• Korean Journal of Microbiology
• /
• v.50 no.4
• /
• pp.372-375
• /
• 2014

This experiment was undertaken to investigate proper conditions for protoplast isolation and genetic transformation of the white rot fungi, Polyporus brumalis. The protoplasts were formed from mycelia at a frequency of $1{\times}10^7/ml$ with 0.5% Usukizyme. The transformation vector (pHYgpt) was constructed using hygromycin resistance gene (hph) for the selectable maker. The yield was 100-160 transformants/${\mu}g$ DNA in a transformation mediated by 40% polyethylene glycol solution with aurintricarboxylic acid, heparin and supermidine. The genomic integration of the pHYgpt was confirmed by hph-specific PCR and the expected amplified band appeared only in the transformants. These results could be an efficient tool in gene engineering of the genus polyporus.

• KSBB Journal
• /
• v.21 no.1 s.96
• /
• pp.49-53
• /
• 2006

The aim of this research is to estimate the values of biological kinetic parameters of pharmaceutical wastewater for understanding biochemical properties. Maximum specific growth rate (${\mu}m$), yield coefficient (Y), and half-velocity coefficient (KS) were determined using oxygen uptake rate (OUR), and the results were 10.49/day (0.437/hr), 0.655, and 38.89 mg/L, respectively. Measured ${\mu}max$ by nonlinear regression of Monod equation was 10.63/day (or 0.443/hr), and this value was similar with above result. These parameters may be used to increase efficiency of pharmaceutical wastewater treatment and to determine amount of oxygen needed to removal BOD and dissolved oxygen in activated sludge process.

• Microbiology and Biotechnology Letters
• /
• v.30 no.1
• /
• pp.26-32
• /
• 2002

For commercial production of Korean fermented anchovy sauce through rapid fermentation, a bacterial strain which showed the high protease activity was isolated from a commercially fermented anchovy sauce. The isolate was Bacillus amyloliquefaciens, and named as B. amyloliquefaciens HTP-8. The incubation temperature, initial pH, and cultivation time for optimal production of protease by B. amyloliquefaciens HTP-8 were $30^{\circ}C$, 7.0, and 3 days, respectively. In jar fermenter, B. amyloliquefaciens HTP-8 showed higher protease activity when grown at pH 7.0. The protease was partially purified by 80% ammonium sulfate precipitation and CM-Sephadex C-50 ion exchange chromatography. The partially purified enzyme had specific activity of 103.3 units/mg, yield of 0.4%, and purification fold of 43.0. The optimal pH and temperature for the protease activity were 10.0 and $50^{\circ}C$, respectively. The protease was relatively stable at the pH range of 7.0~12.0 and at the temperatures below 4$0^{\circ}C$. The activity of the enzyme was inhibited by $Ag^{＋}$ /, $Ba^{2＋}$ and selectively inhibited by PMSF, suggesting that it is a serine protease.

• Korean Journal of Oriental Medicine
• /
• v.4 no.1 s.4
• /
• pp.115-127
• /
• 1998

To improve the quality control of frequently used oriental medicinal plants, the storage, cutting, processing and decokting methods of Rehmannia glutinosa Libosch. var. purpurea Makino(熟地黃) were examined. The contents of 5-hydroxymethyl-2- furaldehyde(5-HMF) of Rehmannia glutinosa Libosch. var. purpurea Makino were analysed by HPLC at various conditions as the standard component. Raw materials were classified into 3 groups with their specific gravity(天 地 人黃) and determined the ding weights and the contents of water, the solid component of Ji-Hwang(地黃) was the most. Rehmannia glutinosa Libosch. var purpurea Makino was steamed and dried nine times and analysed the content of 5-HMF on every time. In the case of Ji-Hwang, the standard component of the ninth sample was produced the most. But which of the tenth samples of Chun-Hwang and Yin-Hwang(天黃 人黃) were the most. The best decokting conditions which were determined by the yield of 5-HMF were as follows : non cutting, soaking time was 0 minutes, decokting time was 75 minutes after boiling. The contents of sugar on each of samples were determined. The contents of standard component increased by steaming number and the contents of sugar decreased.

• KSBB Journal
• /
• v.10 no.3
• /
• pp.271-282
• /
• 1995

The authentic hGH converted from met-hGH by immobilized ApM was purified by successive chromatographic processes based on the differences in isoelectric points, hydrophobicities and charges. The final recovery yield was about 14.1% and the specific activity of the purified hGH was 2.75IU per mg when assayed by enzyme immunoassay. The purified hGH was verified to be authentic hGH through the analysis of amino acid composition, amino-terminal amino acid sequence, carboxy-terminal amino acid and tryptic peptide map. The purity of purified hGH was higher than that of commercial hGH when assessed by SDS-PAGE, PAGE, IEF and HSGF. In weight-gain assay and tibia test with hypophysectomized rats, the hGH produced in this study showed the same growth effect as the commercial hGH.

• Journal of Korean Society of Environmental Engineers
• /
• v.29 no.5
• /
• pp.515-520
• /
• 2007

Recently, the treat of sludge is usually progressed by ocean disposal. But it will be totally banned by content of its heavy metal according to London Dumping Convention, gradually. The stable way of treat of sewage sludge should be examined urgently. To solve the problem, recently, there are efficient and environment-oriented method. One of them is to produce absorbent through the activation. This study produces absorbent through steam activation. As basic experiment, optimum activation condition for preparation of good absorbent is researched through study of the fellowing variables : steam flow rate, activated temperature, activation time. As the result of this with standard on iodine adsorptivity, it is chosen, that steam flow rate "30 mL/hr", activation temperature $"500^{\circ}C"$, activation time "60 minutes". At the time, iodine adsorptivity and yield shown that 228.4 mg/g, 77.23%. And also, by using nitrogen adsorption, SEM and EDS are confirmed that pore development, specific surface area, mean pore size, chemical component and content. Pore developed by steam activation is also confirmed that it is micropore.

• Environmental Engineering Research
• /
• v.19 no.3
• /
• pp.283-287
• /
• 2014

Cultivation of microalgae using wastewater exhibits several advantages such as nutrient removal and the production of high valuable products such as lipid and pigments. With this study, two types of wastewater from instant noodle factory; mixed liquor suspended solids (MLSS) and effluents after sedimentation tank were investigated for green microalga Scenedesmus sp. cultivation under laboratory condition. Optimal wastewater dilution percentage was evaluated in 24 wells microplate. MLSS and effluent without dilution showed the highest specific growth rate (${\mu}$) of $1.63{\pm}0.11day^{-1}$ and $1.57{\pm}0.16day^{-1}$, respectively, in which they were significantly (p < 0.05) higher than Scenedesmus sp. grown in BG11 medium ($1.08{\pm}0.14day^{-1}$). Ten days experiment was also conducted using 2000 ml Duran bottle as culture vessel under continuous light at approximately 5000 lux intensity and continuous aeration. It was found that maximum biomass density of microalgae cultivated in MLSS and effluent were $344.16{\pm}105.60mg/L$ and $512.89{\pm}86.93mg/L$ respectively and there was no significant (p < 0.05) difference on growth to control (BG11 medium). Moreover, cultivation microalgae in wastewater could reduce COD in wastewater by 39.89%-73.37%. Therefore, cultivation of Scenedesmus sp. in wastewater from instant noodle factory can yield microalgae biomass production and wastewater reclamation using photobioreactor simultaneously.

• Applied Biological Chemistry
• /
• v.32 no.3
• /
• pp.309-314
• /
• 1989

The cultural condition of Enterobacter agglomerans U-1, a polysaccharide producing soil bacterium, was examined. The optimal medium composition was that contains the following components per liter of distilled water; $sucrose(23.75\;g/L),\;peptone(2.06\;g/L),\;yeast\;extract(0.5\;g/L),\;KH_2PO_4(1.0\;g/L)$ and $MgSO_4{\cdot}7H_2O(1.0 g/L)$. The optimum temperature for polysaccharide production was $30^{\circ}C$, where 8.5 g/L of polysaccharide was produced. The apparent viscosity of fermentation broth after 3 days was 240 mPa.s. at $70sec^{-1}$. The product yield and specific productivity were 36% and 142.07 mg/g/h.

• Microbiology and Biotechnology Letters
• /
• v.16 no.4
• /
• pp.282-286
• /
• 1988

Growth kinetic parameters for mass cultivation of Chinese Hamster Ovary (CHO) cells are estimated by measuring oxygen uptake rates. It Is found that there is strong correlation between cell growth and oxygen consumption, showing that correlation factor is 0.83. Derived linear model predicts actual cell density very well. It tells that oxygen uptake rate can play important role in indirectly measuring cell density when conventional method of estimating cell density is no longer meaningful due to heavy cell clumpings. Cell yield per oxygen consumption, $Y_{\chi}o$ and mass transfer coefficient for oxygen, Ka are also estimated as 1.26$\times$10$^4$cells/mmole $O_2$ consumed and 1.01/h, respectively. Average specific growth rate over all runs is 2.891/day for CHO cells with producting 2 grams of tPA per day under continuous perfusion operations.

• Journal of the Korean Institute of Gas
• /
• v.13 no.6
• /
• pp.44-48
• /
• 2009

In this paper, two different types of natural gas liquefaction cycle with 2 staged compression were designed and simulated to develop liquefaction process which is the core technology in the Industry of natural gas liquefaction plant. These include the cascade cycle with inter-cooler which is consisted of propane, ethylene and methane cycle. One of these is that liquid-gas heat exchanger is applied to between methane and ethylene cycles, and another is that liquid-gas heat exchanger is added to between ethylene and propane on the above process. Also, these cycles are compared with two staged cascade process using an inter-cooler. The COP of process2 is shown about 14.0% higher than that of process1, respectively. Also, the yield efficiency of LNG improved comparing with process1 with 11.5% lower specific power.