequent oligosaccharide consumption was monitored by checking their supernatant with HPLC. During initial cultivation for 38 hour, glucose was the sole carbon source leading to rapid growth. After cell growth stopped, the maltose and glucose concentrations increased due to degradation of maltotriose and maltotetraose, but glucose level was maintained at around 3.0%. After 70 hour fermentation, maltose slowly converted to glucose, and vancomycin production continued during the period.

• 한국식품영양학회지
• /
• 제10권1호
• /
• pp.117-121
• /
• 1997

Arthrobacter sp. L-3로부터 glucose isomerase의 생산성을 검토하였다. 배지의 탄소원으로는 glucose와 xylose를 혼합해서 공급한 것이 효소 생산성이 가장 높았다. 질소원으로는 yeast extract가 가장 높은 효소 생산성을 나타내었다. Glucose isomerase의 생산성은 배양시간이 40시간일 때 가장 높게 나타났다.

• 한국식품과학회지
• /
• 제28권6호
• /
• pp.1151-1156
• /
• 1996

Candida parapsilosis KFCC-10875를 사용하여 xylose와 glucose가 xylitol 생산에 미치는 영향을 조사하였다. Xylose만 50 g/l 함유하는 배지에서 배양하면 xylitol만 생성되었고 xylose에 glucose를 첨가하여 배양하면 부산물로 ethanol과 glycerol이 생성되었다. Glucose 함량이 높을수록 xylitol 생성량은 감소하였지만 ethanol과 glycerol의 양은 증가하여 xylose 10 g/l와 glucose 40/l일 때 최대값 각각 21.5 /l, 3.6 g/l의 최대값을 나타내었다. Glucose에서는 xylitol이 생성되지 못하기 때문에 glucose만 존재하는 배지에서는 xylitol이 전혀 생성되지 않았다. Xylose에 대한 glucose의 비율을 증가시키며 배양한 결과 glucose 비율이 높을수록 이용된 xylose에 대한 생성된 xylitol의 수율이 감소하였다. 첨가하는 ethanol의 농도를 변화시키면서 배양한 결과 첨가된 ethanol의 농도가 증가할수록 xylose에 대한 생성된 xylitol의 생산이 감소하였고 부산물을 제거한 후 배양할 경우 xylitol생산이 저해되지 않았다. 이것은 xylose에 대한 생성된 xylitol의 수율이 ethanol가 같은 부산물에 의한 것이라는 것을 의미한다. Xylose 또는 glucose에서 성장한 균체를 약 20 g/l로 농축하여 xylose 50g/l가 포함된 발효배지에 접종하여 배양하였다. Glucose에서 성장한 균체를 사용한 xylitol 생산에서 xylose reductase와 xylitol dehydrogenase의 총역가는 농축균체를 사용하지 않는 일반 배양의 그것과 거의 비슷하였다. 그러나, xylose에서 성장한 농축균체를 사용한 발효에서의 xylose reductase의 역가와 xylitol dehydrogenase의 역가는 비교적 높게 나타나 일반배양의 역가와 비슷하였다. 그러므로 xylitol 생산성은 균체농도를 증가시킬수록 비례적으로 증가하여 xylose에서 성장한 농축균체로 발효시간 18시간에 50 g/l의 xylose로부터 40 g/l의 xylitol을 얻을 수 있었다.

• Biotechnology and Bioprocess Engineering:BBE
• /
• 제7권3호
• /
• pp.171-177
• /
• 2002

The metabolic flux pattern for L-histidine production was analyzed when glucose and/or acetate were used as carbon sources. Total L-histidine production was enhanced when mixed substrate (glucose and acetate) was used, compared wish that when either glucose or acetate was used as the sole carbon source. Theoretical maximum carbon fluxes through the main pathways for L-histldine production, cell growth, and ATP consumption for cell maintenance were obtained by the linear programming (LP) method. By comparison of the theoretical maximum carbon fluxes tilth actual ones, it was found that a large amount of glucose was actually used for maintenance of cell viability. On the other hand, acetate was used for cell growth. After depletion of acetate in the mixed substrate culture, the flux for glucose to L-histldine synthesis was markedly enhanced. A strategy for effective L-histidine production using both carbon sources was proposed.

• 공업화학
• /
• 제18권2호
• /
• pp.162-167
• /
• 2007

본 연구에서는 Clostridium beijerinckii Donker 1926을 이용한 연속식 혐기성 소화공정에서 수소 생산과 동력학적 특성을 고찰하였다. 기질은 glucose를 사용하였고, 0.5, 0.25, 0.125일의 체류시간 (hydraulic retention time, HRT)에서 실험이 이루어졌으며, 모든 HRT의 조건에서 탄산화물은 99% 이상의 제거효율를 나타내었다. 체류시간이 짧을수록, COD 제거율은 낮은 반면에, 전체 가스 중에서 수소 가스 함량과 수소 발생량이 높게 나타났다. 또한, 정상상태에서, 증식 수율과 수소가스 생성 수율은 각각 0.27 g-VSS/g- glucose, 0.26 L/g-glucose로 나타났다. 본 실험에 사용된 균주를 glucose와 같이 당 성분이 함유된 폐수처리에 적용하면 수소를 생산할 수 있으며, 이러한 실험 결과들을 잘 활용하면 대체에너지로서, 실제적인 수소가스 생산 시스템에 적용할 수 있을 것이다.

• 동아시아식생활학회지
• /
• 제7권1호
• /
• pp.29-33
• /
• 1997

The efficient production of glucose isomerase (G. I0.) produced form Arthrobacter sp. L-3 was studied. The optimum culture time of the enzyme was 40hr. The maximum enzyme activity was found at glucose concentration 1%. G. I. activity did not affect inoculum size. The glucose isomerase activity was strongly influenced by the addition of glucose.