• Proceedings of the Korean Vacuum Society Conference
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• 2014.02a
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• pp.216.1-216.1
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• 2014

Closed drift ion source는 그 특성으로 인하여 강판 표면처리, 금속 표면 산화막 형성, 폴리머 혹은 기타 표면 개질 등 다양한 분야에서 사용이 되고 있다. 다양한 환경에서 사용 되는 소스의 특성으로 인하여 각기 다른 공정에 대한 최적의 특성이 요구 되며, 이러한 공정 환경에 맞춘 소스를 설계하기 위해서 ion source내 전극의 구조 및 자기장 세기 등 이온소스의 구조적 특성에 대한 연구가 필요하게 된다. 본 연구에서는 선형 이온소스의 구조 설계를 위한 실험을 소형(이온빔 인출 슬릿 직경: 60 mm) 이온빔 인출 장치를 제작하여 전극 구조에 따른 방전 특성을 우선적으로 평가를 실시하여 소형 이온빔 인출 장치에서 도출된 결과를 바탕으로 0.3 m급 linear closed drift ion source 설계에 대한 변수를 조사 하였다. 실험은 양극-음극(C-A) 간 간격 및 음극 슬릿(C-C) 간격 그리고 자기장 세기 조건에서 방전 전류 및 인출 이온빔 전류량 측정하였으며, 이 결과를 전산모사 결과와 비교 하였다. 방전전압 1~5 kV, 가스유량 10~50 sccm 조건에서 Ar 이온빔 방전 특성을 평가한 결과, 양극-음극(C-A) 간격이 넓을수록, 음극-음극(C-C) 간격이 좁을수록 방전 전류량이 증가함을 확인 하였다. 또한, 공정 가스 압력 및 자기장 세기 변화에 따른 1~5 kV의 방전 전압에 대한 방전 특성의 관찰 결과, 압력 및 자기장 변화에 따라서 방전 전류의 변화를 관찰 할 수 있었으며, 이에 대한 결과를 통하여 이온 소스 구조 내부에서의 방전 영역에 대한 압력과 자기장 세기에 대한 영향을 분석 할 수 있었다.

• Proceedings of the Materials Research Society of Korea Conference
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• 2010.05a
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• pp.30.1-30.1
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• 2010

Hydrogen silsesquioxane (HSQ)는 spin-on glass (SOG)의 일종으로 spin-coating이 가능하며 $400^{\circ}C$ 이상의 고온에서의 어닐링을 통해 silica로 변환되는 물질이다. 이 물질은 가시광선 영역에서 95% 이상의 높은 투과도를 나타내며 산화물로의 변환 공정이 간단하며 표면 개질이 용이하기 때문에 나노 바이오, 반도체, 광전자 소자 등의 다양한 분야로의 적용이 기대되는 물질이다. 최근 나노 기술의 발전에 따라 다양한 나노 구조물을 이용하여 소자들의 효율을 향상시키는 연구가 활발하게 진행되고 있다. 따라서 HSQ를 이용하는 소자의 효율을 높이기 위해서는 쉽고 간단하면서 생산성이 높은 HSQ 나노 구조물 제작 기술에 대한 연구가 필요하다. 현재 개발된 대면적 HSQ 나노 구조물 제작 기술로는 e-beam lithography, x-ray lithography, room temperature nanoimprint lithography 등이 있다. 하지만 이와 같은 나노 패터닝 기술들은 생산성이 낮거나 공정이 복잡한 단점이 있다. 본 연구에서는 poly(dimethylsiloxane) (PDMS) mold를 이용한 직접 printing 기술을 통해 HSQ 나노 구조물을 제작하는 기술을 개발하였다. 이 기술은 대면적에 간단한 기술로 HSQ 나노 패턴을 제작할 수 있으며 master mold의 패턴이 그대로 HSQ layer로 전사되기 때문에 제작이 까다로운 아날로그 패턴도 손쉽게 제작할 수 있는 장점을 가지고 있다. 따라서 이와 같은 HSQ 직접 printing 기술을 이용하여 HSQ 아날로그 나노 패턴을 제작하고 이의 응용기술에 대한 연구를 진행하였다.

• Journal of Korea Technical Association of The Pulp and Paper Industry
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• v.47 no.2
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• pp.42-52
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• 2015

In this study, cellulose nanofibrils (CNF) were modified through carboxymethylation or TEMPO-mediated oxidation and their effects on ionicity and characteristics of sheet, film, and foam were investigated. Carboxymethylation was carried out on pulp fibers as a pre-treatment before preparation of CNF. The gel-like and translucent CNF hydrogel was obtained by grinding of carboxymethylated cellulose fibers. Carboxymethylated CNF film and freeze dried sheet showed higher transparency than that of untreated CNF. The CNF sheet with high strength and the CNF foam without large ice crystals were obtained by using the carboxymethylated CNF. TEMPO-mediated oxidation was carried out as a post-treatment of CNF. The zeta potential and charge demand of TEMPO-oxidized CNF were increased with an increase in oxidation time and addition amount of NaClO. The density of sheet made of TEMPO oxidized CNF was increased with the amount of oxidizing agent. The TEMPO oxidized cellulose nanofiber (TOCN) which was obtained from supernatant after centrifugation could be converted to transparent film.

• 한국신재생에너지학회:학술대회논문집
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• 2008.10a
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• pp.21-24
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• 2008

We have developed a $kW_e$ class liquid fuel based solid oxide fuel cell (SOFC) system. Our final target is to develop the 1 $kW_e$ diesel based SOFC system for residential power generator(RPG). In this study, we present the conceptual design of SOFC system. System is composed of hot-box and cold-box. Planar typed SOFC stack, heat exchanger, combustor for stack tail gas, and fuel processor, such as fuel reformer and desulfurizer, are contained in the hot-box. And several balance of plants(BOP), such as fuel suppliers and controller, are contained in the cold-box. Before the SOFC system fabrication, we have already operated the selfsustaining fuel processor, and heat exchange of all heat-related components is simulated using ASPEN HYSYS, because heat maintenance and management in hot-box are important for stable operation of SOFC system. The self-sustained fuel processor was successfully operated for about 250 hours, and heat exchange is enough to operate the SOFC system.

• Proceedings of the Materials Research Society of Korea Conference
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• 2012.05a
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• pp.93.2-93.2
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• 2012

연료전지는 전기화학반응을 이용한 발전 장치로서 기존 장치에 비하여 발전 효율이 높아 화석연료를 사용하면서 현재 당면 과제인 $CO_2$ 배출량 절감이 가능하고, 환경 보전성이 우수하여 미래의 전원으로 많은 연구개발이 진행되고 있다. 특히 제3세대 연료전지라 불리는 고체산화물 연료전지(Solid Oxide Fuel Cell이하 SOFC)는 고가의 외부 개질 장치 없이도 연료가 갖는 화학에너지를 연소과정 없이, 공기와 $H_2$, CO, $CH_4$와 같은 환원성 가스를 공급받아 $600{\sim}1000^{\circ}C$에서 전기화학적 반응을 통하여 직접 전기를 얻는 방식이며, 낮은 소음과 진동으로 인하여 온 사이트(On-site) 발전이 가능한 장점이 있는 연료전지이다. Decalcomanie는 전사용지에 Screen printing하여 건조 후 coating하는 방법으로 기존의 여러 coating 방법보다 다전지셀 제작이나 Buffer layer의 적용이 용이하고, 소재의 크기나 두께조절이 간편하며, 구성층의 표면조도나 굴곡에 대응이 용이한 방법이다. 새로운 Decalcomanie를 사용하여 평관형 다전지식 SOFC Cell 제작 및 각 Buffer layer에 적용, Screen printing법과 동일한 Cell 제조 후 MPD와 Impedance 분석을 통하여 Support 위에 전사지를 이용, 적층한 Cell의 전기화학적 특성에 관하여 분석하였다.

• Textile Coloration and Finishing
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• v.11 no.4
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• pp.50-56
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• 1999

The adhesive properties of polyester cord in rubber matrix were investigated according to the surface modification. The polyester cord was oxidized in sodium hypochlorite solution, and graft-polymerized with acrylic acid under the irradiation with ultraviolet light, and then coated with resorcinol-formaldehyde latex (RFL). The modified surface was checked with scanning electron microscope. The adhesive properties were measured by the full-Out method, and evaluated with regard to the energy of adhesion and the maximum load. The polyester was not oxidized in sodium hypochlorite solution, so the surface was not able to etch to produce the coarse topology. As the concentration of acrylic acid and the reaction time were increased, the graft yields were also increased. It was considered that the acrylic acid would swell the polyester and diffuse easily to the inner side of substrate. The adhesive properties of polyeser to rubber matrix were affected by the surface condition. Namely, the maximum load was almost same, but the energy of adhesion was rather higher In the polyester grafted with acrylic acid than in control one. We concluded that the flexible aliphatic chains of polyacrylic acid situated in the interface of cord and rubber matrix were distributed well the stress and strain all over the filler resulting the high energy of adhesion.

• Transactions of the Korean hydrogen and new energy society
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• v.18 no.2
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• pp.132-139
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• 2007

Popular techniques for producing synthesis gas by converting methane include steam reforming and catalyst reforming. However, these are high temperature and high pressure processes limited by equipment, cost and difficulty of operation. Low temperature plasma is projected to be a technique that can be used to produce high concentration hydrogen from methane. It is suitable for miniaturization and for application in other technologies. In this research, the effect of changing each of the following variables was studied using an AC Glidarc system that was conceived by the research team: the gas components ratio, the gas flow rate, the catalyst reactor temperature and voltage. Glidarc plasma reformer was consisted of 3 electrodes and an AC power source. And air was added for the partial oxidation reaction of methane. The result showed that as the gas flow rate, the catalyst reactor temperature and the electric power increased, the methane conversion rate and the hydrogen concentration also increased. With $O_2/C$ ratio of 0.45, input flow rate of 4.9 l/min and power supply of 1 kW as the reference condition, the methane conversion rate, the high hydrogen selectivity and the reformer energy density were 69.2%, 36.2% and 35.2% respectively.

• Membrane Journal
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• v.26 no.2
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• pp.87-96
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• 2016

Ceramic materials have attracted increasing attention in the last 10 years because of their high thermal stability and high permeation property compared with polymeric nanofiber membranes. Recently, novel nanofiber ceramic membranes with high porosity and flux have been fabricated from metal oxide nanofibers. To improve the performance of ceramic membranes and reduce their costs, a new ceramic membrane with a selective separation layer made of nanofibers was fabricated by electrospinning process and modification process for filtration system. This review summarizes the research trends for the development of ceramic nanofiber membrane over the past few years.

• Korean Journal of Air-Conditioning and Refrigeration Engineering
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• v.16 no.11
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• pp.1013-1020
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• 2004

The hybrid system of gas turbine and fuel cell is expected to produce electricity more efficiently than conventional methods, especially in small power applications such as distributed generation. The solid oxide fuel cell (SOFC) is currently the most promising fuel cell for the hybrid system. To realize the conceptual advantages resulting from the hybridization of gas turbine and fuel cell, optimized construction of the whole system must be the most important. In this study, parametric design analyses for pressurized GT/SOFC systems have been peformed considering probable practical limiting design factors such as turbine inlet temperature, fuel cell operating temperature, temperature rise in the fuel cell and soon. Analyzed systems include various configurations depending on fuel reforming type and fuel supply method.

• Transactions of the Korean hydrogen and new energy society
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• v.21 no.5
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• pp.405-411
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• 2010

A 5kW class SOFC cogeneration system consisted of a hot box part, a cold BOP (balance of plant) part, and a hot water reservoir. The hot box part contained a stack, a fuel reformer, a catalytic combustor, and heat exchangers. A cold BOP part was composed of blowers, pumps, a water trap, and system control units. A 5kW stack was designed to integrate 2 sub-modules. In this paper, the 5kW class SOFC system was operated using 2 short stacks connected in parallel to test the sub-module and the system. A short stack had 15 cells with $15{\times}15 cm^2$ area. When a natural gas was used, the total power was about 1.38 kW at 120A. Because the sub-modules were connected in parallel and current was loaded using a DC load, voltages of sub-modules were same and the currents were distributed according to the resistance of sub-modules. The voltage of the first stack was 11.46 V at 61A and the voltage of the second stack was 11.49V at 59A.