• Korean Journal of Fisheries and Aquatic Sciences
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• v.28 no.5
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• pp.599-606
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• 1995

The feasibility of foam separation to remove protein produced from fish culture water was investigated, By assuming foam separation column as a single well-mixed pool, a simplified model for foam separator conditions was alse studied under the batch operation. The model indicated that the protein removal could be described as a first-order reaction whose rate increases with both superficial air velocity and protein concentration in the bulk solution. from ,the results of an experimental study on the effects of superficial air velocity, the protein concentration, temperature, and pH on protein removal, the superficial air velocity and initial protein concentration in bulk solution were found to be important operational factors. Other experimental results important that foam separator operated under batch conditions would be considered as a completely mixed reactor. The protein removal rate by foam separation process was increased proportionally with the superficial air velocity, and the adsorptive removal rate of protein was found to obey Langmuir adsorption formula. The preposed simplified model was verified with the experimental data obtained from this study. Under the experimental range used, both temperature and pH did not affect the protein removal.

• Journal of Korean Society of Environmental Engineers
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• v.36 no.2
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• pp.147-152
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• 2014

In this research, polysulfone hollow fiber membrane was used to recover $CO_2$ which is one of greenhouse gases from flue gas stream being emitted after the combustion of fossil fuels. The prerequisite requirement is to design the membrane process producing high-purity $CO_2$ from flue gas. For separation of $CO_2$, a membrane module and flue gas containing 10% carbon dioxide was used. The effects of operating conditions such as pressure, temperature, feed gas composition and multi-stage membrane on separation performance were examined at various stage cuts. Higher operating pressure and temperature increased carbon dioxide concentration and recovery ratio in permeate. Recovery ratio and separation efficiency increased if a higher content of $CO_2$ injection gas composition. Three-stage membrane system was producing a 95% $CO_2$ with 90% recovery from flue gas. The separation efficiency of three-stage membrane system was higher than one-stage system.

• Proceedings of the Korean Vacuum Society Conference
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• 2011.02a
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• pp.196-196
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• 2011

팔라듐-구리 합금 분리막은 세륨산화물로 전처리된 다공성 니켈 지지체 위에 마그네트론 스퍼터 공정과 구리리플로우 공정에 의해 제조되었다. 스퍼터 공정은 얇고 치밀한 팔라듐 합금 분리막 증착을 위해 아주 효과적이다. 본 연구에서는 고온 스퍼터 공정에 의해 증착된 팔라듐 상부에 유동성과 열적확산이 우수한 구리를 코팅한 후, 반도체 분야에서 기가 패턴 매립시 사용하는 구리리플로우 공정을 도입하였다. 구리리플로우 공정은 치밀하고 미세기공이 존재하지 않는 표면을 구현하고 무한대의 수소 투과도를 가능하게 한다. 이로써 마그네트론 스퍼터에 의해 $200^{\circ}C$에서 팔라듐과 구리를 순차적으로 코팅한 후, $700^{\circ}C$에서 2시간 구리리플로우 공정을 실시하여 $7.5{\mu}m$ 두께의 팔라듐-구리 합금 분리막이 제조되었다. 세륨산화물(CeO2)은 고온에서 장시간 운전하는 동안 다공성 니켈 지지체의 금속성분이 팔라듐 합금층으로 확산하는 금속의 확산 문제를 개선하고자 지지체와 코팅층 사이에 확산방지막으로 도입되었으며, 균일한 스퍼터 증착을 위해 평탄한 표면의 지지체를 구현하였다. 투과도 테스트는 100-400kPa 의 압력차, 673-773K 의 온도 조건에서 순수한 수소가스로 실시하였다. 표면 미세기공이 없는 치밀한 팔라듐-구리 합금 분리막은 혼합가스에서 질소의 투과 없이 수소만을 투과하는 무한대의 우수한 분리도를 나타내었으며, 상용온도 $500^{\circ}C$에서 12.6ml/$cm^2{\cdot}min{\cdot}atm$의 수소 투과 능력을 보였다. 본 연구에 의해 제조된 팔라듐-구리 합금 분리막은 표면 미세기공이 없는 치밀한 분리막 제조를 가능하게 하였으며 열팽창계수가 팔라듐과 매우 비슷한 세륨산화물($CeO_2$)로 인해 지지체층과 코팅층과의 접합력이 향상되고 수소취성에 강하고 높은 열적 안정성을 갖는다.

• KSBB Journal
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• v.14 no.1
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• pp.17-23
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• 1999

Studies were carried out to elucidate the effects of pressure, temperature and mobile phase composition on supercritical $CO_2$ chromatographic separations of paclitaxel, baccatin III, 10-deacetyl baccatin III, 7-epi-10-deacetyltaxol, cephalomanine, and 10-deacetyltaxol. High resolutions of paclitaxel, 10-deacetylbaccatin III, 10-deacetyltaxol were observed with optimized pressure, temperature, and mobile phase composition. The highest resolution between paclitaxel and 10-deacetylbaccain III was observed at 275 kg/$\textrm{cm}^2$, $40^{\circ}C$ with the mobile phase composition of gradient mixture of 3.9-3.6 mL/min $CO_2$, 0.1-0.4 mL/min methanol for 20 min. Resolutions of baccatin III, capalomannine, and 7-epi-10-deacetyltaxol were found to be low in this study. On-line coupled SFE/SFC process was applied to isolate paclitaxel from yew tree powder. As a consequence, paclitaxel with a purity of 95% was obtained with a recovery yield of 38%.

• Membrane Journal
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• v.1 no.1
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• pp.34-43
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• 1991

The relationships between affinity of membranes and optimum operation conditions were investigated in the pervaporation of water(1)/ethanol(2) mixture through cellulose acetate(CA) membranes having more affinity to water and silicone rubber(SR) membranes having more affinity to ethanol. CA and SR membranes were prepared and amount of sorption, sorption selectivity, pervaporation separation factor and pervaporation rate in both of membranes were determined and compared. The effects of downstream pressure were analyzed using Thompson diagram and the sorption and pervaporation characteristics with composition of feed and operation temperature were examined in terms of affinity, activity coefficient, plasticizing effect and activation energy of individual species. In the separation of water through CA membranes, high performance of both pervaporation separation factor (water to ethanol, $[\alpha^2_1]_{PV}$) and pervaporation rate was obtained in the conditions of low downstream pressure, middle range of feed concentration and high temperature. In the separation of ethanol through SR membranes, pervaporation separation factor(ethanol to water, $[\alpha^2_1]_{PV}$) increased with downstream pressure and decreased with concentration of ethanol in feed and operation temperature, while pervaporation rate showed opposite trends to those of ($[\alpha^2_1]_{PV}$).

• Korean Chemical Engineering Research
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• v.48 no.4
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• pp.515-518
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• 2010

D,L-tryptophans were separated by using $Chirobiotic^{(R)}$ T HPLC column. Mobile phases were the mixture of methanol and water(70:30, 80:20, 90:10, v/v). Experimental temperatures were adjusted as 25, 40 and $55^{\circ}C$ in order to compare retention times. Difference in D,L-tryptophan retention times was studied in terms of the interaction between stationary phase and tryptophans. Selectivity, resolution and efficiency of column were utilized to find an optimum separation condition. Retention times were shortened by increasing the amount of methanol in mobile phase and the temperature of column. The best selectivity and resolution was obtained with the temperature($25^{\circ}C$) and the ratio of mobilephase(70/30 v/v%).

• Korean Journal of Environmental Biology
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• v.17 no.2
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• pp.209-215
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• 1999

Changes of malate dehydrogenase isozyme in oyster exposed to different temperature, pH and salinity were investigated by polyacrylamide gel electrophoresis. MDH isozyme in control group was separated into two bands on the positive side. In case of temperature and pH stress, MDH isozyme was separated into only one band after 12 hours exposure but two bands after 24, 48 hours exposure on the positive side. In case of salinity stress, after 12 hours exposure, MDH isozyme bands were separated into two bands in 5 ppt, 30 ppt and three bands in 10 ppt, 40 ppt concentration on the positive side. After 24 hours and 48 hours exposure case in salinity stress, MDH isozyme bands was separated into two bands on the positive side in all concentration. Activities of isozyme bands show their characteristics according to the condition of experiment. In conclusion, changes of MDH isozyme was a biochemical defense mechanism in oyster and result from effect of environmental stress to oyster.

• Journal of Navigation and Port Research
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• v.37 no.2
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• pp.129-135
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• 2013

Recently, waste water treatment system is developed in small and middle size to get more economic advantage. Freeze concentration system has high thermodynamic efficiency and low energy consumption, can re-use purified water and cold energy obtained from ice. This study was experimentally performed to investigate pollution containment in frozen layer by cooling wall temperature, air-bubble flow methods, initial ice-lining thickness of frozen layer in NaCl aqueous solution and the representative heavy metals, Pb and Cr aqueous solution. As the result, a decrease in the cooling wall temperature bring a higher growth rate of ice front and the more solute was involved in frozen layer. The method to inject directly air-bubble into ice-liquid interface through ring shape nozzle gave high purity of ice compared to indirect method. Ice lining in 5mm thickness resulted in frozen layer with higher purity than 1mm thickness.

• Proceedings of the Membrane Society of Korea Conference
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• 1994.03a
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• pp.53-77
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• 1994

기체 분리 방법의 종류 일반적으로 기체를 분리하는 방법에는 다음과 같이 3가지 종류가 있다. Cryogenic Separation (심냉분리법) : 기체를 압축, 냉각, 액화 시킨후 boiling point 차이를 이용한 증류볍으로 분리하는 방법을 말하며 기체 분리 기술중 가장 오래된 기술이다. Adsorption (흡착법) - PSA : 분리 하고자 하는 기체를 흡착제에 흡착 시키고 흡착되지 않는 잔류 기체는 다른 용리에 이송한 후 흡착된 기체를 온도차, 압력차 등을 이용하여 탈착 시키면서 기체를 분리하는 방법이다. Membrane Separation (막분리법) : 특수하게 제작된 막의 한쪽면으로기체 (여러 종류의 기체분자로 구성된 혼합기체)가 접촉되어 막 반대면의 압력이 저압 상태로 될때 혼합기체증의 특정기체가 막을 투과하는 현상을 이용하여 분리하는 방법을 말하며 이때에 투과현상은 막과 친화성이 좋은 특정기체분자가 압력차를 Driving Force로 하여 막의 표면에 용해 되고 이어서 막 내부에서 농도구배에 의한 확산이 일어나고 다른면에서 탈착 되어지는 원리이다.

• Transactions of the Korean Society of Automotive Engineers
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• v.18 no.1
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• pp.93-98
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• 2010

An object of this study is to confirm the opening amount of the throttle valve that is begun the temperature separation of vortex tube for various engine speed and load condition in a common rail diesel engine. The vortex tube located at downstream of the exhaust manifold is a device separating the incoming exhaust gas to hot and cold stream. To find optimum separation efficiency of vortex tube, the opening amount of throttle valve has been investigated for various engine speed and load conditions. Engine speed was found that the influence of engine speed was dominant compared with that of engine load. As engine speed was increased, the throttle opening amount starting temperature separation was reduced.