• 제목/요약/키워드: gas diffusion

검색결과 1,043건 처리시간 0.038초

밀폐공간 및 강제환기공간에의 천연가스 고압분출 시 농도 확산분포 거동해석 (I) (The Diffusion Behavier Analysis Caused by High Pressure Natural Gas Leak in Enclosure with and without Ventilation System (I))

  • 하태웅;하종만;김은자
    • 한국가스학회지
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    • 제16권4호
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    • pp.23-31
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    • 2012
  • 밀폐 공간 내의 천연가스 공급 시스템에서 가스 누설에 따른 재난을 방지하고 보다 안전한 설계를 하기 위해서는 누출된 천연가스의 확산거동을 이해하고 예측할 수 있는 기술이 필요하다. 본 연구에서는 CFD를 사용한 해석법을 제시하고, 기 수행된 British Gas Technology Co.의 실험결과와 비교하여 타당성을 제시하였다. 노즐에서의 분출유량 2D 해석 결과는 실험결과와 2.6% 이내로 잘 일치함을 보였다. 또한, 다양한 강제 환기 조건에 따른 가스 확산 특성을 비정상상태 3차원 CFD 해석을 수행한 결과 실험결과와 정성적인 경향이 잘 일치됨을 보였다.

지하매설 가스배관의 가스 누출시 지하 확산거동에 관한 연구 (A Study on the Diffusion Behavior of Leak Gas from Underground Gas Pipeline)

  • 최송천;조영도;김교선
    • 한국가스학회지
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    • 제3권2호
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    • pp.43-52
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    • 1999
  • 지하에 매설된 도시가스 배관에서의 누출 가스에 대한 확산 거동을 관찰하기 위하여 지중 확산실험조를 제작하여 실험하였다. 실험조는 도시가스 공급위치와 농도의 측정위치를 변화시킬 수 있도록 acryl로 제작하였으며, MOS 센서를 이용하여 도시가스 농도를 측정하였다. 가스의 지하 확산을 측정하기 위한 토질로서 주문진 표준사와 화강풍화토를 이용하였으며, 가스누출 속도 변화에 따른 도시가스 농도 변화를 시간에 따라 측정하였다. 누출점으로부터 센서의 측정위치가 가까울수록 또는 누출 속도가 증가할수록 가스의 감지시간이 감소하였으며, 누출가스 농도의 빠른 증가로 인하여 정상상태시 높은 농도를 나타내었다. 또한, 주문진 표준사보다 다짐에 의해 밀도가 증가한 화강풍화토에서 초기에 농도가 낮게 측정되었으나, 시간이 지남에 따라 농도가 높게 나타났다.

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가스 확산층(GDL)내부의 물이 연료전지 성능에 미치는 영향 (The Effect of Liquid Water in Fuel Cell Cathode Gas Diffusion Layer on Fuel Cell Performance)

  • 박상균
    • Journal of Advanced Marine Engineering and Technology
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    • 제39권4호
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    • pp.374-380
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    • 2015
  • 본 연구에서는 연료전지 캐소드 가스 확산층에서의 물의 영향이 연료전지 성능에 미치는 영향을 검토하기 위하여 연료전지 스택의 부하 변동에 따른 가스 확산층에서의 2상 현상의 구현이 가능한 동적 모델을 개발하였다. 개발된 모델에 대하여 2상의 영향에 의한 연료전지 부하변동에 따른 연료전지 스택 성능, 가스 확산층 내부에서의 물 증기와 산소의 농도분포, 가스 확산층의 두께 및 다공성이 연료전지 스택 전압에 미치는 영향에 대하여 검토하였다. 그 결과 본 연구의 범위 내에서 연료전지 스택 전압은 부하에 관계없이 2상 모델이 1상 모델보다 낮아짐을 알 수 있다. 촉매층 부근 가스 확산층에서의 산소 농도는 가장 낮고 물 증기의 농도는 가장 높음을 알 수 있었다. 또한, GDL의 두께가 두꺼울수록 GDL의 다공성이 작을수록 연료전지 스택 전압이 낮아짐을 알 수 있었다.

CONCENTRATION CONTOURS IN LATTICE AND GRAIN BOUNDARY DIFFUSION IN A POLYCRYSTALLINE SOLID

  • Kim, Yongsoo;Wonmok Jae;Saied, Usama-El;Donald R. Olander
    • 한국원자력학회:학술대회논문집
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    • 한국원자력학회 1995년도 추계학술발표회논문집(2)
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    • pp.707-712
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    • 1995
  • Grain boundary diffusion plays significant role in the fission gas release, which is one of the crucial processes dominating nuclear fuel performance. Gaseous fission products such as Xe and Kr generated inside fuel pellet have to diffuse in the lattice and in the grain boundary before they reach open space in the fuel rod. In the mean time, the grains in the fuel pellet grow and shrink according to grain growth kinetics, especially at elevated temperature at which nuclear reactors are operating. Thus the boundary movement ascribed to the grain growth greatly influences the fission gas release rate by lengthening or shortening the lattice diffusion distance, which is the rate limiting step. Sweeping fission gases by the moving boundary contributes to the increment of the fission gas release as well. Lattice and grain boundary diffusion processes in the fission gas release can be studied by 'tracer diffusion' technique, by which grain boundary diffusion can be estimated and used directly for low burn-up fission gas release analysis. However, even for tracer diffusion analysis, taking both the intragranular grain growth and the diffusion processes simultaneously into consideration is not easy. Only a few models accounting for the both processes are available and mostly handle them numerically. Numerical solutions are limited in the practical use. Here in this paper, an approximate analytical solution of the lattice and stationary grain boundary diffusion in a polycrystalline solid is developed for the tracer diffusion techniques. This short closed-form solution is compared to available exact and numerical solutions and turns out to be acceptably accurate. It can be applied to the theoretical modeling and the experimental analysis, especially PIE (post irradiation examination), of low burn up fission. gas release.

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Numerical Model for Stack Gas Diffusion in Terrain Containing Buildings - Application of Numerical Model to a Cubical Building and a Ridge Terrain -

  • Sada, Koichi;Michioka, Takenobu;Ichikawa, Yoichi
    • Asian Journal of Atmospheric Environment
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    • 제2권1호
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    • pp.1-13
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    • 2008
  • A numerical simulation method has been developed to predict atmospheric flow and stack gas diffusion using a calculation domain of several km around a stack under complex terrain conditions containing buildings. The turbulence closure technique using a modified k-$\varepsilon$-type model under a non hydrostatic assumption was used for the flow calculation, and some of the calculation grids near the ground were treated as buildings using a terrain-following coordinate system. Stack gas diffusion was predicted using the Lagrangian particle model, that is, the stack gas was represented by the trajectories of released particles. The numerical model was applied separately to the flow and stack gas diffusion around a cubical building and to a two-dimensional ridge in this study, before being applied to an actual terrain containing buildings in our next study. The calculated flow and stack gas diffusion results were compared with those obtained by wind tunnel experiments, and the features of flow and stack gas diffusion, such as the increase in turbulent kinetic energy and the plume spreads of the stack gas behind the building and ridge, were reproduced by both calculations and wind tunnel experiments. Furthermore, the calculated profiles of the mean velocity, turbulent kinetic energy and concentration of the stack gas around the cubical building and the ridge showed good agreement with those of wind tunnel experiments.

용융탄산염 연료전지 연료극 기체 유로 높이에 따른 가스 확산 및 단전지 성능 변화 연구 (Effect of Anode Gas Channel Height on Gas Diffusion and Cell Performance in a Molten Carbonate Fuel Cell)

  • 이정현;김도형;김범주;강승원;임희천
    • 한국수소및신에너지학회논문집
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    • 제20권6호
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    • pp.479-484
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    • 2009
  • The effect of anode gas channel height on gas diffusion and cell performance in a 100 $cm^2$ class molten carbonate single cell is investigated. Single cell separators with three different channel height are used. The effect of the gas channel height on the distribution of the reactive gas concentration is evaluated by the two-dimensional concentration diffusion equation. The overpotential caused by concentration drop with different channel height is estimated by the voltage decay related to diffusion of reactants, well known as concentration polarization, using limiting current density. The estimation could have the possibility to identify the reactant mass transfer polarization in the complicate factors of the overall electrodes.

광산란과 입자포집을 이용한 동축류 확산화염 내의 실리카 입자의 성장 측정(II) - 확산의 영향 - (An Experimental Study of Silica Particle Growth in a Coflow Diffusion Flame Utilizing Light Scattering and Local Sampling Technique (II) - Effects of Diffusion -)

  • 조재걸;이정훈;김현우;최만수
    • 대한기계학회논문집B
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    • 제23권9호
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    • pp.1151-1162
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    • 1999
  • The effects of radial heat and $H_2O$ diffusion on the evolution of silica particles in coflow diffusion flames have been studied experimentally. The evolution of silica aggregate particles in coflow diffusion flames has been measured experimentally using light scattering and thermophoretic sampling techniques. The measurements of scattering cross section from $90^{\circ}$ light scattering have been utilized to calculate the aggregate number density and volume fraction using with combination of measuring the particle size and morphology through the localized sampling and a TEM image analysis. Aggregate or particle number densities and volume fractions were calculated using Rayleigh-Debye-Gans and Mie theory for fractal aggregates and spherical particles, respectively. Flame temperatures and volumetric differential scattering cross sections have been measured for different flame conditions such as inert gas species, $H_2$ flow rates, and burner injection configurations to examine the relation between the formation of particles and radial $H_2O$ diffusion. The comparisons of oxidation and flame hydrolysis have also been made for various $H_2$ flow rates using $N_2$ or $O_2$ as a carrier gas. Results indicate that the role of oxidation becomes dominant as both carrier gas($O_2$) and $H_2$ flow rates increases since the radial heat diffusion precedes $H_2O$ diffusion in coflow flames used in this study. The effect of carrier gas flow rates on the evolution of silica particles have also been studied. When using $N_2$ as a carrier gas, the particle volume fraction has a maximum at a certain carrier gas flow rate and as the flow rate is further increased, the hydrolysis reaction Is delayed and the spherical particles finally evolves into fractal aggregates due to decreased flame temperature and residence time.

벼 품종유형간 잎 기공밀도와 기체확산저항 비교 (Comparative Study of Stomatal Density and Gas Diffusion Resistance in Leaves of Various Types of Rice)

  • ;;;;이주열
    • 한국작물학회지
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    • 제40권2호
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    • pp.125-132
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    • 1995
  • 유형이 다른 품종들간에 기공밀도와 기체확산저항의 차이와 광합성 속도에 미치는 영향 등을 비교 검토한 바 일반적으로 Indica 품종의 기공밀도가 Japonica 품종보다 컸으나 기체확산은 작았다. Indica 품종과 Japonica 품종간의 교잡을 통하여 육성한 품종들의 기공밀도와 기체확산 저항은 중간가를 나타냈다. 기공밀도와 기체확산저항 광합성 속도 간에는 현저한 정의 상관을 보였지만 특수엽중과는 현저한 질의 상관을 보였고, 단엽면적과의 상관관계는 현저하지 않았다. Indica 품종과 Japonica품종간의 교잡을 통하여 Indica 품종의 기공밀도가 크고 기체확산저항이 낮은 특성과 Japonica 품종의 특수 엽중이 큰 특성을 결합할 수 있다면 광합성 속도를 더욱 높일 수 있으리라 추측된다.

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합성가스를 이용한 역확산버너의 연소 및 복사열전달 특성, Part 1 : 공기-연료 연소 (Radiation Heat Flux and Combustion Characteristics of Inverse Diffusion Flame Burner Using Synthesis Gas, Part 1 : Air-Fuel Combustion)

  • 이필형;박창수;이재영;박봉일;황상순;이성호;안용수
    • 한국연소학회지
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    • 제14권4호
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    • pp.33-40
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    • 2009
  • Waste Thermal Pyrolysis Melting process was proposed and has been studied in order to prevent air pollution by dioxin and fly ash generated from combustion process for disposal of waste. In this study, applicability as the fuel of diffusion burner of synthesis gas formed from Waste Thermal Pyrolysis process was addressed. Results showed that there is no big difference in the flame shape between MNDF and SNDF, and lift off was detected in MIDF but flame is more stable in SIDF which contains hydrogen with high combustion velocity as flow rate in first nozzle is increased. And radiation heat flux in inverse diffusion flame of synthesis gas was found to be more by 1.5 times than that in inverse diffusion flame of methane because of higher mole fraction of $CO_2$ with high emissivity in product gas.

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Two-dimension Numerical Simulation of Stack Flue Gas Dispersion

  • Park, Young-Koo;Wu, Shi-Chang
    • 한국응용과학기술학회지
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    • 제29권1호
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    • pp.33-39
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    • 2012
  • A numerical simulation of plume from a stack into atmospheric cross flow is investigated using a two-dimension model. The simulation is based on the ${\kappa}{\sim}{\varepsilon}$ turbulence model and a finite volume method. In this paper, it mostly researches how the wind velocity affects the flue gas diffusion from an 80 m high stack. Wind velocity is one of the most important factors for flue gas diffusion. The plume shape size, the injection height, the NO pollutant distribution and the concentration at the near ground are presented with two kinds of wind velocities, 1 m/s and 5 m/s. It is found that large wind velocity is better for flue gas diffusion, it generates less downwash. Although the rise height is lower, the pollutant dilutes faster and more sufficient.