• Applied Chemistry for Engineering
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• v.18 no.5
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• pp.438-443
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• 2007

Titanium oxide films were deposited by the HCP (hollow cathode plasma) reactor at room temperature. With results of simulation about HCP reactor, the temperature profile is uniform on substrate regardless of the heat generation at cathode. The velocity profile on the surface of substrate is more uniform with increasing the gap between cathode and substrate, and surface roughness was decreased with increasing the gap between cathode and substrate. We could confirm that the composition of oxide increased with RF-power, and the ratio of O to Ti in the films was about 2 : 1 at RF-power of 240 watt and distance between cathode and substrate of 3 cm.

• Proceedings of the Korean Vacuum Society Conference
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• 2009.08a
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• pp.318-318
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• 2009

• Clean Technology
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• v.20 no.4
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• pp.425-432
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• 2014

The effect of two important parameters of a catalytic membrane reactor (CMR), hydrogen selectivity and hydrogen permeance, coupled with an Ar sweep flow and an operating pressure on the performance of a water gas shift reaction in a CMR has been extensively studied using a one-dimensional reactor model and reaction kinetics. As an alternative pre-combustion $CO_2$ capture method, the feasibility of capturing a pressurized and concentrated $CO_2$ in a retentate (a shell side of a CMR) and separating a purified $H_2$ in a permeate (a tube side of a CMR) simultaneously in a CMR was examined and a guideline for a hydrogen permeance, a hydrogen selectivity, an Ar sweep flow rate, and an operating pressure to achieve a simultaneous capture of a concentrate $CO_2$ in a retentate and production of a purified $H_2$ in a permeate is presented. For example, with an operating pressure of 8 atm and Ar sweep gas for rate of $6.7{\times}10^{-4}mols^{-1}$, a concentrated $CO_2$ in a retentate (~90%) and a purified $H_2$ in a permeate (~100%) was simultaneously obtained in a CMR fitted with a membrane with hydrogen permeance of $1{\times}10^{-8}molm^{-2}s^{-1}Pa^{-1}$ and a hydrogen selectivity of 10000.

• Applied Chemistry for Engineering
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• v.25 no.4
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• pp.401-408
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• 2014

In membrane bio-reactor (MBR), the aeration control is one of the important independent variables to decrease fouling and to save energy with shear stress change on the membrane surface. The paper was carried out for numerical simulation of 3-dimensional fluid flow phenomena of the cylindrical bioreactor with submerged flat membranes equipped in the center and supplied the air from the bottom by using the COMSOL program. The viscosity and temperature of solution were assumed to be constant, and the specific air demand based on permeate volume ($SAD_p$) defined as scouring air per permeate rates was used as a variable. The calculated CFD velocities were compared with those of the velocity meter measurement and video image analysis, respectively. The results were good agreement each other within 11% error. For fluid flow in the reactor the liquid velocity increased rapidly between the air diffuser and membrane module, but the velocity decreased during flowing of the membrane module. Also, the velocity increased as it was near from the reactor wall to the central axis. The calculated shear stress on the membrane surface showed the highest value at the center part of the module bottom side and increased as aeration rate increased. Especially, the wall shear stress increased dramatically as the aeration rate increased from 0.15 to 0.25 L/min.

• Applied Biological Chemistry
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• v.37 no.2
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• pp.130-141
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• 1994

A continuous two-stage membrane (1st-SCMR, MWCO 10,000; 2nd-SCMR, MWCO 5,000) reactor was developed and optimized for the production of fish skin gelatin hydrolysate with different molecular size distribution profiles using trypsin and pronase E. The optimum operating conditions in the 1st-step membrane reactor using trypsin were: temperature, $55^{\circ}C$ ; pH 9.0; enzyme concentration, 0.1 mg/ml; flux, 6.14 ml/min; reaction volume, 600 ml; and the ratio of substrate to trypsin, 100 (w/w). After operating for 1 hr under the above conditions, 79% of total amount of initial gelatin was hydrolysed. In the 2nd-step using pronase E under optimum operating conditions[temperature, $50^{\circ}C$ ; pH 8.0; enzyme concentration, 0.3 mg/ml; flux, 6.14 ml/min; reaction volume, 600 ml; and the ratio of substrate to pronase E, 33 (w/w)], the 1st-step hydrolysate was hydrolysed above 80%. Total enzyme leakages in the 1st-step and 2nd-step membrane reactors were about 11.5% at $55^{\circ}C$ for 5hrs and 9.0% at $50^{\circ}C$ for 4 hrs, respectively. However, there was no apparent correlation between enzyme leakage and substrate hydrolysis. The membrane has a significant effect on activity lose of trypsin and pronase E activity for 1 hr of the membrane reactors operation. The loss of initial activity of enzymes were 34% and 18% in the 1st-step and 2nd-step membrane reactor, whereas were 23% and 10% after operating time 3 hr in the 1st-step and 2nd-step membrane reactor lacking the membrane, respectively. The productivities of 1st-step and 2nd-step membrane reactor for 8 times of volume replacement were 334 mg and 250 mg per mg enzyme, respectively.

• Membrane Journal
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• v.4 no.3
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• pp.152-162
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• 1994

The photodegradation efficiency of formic acid on $TiO_2$ photocatalytic membranes was investigated. A new titania membrane reactors for purification of water combining microfiltration with photocatalytic degradation of organic compounds were developed. Titania membrane tubes(average pore size of $0.2\mu m$) were prepared by the slip casting, and porous thin films of $TiO_2$ were formed on the tube surface by the sol-gel process to increase the surface area, and consequently to increase photodegradation efficiency of organic compounds. The UV light with the wavelength of 365 nm was used as a light source for photocatalytic reactions. The photodegradation efficiency of the organic compounds was strongly dependent on the flux of the solution, the microstructure of the membrane (sol pH), and the amount of $O_2$ supplied. The effects of the primary oxidant such as $H_2O_2$ and dopants such as $Nb_2O_5$ on the photodegradation efficiency were also investigated. The results showed that more than 80% of formic acid could be degraded using membrane coated with a $TiO_2$ sol of pH 1.45. The photodegradation efficiency could be improved by about 20% when adding $H_2O_2$ in feed solution or doping $TiO_2$ membranes with $Fe_2O_3$.

• 한국가스학회:학술대회논문집
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• 2003.10a
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• pp.145-148
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• 2003

• Proceedings of the KOR-BRONCHOESO Conference
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• 1991.06a
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• pp.16-16
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• 1991

렉틴(Lectins)은 세포막의 당단백질의 과당류 말단기에 특이적으로 결합하는 비면역성의 당단백질 혹은 단백질을 말하는데 정상세포와 변형된 세포에서 렉틴반응의 차이가 남으로써 요즘에는 렉틴을 병리학적 진단에 이용 가능하게 되었다. “Loss of contact inhibition”은 세포 악성화의 중요한 특징으로 세포의 악성화는 세포막의 구조의 변화와 관계가 있을 것으로 알려져 왔으며 1989년 후두암에서 PNA의 반응이 양성 반응을 나타낸다고 보고되어 저자들은 7가지의 렉틴을 이용하여 후두암전구증의 하나인 후두각화증에서 이형성(Atypia)의 존재유무에 따른 렉틴 반응의 변화를 알아보고자 본 연구를 시행하여 다음과 같은 결과를 얻었다. 1. 이형성이 없는 단순 후두각화증에서는 Con A와 WGA만이 기저세포에 반응이 있었으며, 후두각화증의 가장 중요한 부위인 극세포층에서는 WGA, RCA-I, PNA, SBA, UEA-I, DBA가 세포질에는 반응이 없이 세포간교에만 염색이 되는것을 관찰할 수 있었고 Con A는 반대로 극세포층의 세포질에 반응을 하였으나 세포간교에는 반응이 없었다. 2. 이형성을 동반한 후두각화증에서, 기저세포에서는 반응의 차이가 없었고 극세포층에서는 UEA-I, RCA-I. WGA, PNA, SBA는 세포간교에서 반응이 나타나지 않았고 세포질에서 양성 반응을 관찰 할 수 있었으며 DBA, Con-A에서는 반응의 차이를 관찰 할 수 없었다. 따라서 후두각화증의 극세포층 세포막에서 UEA-I, RCA-I, WGA, PNA, SBA 반응의 소실은 후두암으로의 진행과 밀접한 관계가 있는 이형성의 존재를 암시한다하겠다.

• Proceedings of the Membrane Society of Korea Conference
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• 1996.04a
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• pp.51-52
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• 1996

무기막을 기체 분리 및 분리막 반응기에 적용하려면 특정 기체에 대한 선택도 뿐만 아니라 절대 투과 속도 또한 높아야 한다. 박막 담지 무기막은 다공성 지지체를 사용하여 그위 또는 그 기공 내에 선택적 투과성을 지니는 막을 합성한 형태로서, 되도록 얇은 선택적 투과막을 지지체에 제조함으로써 투과도를 향상시킬 수 있다. 고온에서 수소에 투과성이 있는 실리카막의 경우 기공의 크기기 4nm 정도인 다공성 유리를 지지체로 하여 화학증착법으로 제조하는 연구가 많이 수행되어 왔으며 400$\circ$ 이상의 온도에서 막을 통한 수소의 투과도는 0.1 cm$^3$[STP]/min-atm-cm$^2$ 수준이었다. 본 연구에서는 실리카 담지 무기막의 수소 투과성 향상을 위하여 기공의 크기가 다공성 유리보다 큰 다공성 알루미나를 지지체로 사용하였으며, 이 지지체의 기공 내부에 솔-젤 및 화학증착법에 의하여 실리카 막을 합성하고 고온에서의 기체 투과 특성을 살펴보았다.

• Proceedings of the Membrane Society of Korea Conference
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• 1996.10a
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• pp.55-57
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• 1996

다공성 무기막은 높은투과도와 뛰어난 내열.내화학성, 그리고 경제성 때문에 기존의 PSA공정이나 증류와 같은 고에너지 분리공정을 대체하는 공정으로 각광을 받고 있다. 무기재료막의 제조하는 방법으로 주로 알콕사이드를 사용하는 솔-젤법(1)과 금속(2) 또는 기상반응(3)을 이용하는 화학증착법이 사용된다. 또한 고온에서 수소를 연속적으로 분리하여 화학평형에 기인한 한계를 극복하여 높은 수율을 얻고자하는 막반응기에 관한 연구가 활발히 진행되고 있다. 본 연구에서는 $\alpha$-알루미나 지지체의 미세한 다공성 구조 내부에서 TEOS(Tetraethylorthosilicate)와 산성의 알코올-물 혼합물을 확산시켜 실리카 솔을 생성시킴과 동시에 젤화시켜 기공의 크기를 감소시켜 막을 제조하였다. 이렇게 제조된 막은 높은 투과도와 낮은 수소선택도(selectivity=3-4)를 보였고, 두번째 단계로 silica sol을 제조하여 진공 하에서 dip-coating을 행하였다. 이렇게 2단계로 기공 구조를 개선시킨 실리카 막은 저압에서 상대적으로 높은 수소의 분리도(selectivity=5-7)를 보였으며 여전히 높은 투과도를 갖는다.