• Proceedings of the Korean Vacuum Society Conference
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• 1999.07a
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• pp.112-112
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• 1999

고분자 표면에 MeV급 이온을 주입하게 되면 화학적, 광학적, 물리적, 전기적 특성 등 기존의 재래식 공정으로는 불가능한 다양한 특성변화가 일어나게 된다. 본 실험에서는 이온 조사에 따른 micro-hardness의 변화에 중점을 두어 관찰하였다. 수 MeV로 가속시킨 Cl과 C 이온을 Kapton, Teflon, PMMA에 조사량을 바꾸어가며 조사하였다. 이때 조사 전후 고분자 시료의 표면 경도는 depth-sensing nanoindentation technique (Nano Indenter II, USA)을 이용하여 측정하였다. 측정깊이는 극표면 효과와 기측효과의 영향을 무시할 수 없는 100nm로 결정하였다. 또한 이와 같은 경도변화를 규명하기 위하여 각각의 시료에 대해 FTIR, Raman, UV-VIS, RBS, XPS 스펙트럼을 측정하였으며, 조사중에 발생되는 가스상 분자들을 RGA를 이용하여 측정하였다. 1 MeV Cl 이온을 Kato에 4x1015ions/cm2 조사하면 경도가 0.35 GPa에서 7.1GPa로 약 20배 정도 증가하게 되며, 이 경도는 stainless steel 경도 2~3 GPa, martensite steel 8~12와 비교하여 보면 상당히 높은 수준임을 알 수 있다. Teflon과 PMMA 시료의 경우 1MeV Cl 이온 4X1015ions/cm2를 조사시키면 각각 경도가 0.31GPa에서 4.1a, 0.30 GPa에서 3.9GPa로 변화하였으며 Kapton에 비하여 상대적으로 경도의 변화가 적음을 알 수 있었다. 이온 주입된 Kapton의 경우 FT-IR측정에 의하여 이온 조사량이 증가함에 따라 C=O 진동, 이미드그룹의 CONH, tertiary amine의 C-N 흡수 피크가 감소되며, 1X1014ions/cm2 이상의 양이 조사되어야 개질변화가 일어남을 알 수 있었다. XPS 측정 결과 Kapton에 조사되는 이온양이 증가할수록 C=O, C-O 및 C-N의 탄소는 감소하고 페닐고리 탄소가 증가함을 알 수 있었다. 또한 이온 조사 중 측정한 RGA에서도 CO 가스가 대량 방출되는 현상을 관찰하였으며 FTIR 및 XPS에서의 C=O 결합의 감소와도 일치하였다. RBS에 의한 CNO 원소의 변화에서도 다른 원소보다 O의 감소가 현저하게 나타남을 확인하였다. UV-VIS 측정을 통해 조사 이온량에 따라 에너지 준위가 변동하여 흡수스펙트럼이 장파장으로 확대됨을 알 수 있었으며, 이는 공액 2중 결합의 형성에 의한 $\pi$-전자 및 기타 결함에 기인한다. PMMA 및 Teflon의 경우 FTIR 측정에 의하여 이온 조사됨에 따라 function group 들의 peak가 세기가 감소되면서 완만해지는 경향을 보이며 원래의 구조를 상실하게 된다. PMMA와 Teflon은 이온 조사가 되면 가교형서보다는 사슬절단이 주로 일어나므로 가교형성이 잘 일어나는 Kapton보다는 상대적으로 경도의 증가가 적음을 알 수 있었다.

• Journal of the Korean Institute of Gas
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• v.11 no.4
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• pp.41-46
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• 2007

The residential fuel cell system was modeled as a box-shaped chamber with vent openings, filled with various components such as reformer, desulfurizer, fuel cell stack and humidifier. When the vent openings are 1% of the total surface and hydrogen leakage 1%, hydrogen concentration is around 0.1% higher than the other regions from leak points in the chamber at 30 seconds and hydrogen concentration is increased from 0.3% to 0.7% in the upper region of the system after 200 seconds. When the vent openings are 1% of the total surface and hydrogen leakage 1%, 3%, 5%, the steady state result of CFD, 5% of hydrogen leakage is reached the lowest ignition limit in the system. When the vent openings are 2% of the total surface and hydrogen leakage 1%, hydrogen concentration is increased in the bottom of the system for 60 seconds. After 250 seconds, hydrogen concentration is reached the steady state in the system. As the vent opening of the total surface increased from 1% to 2%, averaged hydrogen mole fraction is under 1% in the system, however, upper regions of the system from the hydrogen leakage points are shown over 1% of hydrogen mole fraction.

• International Journal of Highway Engineering
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• v.13 no.2
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• pp.41-48
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• 2011

Warm-mix asphalt(WMA) technology has been developed to allow asphalt mixtures to be produced and compacted at a significantly lower temperature. The WMA technology was identified as one of means to lower emissions for $CO_2$ and has been spread so quickly in the world. Recently, two innovative WMA additives has been developed to reduce mixing and paving temperatures applied in asphalt paving process in Korea. Since the first public demonstration project in 2008, many WMA projects have successfully been constructed in national highways. In 2010, the WMA field trial was conducted on new national highway construction under Dae-Jeon Regional Construction Management Administration. The two different WMA loose mixtures(WMA and WMA-P) and a HMA mixture were collected at the asphalt plant to evaluate their mechanical performance in the laboratory. The Third-scale Model Mobile Loading Simulator(MMLS3) was adopted to evaluate rutting resistance and moisture damage under different traffic and environmental conditions. In this study, plant-produced WMA mixtures using two WMA additives along with the conventional hot mix asphalt(HMA) mixtures were evaluated with respect to their rutting resistance and moisture susceptibility using MMLS3. Based on the limited laboratory test results, plant-produced WMA mixtures are superior to HMA mixtures in rutting resistance and the moisture susceptibility. The WMA additive was effective for producing and compacting the mixture at $30^{\circ}C$ lower than the temperature for the HMA mixture.

• Proceedings of the Korean Vacuum Society Conference
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• 1999.07a
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• pp.201-201
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• 1999

소수성의 특성을 가지는^g , pp (polypropylene)의 표면을 이온 보조 반응법(IAR)으로 처리하여 친수성으로 개질하였다. 이온빔 보조 반응법은 고에너지 이온빔을 이용한 기존의 표면처리 방식과는 달리 1keV 영역의 에너지를 가진 이온빔을 조사하면서 시료 주위에 반응성 가스를 불어넣어 줌으로써 표면의 성질을 변화시키는 방법이다. 여기서 조사된 수소이온의 에너지는 0.6에서 1.0keV까지 변화시키고 시료의 주변에 불어주는 산소의 양은 0에서 8ml/min으로 변화시켰으며 이온 조사량은 5x1014에서 1x1017ions/$\textrm{cm}^2$까지 변화시켰다. 그 결과 처리하지 않은 시료의 접촉각은 93$^{\circ}$이었으며 이온조사량이 1x1017ions/$\textrm{cm}^2$이고 가속에너지가 1.0keV인 조건에서 수소 이온빔만으로 처리한 시편의 경우 접촉각은 60$^{\circ}$정도 였으나 수소이온보조 반응법으로 처리한 시편의 경우는 $10^{\circ}$이하까지 접촉각이 감소하였음을 알 수 있었다. 이는 표면처리에 따른 표면의 친수성 작용기의 형성을 예상할 수 있으며 그 존잴르 확인하기 위하여 대기중과 물속에서 각각 보관한 시료의 접촉각과 표면에너지를 계산하여보았다. 그 결과 대기중에서 방치한 시편의 경우40$^{\circ}$ 정도로 감소하였으나 증류수에 보관한 시료의 경우는 15$^{\circ}$정도의 변화를 보였다. 물과 Formamide의 접촉각의 측정으로 표면에너지를 계산한 결과 산소분위기에서 수소이온빔으로 처리된 시료는 23dyne/cm에서 64dyne/cm이상까지 변화함을 관찰하였다. 위의 결과들이 표면거칠기에 미치는 영향을 고찰하기 위해 처리되지 않은^g , pp 의 근(root mean square)값은 8.30nm이었고 1kevdpsj지에서 불어준 산소4ml/min이고 이온 조사량이 1x1017ions/$\textrm{cm}^2$인 경우 접촉각은 $10^{\circ}$를 나타냈으며 rms값은 20.8nm를 나타내었다. XPS (X-ray photoelectron spectroscopy) 분석을 통하여 1x1017ions/$\textrm{cm}^2$에서 산소기체를 4ml/min 불어넣어준 후 C-O, C=O, (C=O)-O등의 친수성 작용기가 형성되었음을 확인하였다.^g , pp 의 접착력을 알아보기 위해 유성 페인트를 전도성 고분자위에 후막 처리하였다. 스카치 테이프를 테스트를 통하여 이온 보조 반응법으로 처리된^g , pp 표면이 처리하지 않은 시편에 비하여 접착력 향상되었음을 확인하였다.

• Applied Chemistry for Engineering
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• v.19 no.5
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• pp.466-470
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• 2008

The objective of this study is to convert methane into hydrogen using a nanoporous catalyst in the $CO_2$ containing syngas generated from the gasified waste. For the purpose, $Ni/Al_2O_3$ catalyst was prepared with the one-pot method. According to analyses of the catalyst, three dimensionally linked sponge shaped particles were created and the prepared nanoporous catalysts had larger surface area and smaller particle size and more uniform pores compared to the sphere shaped commercial catalyst. The catalyst for reforming reaction gave the highest $CH_4$ conversion of 91%, and $CO_2$ conversion of 92% when impregnated with 16 wt% of Ni at the reaction temperature of $750^{\circ}C$. At that time, the prepared catalyst remarkably improved the $CH_4$ and $CO_2$ conversion up to 20% compared to the commercial one.

• Applied Chemistry for Engineering
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• v.21 no.3
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• pp.343-348
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• 2010

The surface of low density polyethylene (LDPE) film was oxyfluorinated under different reaction conditions to introduce hydroperoxide groups and change surface characteristics. Hydroperoxide functional groups created by oxyfluorination were used as active sites for graft polymerization with hydrophobic monomer, acryl amide (AM), and hydrophilic monomer, methyl methacrylate (MMA) to carry out the second modification of the LDPE film surface. The surface properties of the OFPE films and grafted OFPE films were characterized by 1,1-diphenyl-2-picrylhydrazyl (DPPH) radical scavenging method, ATR-IR, contact angle measurement and DSC. From the results of DPPH method, the amount of hydroperoxide groups on the oxyfluorinated LDPE film continuously increased as the total pressure in the oxyfluorination and the partial pressure of fluorine gas increased. The water contact angle and surface free energy measurements showed that hydrophilic liquid (water) contact angle on LDPE film surface decreased with hydrophilic AM grafting and hydrophobic liquid (methylene diiodide) contact angle on LDPE film surface decreased with hydrophobic MMA grafting. These were attributed to AM or MMA monomer grafting and the wettability of LDPE filmsurface to hydrophilic and hydrophobic liquids were improved.

• Journal of Adhesion and Interface
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• v.6 no.3
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• pp.1-9
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• 2005

This study investigated the influence of atmospheric plasma factors such as RF power, treatment time, the gap distance between discharge and sample, and the gas flow rate of Ar on the surface property by using the design of experiment (DOE) method. The plasma treatment time (s), plasma power (W), gap distance (mm) between discharge and sample, and flow rate of Ar gas were in order of important factors for changing the surface free energy of PMMA plates. As a result, the most effective factor for improving the surface free energy of PMMA plates is the distance (mm) from discharge glow to sample plate. Because of the interaction between plasma power (W) and treatment time (s), the power dose (J) factor which multiply plasma power (W) by treatment time (s) should be significantly considered. The optimum condition for maximizing the surface free energy of PMMA plate was found at 1500J of power dose. Through XPS and AFM analysis, we also observed the change of chemical composition, surface morphology and roughness before and after plasma treatment. It is considered that the change of surface free energy of PMMA plate with plasma treatment is influenced by the introduction of polar functional group as well as the increase of surface roughness.

• Korean Chemical Engineering Research
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• v.44 no.2
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• pp.160-165
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• 2006

A Pd-Cu-Ni alloyed hydrogen membrane has fabricated on porous nickel support formed by nickel powder. Porous nickel support made by sintering shows a strong resistance to hydrogen embrittlement and thermal fatigue. Plasma surface modification treatment is introduced as pre-treatment process instead of conventional HCl wet activation. Nickel was electroplated to a thickness of $2{\mu}m$ in order in to fill micropores at the nickel support surface. Palladium and copper were deposited at thicknesses of $4{\mu}m$ and $0.5{\mu}m$, respectively, on the nickel coated support by DC sputtering process. Subsequently, copper reflow at $700^{\circ}C$ was performed for an hour in $H_2$ ambient. And, as a result PdCu-Ni composite membrane has a pinhole-free and extremely dense microstructure, having a good adhesion to the porous nickel support and infinite hydrogen selectivity in $H_2/N_2$ mixtures.

• Applied Chemistry for Engineering
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• v.33 no.6
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• pp.624-629
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• 2022

Formaldehyde is an indoor pollutant that is harmful to humans, such as causing respiratory and skin diseases. Nitrogen plasma treatment was performed to introduce nitrogen groups on the surface of the activated carbon fibers (ACFs), and the adsorption characteristics of formaldehyde for the surface-modified ACFs were considered. As the nitrogen gas flow rate increased, the content of nitrogen functional groups introduced to the surface of the ACFs increased by about 7%, and the ratio of nitrogen functional groups to each type present was similar. Ultramicropores increased on the ACFs surface due to the etching effect of plasma treatment. The adsorption efficiency of formaldehyde on the modified ACFs surface was also enhanced. However, under the nitrogen flow rate of 120 sccm or more, the surface of the ACFs was excessively etched, and the specific surface area and the formaldehyde adsorption capacity decreased. Therefore, the content of the nitrogen groups is the main factor in the adsorption of formaldehyde on the nitrogen plasma-treated ACFs, but it can be found that the adsorption efficiency of formaldehyde is improved when the ACFs have a suitable pore structure.

• The Journal of the Institute of Internet, Broadcasting and Communication
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• v.22 no.1
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• pp.135-140
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• 2022

In addition to the stack that directly generates electricity by the reaction of hydrogen and oxygen, the fuel cell power generation system has a reformer that generates hydrogen from various fuels such as methanol and natural gas. It also consists of a power converter that converts the DC voltage generated in the stack into a stable AC voltage. The fuel cell output of such a system is direct current, and in order to be used at home, an inverter device that converts it into alternating current through a power converter is required. In addition, a DC-DC step-up converter is used to boost the fuel cell voltage to about 30~70V, which is the inverter operating voltage, to about 380V. The DC-DC step-up converter is a DC voltage variable device that exists between the fuel cell output and the inverter. Accordingly, since a constant output voltage of the converter is generated in response to a change in the output voltage of the fuel cell, the inverter can receive constant power regardless of the voltage change of the fuel cell. Therefore, in this paper, we discuss the detailed hardware design of the full-bridge converter, which is the main power source of the inverter that receives the fuel cell output voltage (30~70V) as an input and is applied to the grid among the members of the fuel cell power generation system.