• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2006년도 추계학술대회
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• pp.443-446
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• 2006

Carbon-supported Platinum (Pt) is the potential electro-catalyst material for anodic and cathodic reactions in fuel cell. Catalytic activity of the metal strongly depends on the particle shape, size and distribution of the metal in the porous supportive network. Conventional preparation techniques based on wet impregnation and chemical reduction of the metal precursors often do not provide adequate control of particle size and shape. We have proposed a novel route for preparing nano sized Pt colloidal particles in solution by oxidation of ethylene glycol. These Pt nano particles were deposited on large surface area carbon support. The process of nano Pt colloid formation involves the oxidation of solvent ethylene glycol to mainly glycolic acid and the presence of its anion glycolate depends on the solution pH. In the process of colloidal Pt formation glycolate actsas stabilizer for the Pt colloidal particle and prevents the agglomeration of colloidal Pt particles. These mono disperse Pt particles in carbon support are found uniformly distributed in nearly spherical shape and the size distribution was narrow for both supported and unsupported metals. The average diameter of the Pt nano particle was controlled in the range off to 3 nm by optimizing reaction parameters. Transmission electron microscopy, CV and RRDE experiments were used to compliment the results.

• 멤브레인
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• 제6권2호
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• pp.109-116
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• 1996

본 연구는 흡착과 막분리를 결합시킨 혼성 시스템을 폐수처리에 응용하기 위한 기초 연구로서, 페놀을 분말활성탄에 의해 흡착하고, 흡착된 페놀을 활성탄과 함께 정밀여과에 의해 분리하였다. 분말활성탄의 입자크기가 클수록 여과저항은 감소하였으며, 활성탄의 양이 적을수록 단절점(break point) 이전의 투과농도 변화율과 페놀 부하 변화율은 증가하였다. 분말활성탄의 입자크기가 작을수록 활성탄의 외표면적과 경막물질전달계수의 증가로 인해 단절점 전의 투과농도는 감소하였다.

• Journal of the Korean Wood Science and Technology
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• 제50권4호
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• pp.256-271
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• 2022

Activated carbon (AC) derived from coconut shells (CS-AC) was obtained through pyrolysis at 700℃ and subsequently activated with H₃PO₄. AC was ground in a Wiley mill several times to form powder particles at particle scales of 80, 100, and 200 meshes. The characterization of the AC was studied using scanning electron microscopy (SEM), X-ray diffraction analysis (XRD), Fourier-transform infrared spectroscopy (FT-IR), and surface area analysis (S_BET). The CS-AC-200 mesh resulted in a higher percentage of mesopores and surface area. This particle size had a larger surface area with angular, irregular, and crushed shapes in the SEM view. The smaller particles had smoother surfaces, less wear, and increased curing depth and ratio of the hardness of the resin composite. Based on the characterization results of the AC, it is evident that CS-AC with a 200 mesh particle size has the potential to be used as a filler in biocomposites.

• Journal of Korean Society for Atmospheric Environment
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• 제20권E2호
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• pp.53-59
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• 2004

The roadway tunnels in urban areas give rise to problems such as a localized air pollution. Here, we report the results of a case study of an urban roadway tunnel measurement. The size-resolved particle sampling was carried out with a two 2-stage filter pack samplers and an Andersen impactor sampler at the center of Buk-Ak tunnel in November 2001. Particle Induced X-ray Emission (PIXE) was applied to determine the elemental composition of size-resolved particles divided into soluble and insoluble fractions. The Thermal/Optical Reflectance (TOR$^{(R)}$) method was also employed in analyzing of elemental carbon (EC) and organic carbon (OC). Mass concentrations of fine (< 1.2 ${\mu}{\textrm}{m}$) and coarse (> 1.2 ${\mu}{\textrm}{m}$) particles are 165 and 48 $\mu\textrm{g}$ m$^{-3}$ , respectively. Total elemental mass concentration (the sum of insoluble coarse, soluble coarse, insoluble fine, and soluble fine) is found to be 24$\mu\textrm{g}$ m$^{-3}$ and comprises only 11 % of total particle mass concentration. The concentrations of EC, OC, and mass show the clear dependency on particle size with the maximum between 0.1 and 0.43 ${\mu}{\textrm}{m}$ aerodynamic diameters. Total carbon (sum of EC and OC) accounts for approximately 70% of mass concentration.n.

• Elastomers and Composites
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• 제44권1호
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• pp.47-54
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• 2009

본 연구에서는 다양한 종류의 보강제를 혼합한 EPDM 컴파운드의 원적외선에 의한 가교 반응을 조사하였다. 보강제가 원적외선에 의한 가교 반응에 미치는 영향을 평가하기 위하여 컴파운드의 발열 온도 및 DSC 분석에 의한 가교도를 측정하였으며, 특히 원적외선에 의한 가교 특성을 비교하기 위하여 동일 조건에서 열풍에 의한 가교 반응을 조사하였다. 원적외선 가교 조건에서 카본블랙을 혼합한 EPDM 컴파운드는 입자크기가 증가함에 따라 열전도도가 증가하며 이에 따라 원적외선에 의한 가교도 역시 증가하였으나, 열풍에 의한 가교도의 변화에는 거의 영향을 주지 못하였다. 보강제 종류에 따른 원적외선 가교 특성 평가 결과, 열전도도가 높은 아세틸렌 블랙을 함유한 컴파운드의 가교도가 가장 높게 나타났으며, 열전도도가 유사한 카본블랙 및 침강실리카의 경우 상대적으로 원적외선 흡수 특성이 우수한 침강실리카 배합 컴파운드의 경우 원적외선에 의한 가교도가 높게 나타났다.

• Carbon letters
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• 제4권3호
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• pp.121-125
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• 2003

The Pt-Ru/Carbon as an anode catalyst supported on the commercial activated carbon (AC) having high surface area and micropore was characterized for application of Direct Methanol Fuel Cell (DMFC). The Pt-Ru/AC anode catalyst used in this experiment showed the performance of $600\;mA/cm^2$ current density at 0.3 V. The borohydride reduction process using $NaBH_4$, denoted as a process A, showed much higher current and power densities than process B prepared by changing the reduction and washing process of process A. The particle sizes are strongly affected by the reduction process than the specific surface area of raw active carbon and the sizes are almost constant when the specific surface area of carbon are over than the $1200\;m^2/g$. Smaller particle size of catalyst and more narrow intercrystalite distance increased the performance of DMFC.

• Elastomers and Composites
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• 제41권3호
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• pp.194-204
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• 2006

본 연구에서는 카본블랙 충전제의 입자크기 및 구조에 따른 고무 배합물의 마찰 마모 특성을 고찰하였다. 카본블랙의 입자크기와 구조에 따라 마모속도 및 형상이 다르게 되며, 최적 마모성능을 설계하기 위해서는 충전제의 입자크기와 구조의 마모 영향도를 사용조건에 따라 고려하여야 한다. 충전제의 입자크기와 구조에 따른 마모속도($W_R$) 영향도를 수준별로 고찰하기 위해 본 연구에서는 구조와 입자크기가 다른 10가지의 카본블랙을 선택하여 동일한 양을 천연고무와 배합하였다. 자체 제작한 칼날형 마찰 마모 시험기를 이용하여 마찰 마모 특성을 평가하였고, 카본블랙의 입자크기와 구조의 영향을 고려한 특성인자(${\psi}=\sqrt{{N_2^2}+{DBP^2}}$)와의 관계를 고찰하였다. 마모속도($W_R$)와 마찰일($W_f$)의 간에는 power-law 관계가 있었으며, 마모속도는 카본블랙의 특성인자에 역비례 관계를 보였다. 이는 카본블랙의 입자 크기가 작고 구조가 잘 발달 될수록 마모 저항특성은 향상된다는 것을 나타낸다.

• Carbon letters
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• 제4권2호
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• pp.79-85
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• 2003

MCMB (mesocarbon microbeads) has been synthesized from coal tar pitch, petroleum pitch and polymer compound generally. But yield of MCMB was low about 20~40 wt% and was not above 50 wt%. Neither MCMB was replaced with natural graphite because of economic performance, refining MCMB, and control of the particle size distribution. This study was performed to elevate yield of MCMB and to develop technique of particle size distribution. As the result, yield of MCMB that was synthesized from coal tar pitch increased more than 60 wt% about raw material and particle size of MCMB was restrained according to control of QI (quinoline insoluble) ingredient in raw pitch, heat treatment temperature and time.

• Progress in Superconductivity
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• 제5권1호
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• pp.65-69
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• 2003

Many researches on fabrication process for BSCCO precursor powders have been developed for high J$_{c}$ BSCCO-2223 tape. Spray pyrolysis method for fabrication of precursor powder has many advantages, such as high purity, fine particle size and low carbon content of BSCCO precursor powder. Fine, spherical powders were prepared by ultrasonic spray pyrolysis from the aqueous solution of metal nitrates. BSCCO precursor powders were synthesized with various solutes concentration and heat treatment conditions. Average particle size for spray pyrolysis powders was $1.5∼3\mu\textrm{m}$. Bi-2223/Ag tape was prepared by PIT method and followed by various sintering conditions. BSCCO precursor powders were characterized by XRD, SEM, EDS, Carbon content and particle size analysis.s.

• 한국연소학회:학술대회논문집
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• 한국연소학회 2000년도 제21회 KOSCO SYMPOSIUM 논문집
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• pp.236-245
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• 2000

A laboratory scale fluidized bed reactor was developed to treat the combustion characteristics of some fuels (wood, paper sludge, refuse derived fuel). The aims were to introduce the means of experiment and interpretation of the results and finally determine the particle characteristics on the pyrolysis and combustion process of the fuel. A single particle combustion process in the fluidized bed was closely observed. Understanding experimental facility characteristics and determining parameters were also carried out. The fuel combustion processes were observed by carbon conversion rate, recovery and mean carbon conversion time. They were estimated with the CO, $CO_2$ gas concentration monitored at the exit of the combustor. Fuel drying and pyrolysis process were governed by temperature distribution in the fuel particle. There was a significant overlap of the drying and devolatilization. However, transition process from devolatilization to char combustion seemed to be determined by mechanical solidity of the fuel particle after devolatilization process.