• Environmental Mutagens and Carcinogens
• /
• v.26 no.1
• /
• pp.20-24
• /
• 2006

An antimicrobial substance was purified from the giant snail body extract (Achatina fulica) using solid-phase extraction and separation on HPLC reversed-phase chromatography. The primary structure were determined by a combination of an automated amino acid sequence and MALDI-TOF Mass. Its molecular mass was found to be 1392.64 Da. This result was in excellent agrement with the theoretical molecular mass calculated from the amino acid sequence. purified peptide showed antimicrobial activity in vitro against Escherichia coli D31. This result indicate that giant snail whole body was potentially antimicrobial.

• 한국생물공학회:학술대회논문집
• /
• 2001.11a
• /
• pp.705-708
• /
• 2001

Enzymatic synthesis and purification of sugar esters using supercritical $CO_2$ were investigated. The observed yield of suagr ester produced by transesterification of methyl glucoside and oleic acid using a lipase(Novozym 435) was 67% at 24 hours of reaction in the supercritical $CO_2$. The solubility of the fatty acids in the supercritical $CO_2$ was measured to find the conditions of supercritical separation of the fatty acids from the reaction mixture. The solubility of capric and oleic acid was 5 ${\times}$ $10^{-4}$, 1.7 ${\times}$ $10^{-4}$ mol/mol $CO_2$, respectively, varying at $35{\sim}50^{\circ}C$ and 80${\sim}$120 atm.

• Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
• /
• 2008.11a
• /
• pp.360-360
• /
• 2008

Steelmaking industry is widely known to use a lot of water and same amount of wastewater is generated. Although toxicity of wastewater from Steelmaking industry is low, it contains an amount of various organic materials and Fe-Oxides. It is important to recycle the wastewater because of water shortages and water pollution. In general, large-scale equipment is necessary to process the wastewater. On the other hand, superconducting high gradient magnetic separation (HGMS) system can process the wastewater in the small space. Superconducting HGMS system that had a purpose to purify the wastewater was assembled. Cryo-cooled Nb-Ti superconducting magnet was used for magnetic separator. This system can operate continuously because contaminated filters can keep on returning after cleaning. The various magnetic seeding reactions were investigated to increase the reactivity of coagulation. Filter cleaning system was developed to decrease the quantity of clean water. This research was supported by a grant from Korea Electrotechnology Research Institute, Republic of Korea.

• Journal of Life Science
• /
• v.7 no.2
• /
• pp.79-87
• /
• 1997

To determine the cause of Vibrio septicemia by understanding the characteristics endotoxin from Vibrio vulnificus, lethal dose, heat resistance and vascular permeability enhancing activity were svaluated using vegestative cell and cell homogenate and the result is as follows: 1. Vibrio vulnificus CDC B3547 of patient origin did not exihibit any significant difference in toxicity compared to Vibrio vulnificus B57 of enviroment origin. 2. Strong toxicity was observed when viable cell count of Vibrio vulnificus CDC B3547 was more than 10$^{7}$/ml. 3. Toxicity of cell homogenate was completely inactivited upon geating at 80$^{\circ}$C for 20min. 4. Cell homogenate did not show hemolyic activity but was acknowleged to have cytotoxicity. 5. Major lethal toxin against mouse was existed in Vibrio vulnificus CDC B3547; however, separation of LPS and LPS-protein complex was not successful using the current technique.

• Transactions of the Korean hydrogen and new energy society
• /
• v.14 no.1
• /
• pp.81-95
• /
• 2003

본 연구는 압력균등화 공정이 추가된 2 컬럼 6 스뎁의 활성탄 PSA공정을 이용하여 비단열, 비등은 조건에서 메탄(80%)과 수소(20%)의 2성분계로부터 수소분리에 관한 연구이다. 공급가스의 압력, 흡착시간, 공급속도와 P/F 비율이 PSA공정에 미치는 영향에 대하여 평가했고 전산모사를 통해 최적조건을 구했다. 전산모사에 의한 최적 조건은 공급속도 17 LPM, 흡착압력 11 atm, P/F 비율이 0.07~0.1로 나타났으며, 이 조건으로부터 순도 99%, 회수율 85% 이상의 수소가스를 얻을 수 있었다.

• Resources Recycling
• /
• v.21 no.3
• /
• pp.74-83
• /
• 2012

Rare earth metals have been made from rare earth compounds which were prepared from rare earth ore concentrates through successive processes such as leaching(i.e. extraction of rare earth elements to liquid media), separation, purification, precipitation. Here, process for treating monazite and bastnasite ore concentrates were briefly reviewed, and metallothermic reduction and fused salt electrolysis methods were introduced as the extraction technologies for rare earth metals.

• Analytical Science and Technology
• /
• v.16 no.3
• /
• pp.179-184
• /
• 2003

Root bark of Ulmus davidiana Plancn. var. japonica Nakai was extracted by using several solvents with different polarities. Each extract was treated on the MMPs obtained from SK-Hep-1 in order to investigate inhibition effect. Zymography of MMPs showed that MeOH extract has significant inhibition effect. On the GC-MS analysis the highest mass to charge ratio (m/z) of the purified substance was 281. Also, on zymography of MMPs the substance showed 47% inhibition effect at the concentration of $314.7{\mu}g/g$. Cell viability of SK-Hep-1 was 60% at $31.47{\mu}g/g$.

• Mycobiology
• /
• v.51 no.3
• /
• pp.148-156
• /
• 2023

Penicillium oxalicum strain can be isolated from the Bletilla striata (Thunb.) Reichb. f. tubers. Its solid-state fermentation products are concentrated by percolation extraction. Separation and purification have been conducted to the ethyl acetate extracts by preparative HPLC. Based on the use of spectrometry, we have determined 17 known compounds, 12,13-dihydroxy-fumitremorgin C (1), pseurotin A (2), tyrosol (3), cyclo-(L-Pro-L-Val) (4), cis-4-hydroxy-8-O-methylmellein (5), uracil (6), cyclo-(L-Pro-L-Ala) (7), 1,2,3,4-tetrahydro-4-hydroxy-4-quinolin carboxylic acid (8), cyclo-(Gly-L-Pro) (9), 2'-deoxyuridine (10), 1-(b-D-ribofuranosyl)thymine (11), cyclo-(L-Val-Gly) (12), 2'-deoxythymidine (13), cyclo-(Gly-D-Phe) (14), cyclo-L-(4-hydroxyprolinyl)-D-leucine (15), cyclo-(L)-4-hydroxy-Pro-(L)-Phe (16), uridine (17). Here, we report compounds 1-3, 5, 7-8, 11-12, 14-17 are first found and isolated from this endophyte.

• Membrane Journal
• /
• v.27 no.3
• /
• pp.205-215
• /
• 2017

Polymer membranes are cheap and easy in fabrication, and show a high permeability and selectivity, thus play pivotal roles in gas separation as well as water purification. However, polymer membranes typically exhibit the trade-off relation between permeability and selectivity; i.e. when the permeability is high, the selectivity is low and vice versa. Facilitated transport has been considered one of the solutions to address this issue. Over the last decades, facilitated transport concept had played an important role in preparing the membranes and providing ideal and various models for the transport. Understanding the nature of carrier, the mobility of matrix and the physico-chemical properties of polymer composites are crucial for facilitated transport. Depending on the mobility of carrier, facilitated transport membrane is classified into three; mobile carrier membrane, semi-mobile carrier membrane, fixed-site carrier membrane. Also, there are four types of reversible reaction between the carrier and the specific target; proton transfer reaction, nucleophilic addition reaction, p-complexation reaction and electrochemical reaction. The facilitated transport membranes have been applied in the separation of CO2, O2 and olefin (propylene or ethylene). In this review, major challenges surrounding facilitated transport membranes and the strategies to tackle these challenges are given in detail.

• Journal of Animal Science and Technology
• /
• v.47 no.6
• /
• pp.1025-1032
• /
• 2005

This study was carried out to separate ovotransferrin in chicken egg white by gel chromatography and heparin affinity chromatography. In gel filtration which was performed with 50mM Phosphate buffer (pH 7.2, 0.15M salt) at a flow rate of 2.0 ml/min, ovotransferrin and ovalbumin were eluted together in fraction number 11-16. In order to separate pure ovotransferrin, fraction No. 12-14 of them which have high concentration of ovotransferrin were concentrated and rechromatographed. However, the ovotransferrin did not separated clearly. In heparin affinity chromatography, the separation was performed with 50mM ethylaminetetraacetic acid (EDTA, pH7.2) and 50mM Phosphate buffer (pH 7.2, 0.15M salt contained) on ferrous and ferric ion saturated column at as same flow rate as gel filtration system's. Ovotransferrin and albumin were eluted together at 10-15min (fraction No.3) and 15-20min (fraction No.4), respectively. However, purified ovotransferrin was eluted at 156-165min and 165-175min (tube No.32-33) with 50 mM phosphate buffer (pH 7.2, 0.15M salt free), respectively. Heparin affinity chromatography with ferric ion saturated column was resulted in the best separation of ovotransferrin rather than separation by gel chromatography and ferrous ion saturated heparin affinity chromatography.