• 제목/요약/키워드: Gas Dispersion

검색결과 406건 처리시간 0.025초

Functionalization of Multi-walled Carbon Nanotube by Treatment with Dry Ozone Gas for the Enhanced Dispersion and Adhesion in Polymeric Composites

  • Kim, Jung-Hwan;Min, Byung-Gil
    • Carbon letters
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    • 제11권4호
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    • pp.298-303
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    • 2010
  • A method of functionalization of multi-walled carbon nanotube (MWNT) at room temperature using dry ozone gas is described. The resulting MWNT were characterized by Fourier transform infrared, x-ray photoelectron spectroscopy, and scanning electron microscopy. Combined to these analyses and solubility in liquids, it could be concluded that the dry ozone gas exposure introduces polar functional groups such as carboxylic groups to MWNT similar to acidic modification of MWNT. Particularly, the stable dispersion of MWNT in water after ozone treatment above a critical level could be obtained, implying potential bio-application. The hydrophilic functional groups on the MWNT introduced by ozone oxidation were helpful in improving the interaction with functional groups in PA6 such as $-NH_2$ and -CONH- resulting in improved mechanical properties.

대단면 지하광산 갱도내 뒷채움 작업장 가스유출 및 확산제어 통기방안 연구 (A Study on the Ventilation Schemes for Gas Leakage and Dispersion Controlling at the Backfilled Working Face in Large-Opening Underground Mine)

  • 응우엔반득;이창우
    • 터널과지하공간
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    • 제28권4호
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    • pp.372-386
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    • 2018
  • 뒷채움한 작업장의 공기질은 채움재의 양생기간 및 이후에 걸쳐 현저히 악화된다. 복합탄산염 기반의 채움재로 뒷채움한 채굴적으로부터 장기간에 걸친 NH3 및 CO2의 유출은 작업공간 내부에서 뿐만 아니라 지표상에서도 관찰된다. 가행광산에서는 가스의 유출은 작업환경을 급격히 악화시키므로 오염된 공간을 희석 시키기 위한 충분한 양의 통기량의 공급, 그리고 유해 가스 유출과 확산을 제어하기 위한 통기방안의 연구가 필요하다. 본 연구는 채움공간내 가스제어를 위한 압력균형 통기기술의 적용성 연구를 목적으로 한다.

Gas Bubble Driven Circulation Systems에서의 이상유동 특성의 시뮬레이션 (A Simulation on the Two-Phase Flow Characteristics in Gas Bubble Driven Circulation Systems)

  • 최청렬
    • 한국시뮬레이션학회논문지
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    • 제7권2호
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    • pp.17-32
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    • 1998
  • The flow fields in Gas Bubble Driven Circulation Systems were numerically analyzed. In various gas flow rate and bubble size, the flow characteristics were predicted. Eulerian-Eulerian approach was used for the formulation of both the continuous and dispersed phases. The modification of the general purpose computer program PHOENICS code was employed to predict the mean flow fields, turbulent characteristics, gas dispersion, volume fraction. The predicted shows very satisfactory agreement with experimental results for all regions of ladle. The results are of interest in the design and operation of wide variety of material processing.

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유해 대기오염물질의 난류확산 수치모의에서 침적한과 부력항 추가에 따른 효과 (Addition Effect of the Deposition and Buoyancy Terms in Modeling Turbulence Diffusion of Hazardous Air Pollutants)

  • 원경미;이화운;지효은;김철희;송창근
    • 한국대기환경학회지
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    • 제22권1호
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    • pp.73-84
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    • 2006
  • Hazardous Air Pollutants (HAPs) are characterized by being relatively heavier and denser than that of ambient air due to the various reasons such as higher molecular weight, low temperature and other complicated chemical transformations (Witlox, 1994). In an effort to investigate transport and diffusion from instantaneous emission of heavy gas, Lagrangian Particle Dispersion Model (LPDM) coupled with the RAMS output was employed. Both deposition process and buoyancy term were added on the atmospheric diffusion equations of LPDM, and the locations and concentrations of dense gas particle released from instantaneous single point source (emitting initially for 10 minutes only) were analyzed. The result overall shows that adding deposition process and buoyancy terms on the diffusion equation of LPDM has very small but detectable effect on the vertical and horizontal distribution of Lagrangian particles that especially transported for a fairly long traveling time. Also the slumping of dense gas can be found to be ignored horizontally compared to the advection by the horizontal wind suggesting that it was essential to couple the Lagrangian particle dispersion model coupled with the RAMS model in order to explain the dispersion of HAPs more accurately. However, during the initial time of instantaneous emission, buoyancy term play an important role on the vertical locations of dense particles for near surface atmosphere and around source area, indicating the importance of densities of HAPs in the beginning stage or short duration for the risk assessment of HAPs or management of heavy vapors during the explosive accidents.

수소가스사고의 피해범위 (Hazard Distance from Hydrogen Accidents)

  • 조영도
    • 한국가스학회지
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    • 제16권1호
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    • pp.15-21
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    • 2012
  • 수소가스의 제트 누출에 의한 확산, 화재, 그리고 폭발에 의한 위험 범위를 분석하고, 안전거리 기준을 설정하기 위한 위험거리를 확산, 화재, 그리고 폭발에 대한 단순한 예측 식들을 제시하였다. 핀홀에 의한 누출과 같은 소량 수소가스 누출속도에 있어서 피해거리는 제트누출 확산에 의한 피해거리가 제트화재에 의한 피해거리보다 크며, 압력의 제곱근에 그리고 누출 홀의 직경에 비례하고 이는 수 십 미터에 이른다. 배관의 완전 파손 또는 저장 탱크의 큰 홀 발생과 같은 대량의 수소가스 누출속도에서는 제트화재의 피해거리가 개방공간의 가스운 폭발에 의한 피해거리보다 크며, 수 백 미터에 이른다. 수소충전소와 건물과의 최소이격거리 즉 안전거리 설정 기준을 대량 수소가스누출 사고시나리오를 기반으로 한다면, 도심지에 수소충전소는 안전거리 기준을 만족시키기 어려울 것이다. 따라서 대량의 수소가스 누출사고를 안전장치들을 통하여 예방하고, 안전거리 기준을 소량의 수소가스누출사고 기준으로 설정 할 수 있다. 그러나 대량누출 가능성이 있는 경우 학교와 병원 등 인구밀집 건물은 수 백 미터의 안전거리를 유지하여야 한다.

가스추진 LNG 운반선의 가스 압축기실에 설치된 가스검출장치의 최적 배치에 관한 연구 (Optimal Gas Detection System in Cargo Compressor Room of Gas Fueled LNG Carrier)

  • 이상원;소예덕;이승훈;이진욱;정은석;강호근
    • 해양환경안전학회지
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    • 제25권5호
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    • pp.617-626
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    • 2019
  • 본 연구는 가스추진 174K급 LNG 운반선의 가스 압축기실에서 발생하는 가스누출 모사를 통해 가스탐지기의 최적 위치를 분석하였으며, 새로 개정된 IGC 코드에 명시된 안전규정을 만족하는 합리적인 방법도 함께 제안하였다. 가스압축기실에서의 LNG 가스누출 수치해석을 위해, 실제 ME-GI 엔진이 장착된 174K급 LNG 운반선의 압축기실 형상과 장비, 배관의 배치와 같은 치수로 3D 설계되었다. 가스누설에 대한 시나리오는 305 bar의 높은 압력과 1 bar의 낮은 압력을 적용하여 진행하였다. 고압용 핀홀의 크기는 4.5, 5.0, 5.6 mm이고 저압용은 100, 140 mm이다. 해석 결과, 5.6 mm 핀홀(고압)과 100, 140 mm 핀홀(저압) 상태의 누출에 대한 환기평가에서 가연성 가스농도는 심각한 위험이 없음을 확인하였다. 그러나 개정된 IGC 코드에 따라 설치된 압축기실의 가스 감지 센서의 실제 위치는 다른 지점으로 이동해야 하고, 측정 지점이 현 규정에서 요구하는 것보다 더 추가되어야 함을 확인하였다.

잠겨진 가스분사장치에서의 2상유동의 열수력학적 특성 (Thermohydraulic Characteristics of Two-Phase Flow in a Submerged Gas Injection System)

  • 최청렬;김창녕
    • 대한기계학회논문집B
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    • 제23권10호
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    • pp.1327-1339
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    • 1999
  • Characteristics of two-phase flow and heat transfer were numerically investigated in a submerged gas Injection system. Effects of both the gas flow rate and bubble size were investigated. In addition, heat transfer characteristic and effects of heat transfer were investigated when temperature of the injected gas was different from that of the liquid. The Eulerian approach was used for the formulation of both the continuous and the dispersed phases. The turbulence in the liquid phase was modeled by the use of the standard $k-{\varepsilon}$ turbulence model. The interphase friction and heat transfer coefficient were calculated by means of correlations available in the literature. The turbulent dispersion of the phases was modeled by introducing a "dispersion Prandtl number". The plume region and the axial velocities are increased with increases in the gas flow rate and with decreases in the bubble diameter. The turbulent flow field grows stronger with the increases in the gas flow rate and with the decreases in the bubble diameter. In case that the heat transfer between the liquid and the gas is considered, the axial and the radial velocities are decreased in comparison with the case that there is no temperature difference between the liquid and the gas when the temperature of the injected gas is higher than the mean liquid temperature. The results in the present research are of interest in the design and the operation of a wide variety of material and chemical processes.

가스 누출 실험, CFD 및 거리산출 비교를 통한 LP가스 누출 검지농도 분포에 대한 고찰 (A Comparison on Detected Concentrations of LPG Leakage Distribution through Actual Gas Release, CFD (FLACS) and Calculation of Hazardous Areas)

  • 김정환;이민경
    • 공업화학
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    • 제32권1호
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    • pp.102-109
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    • 2021
  • Recently, an interest in risk calculation methods has been increasing in Korea due to the establishment of classification code for explosive hazardous area on gas facility (KGS CODE GC101), which is based on the international standard of classification of areas - explosive gas atmospheres (IEC 60079-10-1). However, experiments to check for leaks of combustible or toxic gases are very difficult. These experiments can lead to fire, explosion, and toxic poisoning. Therefore, even if someone tries to provide a laboratory for this experiment, it is difficult to install a gas leakage equipment. In this study we find out differences among actual experiments, CFD by using FLACS and calculation based on classification code for explosive hazardous area on gas facility (KGS CODE GC101) by comparing to each other. We develpoed KGS HAC (hazardous area classification) program which based on KGS GC101 for convenience and popularization. As a result, actual gas leak, CFD and KGS HAC are showing slightly different results. The results of dispersion of 1.8 to 2.7 m were shown in the actual experiment, and the CFD and KGS HAC showed a linear increase of about 0.4 to 1 m depending on the increase in a flow rate. In the actual experiment, the application of 3/8" tubes and orifice to take into account the momentum drop resulted in an increase in the hazardous distance of about 1.95 m. Comparing three methods was able to identify similarities between real and CFD, and also similarities and limitations of CFD and KGS HAC. We hope these results will provide a good basis for future experiments and risk calculations.

Carbon Molecular Sieve Membranes Dispersed with Nano Particles

  • H.Suda;Ha, K.raya
    • 한국막학회:학술대회논문집
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    • 한국막학회 2004년도 Proceedings of the second conference of aseanian membrane society
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    • pp.183-186
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    • 2004
  • Nano particles-containing CMS membranes were prepared by pyrolysis of polyimides dispersed uniformly with precursors and their gas separation performances were examined, to elucidate the permeation mechanism and to further improve the gas separation performance. Consequently, it was suggested that the separation performance could be controlled by doping nano-particles in the CMS membranes, and that optimization of various factors, such as the size, content, and dispersion state of the nano particles would contribute for further improvement of the gas separation performance.

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