• 한국생물공학회:학술대회논문집
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• 2000.11a
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• pp.287-290
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• 2000

To examine effects of agitation and aeration as well as adding of glucose and yeast extract on cell growth and polysaccharide production by Paecilomyces japonica, batch culture was carried out at 5L jar fermenter at $27^{\circ}C$ with the initial pH 7 for 7 days cultivation(innoculum size 2%, working volume 3L). Media compositions(g/L) were 30 glucose, 20 yeast extract, 0.5 $KH_2PO_4$, $0.1\;CuCl_2\;{\cdot}\;2H_2O$. Optimum culture conditions of agitation and aeration in batch culture were 400 rpm and 1.0 vvm, resulting in 23.1 g/L biomass and 2.5 g/L polysaccharide. Additional feeding of glucose and yeast extract with a pulse mode conferred an advantage on cell growth and polysaccharide production with showing the results of 29.2 g/L and 3.3 g/L, respectively.

• 한국생물공학회:학술대회논문집
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• 2001.11a
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• pp.434-437
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• 2001

Shaking cultivation was carried out in 250 mL Erlenmeyel' flasks containing 60 mL of culture solution for 7 days. Artificial seawater was used as a basal culture medium. The cultivation was performed under the conditions that the temperature ranged from $4^{\circ}C$ to $32^{\circ}C$, the agitation speed 50 rpm to 200 rpm, and the sugar concentration 5 g/L to 35 g/L. The medium condition was cultured that sugar and nitrogen ratio 1.25 to 10. The biomass. the lipid content in biomass, and the DBA content of lipid were investigated according to the cultivation conditions. The lipid in biomass was distributed between 10 and 349'0, the DHA in lipid 34% to 43% of the lipid. and the biomass concentration 0.425 g/L to 4.50 g/L.

• 한국생물공학회:학술대회논문집
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• 2000.04a
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• pp.231-234
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• 2000

The polysaccharide has been known to have an antitumor activity, which were extracted from the fruiting bodies, mycelia, and culture broths of Agaricus blazei. For the cell growth and the polysaccharide production, the optimal medium contained 8% glucose, 2% yeast extract, 0.1% $MgSO_4{\cdot}7H_2O$, 0.2% $KH_2PO_4$, 0.2% $CaCl_2{\cdot}2H_2O$ and 0.2% $MnSO_4{\cdot}5H_2O$. When 0.2% of glutamic acid was added at 4day, the cell concentration was 13.5 g/L and the polysaccharide production was 9.9 g/L, respectively.

• Journal of Applied Biological Chemistry
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• v.61 no.2
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• pp.119-124
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• 2018

In vitro anticancer and antioxidant effects of acetone extract from leaves of Eucommia ulmoides Oliver were investigated. The extraction yield and total phenolic content of the acetone extract were $1.13{\pm}0.033%$ (w/w) and $36.7{\pm}1.96mg$ gallic acid equivalents/g-extract, respectively. $GI_{50}$ values of the acetone extract for human non-small cell lung cancer cells (A549), human colon cancer cells (SNU-C4), human cervical cancer cells (HeLa), and human embryonic lung epithelial cell (L132) were 53.4, 53.8, 88.3, and $153.9{\mu}g/mL$, respectively. The acetone extract effectively inhibited the proliferation of human non-small cell lung cancer (A549) and colon cancer (SNU-C4) cells in a concentration-dependent manner, but was less cytotoxic with human normal cells (L132). $EC_{50}$ values of the acetone extract for free radical scavenging, reducing power, and lipid peroxidation inhibition were about 2,000, 275.8, and $257.9{\mu}g/mL$, respectively. The acetone extract showed a potent reducing power and lipid peroxidation inhibitory activity in a concentration-dependent manner.

• Applied Biological Chemistry
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• v.41 no.7
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• pp.496-499
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• 1998

For the production of theobromine from caffeine, 5 strains of bacteria capable of producing theobromine were isolated from soil. Among them, the strain CT-017 showed the best ability of producing theobromine, and was partially identified as a Pseudomonas sp. For the production of theobromine, fructose was the most effective carbon source at an optimum concentration of 5 g/l. The most effective nitrogen source was 5 g/l of beef extracts. And 0.02 g/l of $Fe^{2+}$, 1.0 g/l of threonine were effective for the production of theobromine. The optimum temperature and initial pH were $28^{\circ}C$ and 6.5, respectively. After 23 hr cultivation, 7.98 g/l of theobromine was produced from 15 g/l of caffeine which corresponds to a conversion yield of 53.2%.

• KSBB Journal
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• v.22 no.5
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• pp.345-350
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• 2007

Phosphosugars are found in all living organisms and are commercially valuable compounds with possible applications in the development of a wide range of specialty chemicals and medicines. In carbohydrate metabolism, fructose 6-phosphate (F6P) is an essential intermediate formed by phosphorylation of 6' position of fructose in glycolysis, gluconeogenesis, pentose phosphate pathway and Calvin cycle. In glycolysis, F6P lies within the glycolysis metabolic pathway and is produced by isomerisation of glucose 6-phosphate. For large-scale production, F6P could be produced from starch using many enzymes such as pullulanase, starch phosphorylase, isomerase and mutase. In enzymatic reactions carried out at high temperatures, the solubility of starch is increased and microbial contamination is minimized. Thus, thermophile-derived enzymes are preferred over mesophile-derived enzymes for industrial applications using starch. Recently, we reported the production of glucose 1-phosphate (G1P) from starch by Thermus caldophilus GK24 enzymes. Here we report the production of F6P from starch through three steps; from starch to glucose 1-phosphate (glucan phosphorylase, GP), then glucose 6-phosphate (phosphoglucomutase, GM) and then F6P (phosphoglucoisomerase, GI). Using 200 L of 1.2% soluble starch solution in potassium phosphate buffer, 1,253 g of G1P were produced. Then, 30% yields of F6P were attained at the optimum reaction conditions of GM : G1 (1 : 2.3), 63.5$^{\circ}C$, and pH 6.85. The optimum conditions were found by response surface methodology and the theoretical values were confirmed by the experiments. The optimum starch concentrations were 20 g/L under the given conditions.

• Journal of Microbiology and Biotechnology
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• v.23 no.4
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• pp.483-488
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• 2013

Ginsenoside Rd was produced from ginsenoside Rc using a thermostable recombinant ${\alpha}-{\small{L}}$-arabinofuranosidase from Caldicellulosiruptor saccharolyticus. The optimal reaction conditions for the production of ginsenoside Rd from Rc were pH 5.5, $80^{\circ}C$, 227 U enzyme/ml, and 8.0 g/l ginsenoside Rc in the presence of 30% (v/v) n-hexane. Under these conditions, the enzyme produced 7.0 g/l ginsenoside Rd after 30 min, with a molar yield of 100% and a productivity of 14 g $l^{-1}\;h^{-1}$. The conversion yield and productivity of ginsenoside Rd are the highest reported thus far among enzymatic transformations.

• Korean Journal of Fisheries and Aquatic Sciences
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• v.42 no.6
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• pp.628-632
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• 2009

In order to estimate acute toxicity of various heavy metals on mysid, Neomysis japonica, the experiments were conducted by renewal bioassay method at $20\pm0.5^{\circ}C$ and $30\pm0.3$ psu salinity. The 96 hr $LC_{50}$ of Neomysis japonica exposed to cadmium, copper, zinc, arsenic, lead and chromium were $90.4\;{\mu}g/L$, $82.3\;{\mu}g/L$, $646.1\;{\mu}g/L$, $1488.5\;{\mu}g/L$, $1758.8\;{\mu}g/L$ and $1609.6\;{\mu}g/L$, respectively, and were ranked in order of toxicity: copper > cadmium > zinc > arsenic > chromium > lead.

• 한국생물공학회:학술대회논문집
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• 2001.11a
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• pp.347-350
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• 2001

The dextran prodution by Leuconostoc mensenteroids NRRL-B512F was studied in a synthetic medium from sucrose as a sole carbon source. Especially, effect of nitrogen source was treated and compared in this study. In oder to maximize the cell growth and dextran produtivity through fermentation two nitrogen sources, yeast extract and tryptone, were used with various concentrations. At the end of fermentation, when the concentration of yeast extract was 9g/L we can obtain the maximum dry cell weight(14.1g/L), dextran dry weight(25.4g/L) and productivity(1.4g/L ${\cdot}$ hr).

• 한국생물공학회:학술대회논문집
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• 2000.11a
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• pp.283-286
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• 2000

In order to maximize the cell growth and the polysaccharide production in Agaricus blazei, two kinds of fed-batch fermentation processes were performed with varying the feeding medium compositions and the feeding process. The relationship between dissolved oxygen and polysaccharide production in batch fermentation was applied to fed-batch fermentation. The biomasss concentration was 18.2 g/L and the polysaccharide production was 10.4 g/L.