• Journal of the KSME
• /
• v.30 no.4
• /
• pp.322-330
• /
• 1990

2상유동의 물리적 문제는 이상화된 계면형상, 경계 및 초기조건과 연속체공식화를 이용한 지배 및 구속관계에 의해 정립된다. 본 글에서는 2상유동모델의 공식화에 대한 근거와 응용의 제한 성등이 제시되었다. 각 2상유동모델들 사이에는 많은 차이점이 존재하고 이들은 모두 주어진 경우에 적절한 평균화 과정에 의해 유도되었다. 2상유동모델링의 가장 큰 어려움은 구속관계의 개발과 관련되어 있으며 실험적 결과와의 송환과정을 통하여 향상될 수 있을 것이다. 구속 조 건의 개발과 함께 2상유동모델링에 대한 연구는 미시적인 동적해석을 위한 다차원 2-유체모델과 총체적인 계의 거동해석을 위한 1차원 2-유체모델, 혹은 단일유체모델의 분야에서 계속 진행되 어야 할 것이다.

• Transactions of the Korean Society of Mechanical Engineers
• /
• v.17 no.5
• /
• pp.1313-1320
• /
• 1993

Flow patterns inside the riser section and the effects of the heater inlet-and exit-restrictions, liquid charging level and the heater inlet subcooling on the flow characteristics inside an open two-phase natural circulation loop were studied experimentally. Three basic circulation modes were observed ; periodic circulation (A)(flow oscillations with incubation(no boiling) period), continuous circulations(stable operation mode with no flow oscillations), and periodic circulation (B) (flow oscillations with continuous boiling). The circulation rate increases and then decreases with the increase of the heating rate and the maximum circulation rate appears with the continuous circulation mode. The decrease of the inlet-restriction or the increase of the exitrestriction destabilizes the system. When the liquid charging level or the inlet subcooling decreases, the continuous circulation mode starts at the lower heating rate and the system is stabilized.

• Transactions of the Korean Society of Mechanical Engineers
• /
• v.15 no.1
• /
• pp.299-307
• /
• 1991

A unified correlation of the interfacial friction factor for air-water and steam-water flows in inclined rectangular channels has been developed. The correlation was expressed in the form of a power law of the liquid and the gas Reynolds number, and the liquid-to-gas viscosity ratio. In addition, a relation between the equivalent roughness and the intensity of wave height fluctuation of the interface has been investigated. A new dimensionless intensity of fluctuation including a liquid film Reynolds number is proposed. It has been shown that the dimensionless equivalent roughness, which is calculated from the Nikuradse equation, can be uniquely related to this dimensionless intensity of fluctuation for both air-water and steam-water flows.

• Journal of the Korean Society for Nondestructive Testing
• /
• v.22 no.5
• /
• pp.545-556
• /
• 2002

Bubble behaviors in two-phase flows have been analyzed by tomography methods such as an algebraic reconstruction technique (ART) and a multiplicative algebraic reconstruction technique (MART). Initially, a bubbly flow and an annular flow have been investigated by cross-sectional view using computer synthesized phantoms. Two tomography methods have been compared to obtain more accurate results of the two-phase flows. Then, reconstruction of three-dimensional density distributions of phantoms with two and three bubbles have been accomplished by the MART method which provided the better results for the two-dimensional reconstructions accurately to analyze the bubble behaviors in the two-phase flow.

• Economic and Environmental Geology
• /
• v.44 no.2
• /
• pp.153-159
• /
• 2011

A comprehensive mechanistic model has been used to determine the flow pattern for gas-oil two-phase flow in pipes of petroleum production system. Depending on operational parameters, geometrical variables, and physical properties of the two phases, the two phases shows a specific flow patterns. For different parameters of the system, How pattern were compared for wide range of superficial velocities of oil and gas. In a variety of parameters, the inclinational angle and superficial velocities of oil and gas are the most dominant factors in determining the flow patterns for two-phase flow in pipelines. Other parameters such as pipe diameter and fluid properties have a limited effect on the change of flow patterns except for near transition. The mechanistic model is shown to be useful to determine the flow pattern in situations where either an experimental evaluation in a laboratory or reliable correlations are not available.

• Proceedings of the Computational Structural Engineering Institute Conference
• /
• 2011.04a
• /
• pp.648-651
• /
• 2011

본 논문에서는 3차원 섬유분포를 가정하여 고유동 섬유보강 시멘트 모르타르의 유동에 따른 섬유방향성변화를 해석적으로 파악해 보았다. 유동흐름은 평면상의 2차원 완전발달 전단흐름을 고려하였다. 유동에 따른 섬유의 회전운동은 섬유간의 상호 간섭효과를 무시한 Jeffery의 기본식에 근거하였다. 굳지 않은 섬유혼입 모르타르의 유동에 따른 섬유방향성 분포 변화를 흐름선과 동일 유동거리 상의 단면에 대해 파악하였다. 그 결과, 단면 내 위치에 따라서 섬유방향성 분포 변화가 크게 차이가 발생하는 것을 확인할 수 있었다. 또한 유동거리에 따른 단면상의 섬유방향성 분포는 초기 유동거리에서 분포 형상에 큰 변화가 발생하였고, 유동에 따라 섬유가 유동방향과 나란하게 놓이는 경향이 커지는 것을 확인할 수 있었다. 이러한 섬유방향성 변화의 예측은 섬유보강 시멘트 복합체의 인장특성에 예측하는데 유용하게 사용될 것이다.

• Nuclear Engineering and Technology
• /
• v.16 no.1
• /
• pp.1-10
• /
• 1984

General time-volume averaged conservation equations and jump conditions for two-phase flows are derived here. The time-averaged equations for a single phase region in two-phase flow are obtained from local instant balance equations by a technique often used for single phase turbulent flow equations. The results obtained by integrating the time averaged equations over a flow volume are spatially averaged twice; first, they are averaged over a single phase region of the k-th phase and then averaged over the total volume of the k-th phase, in a flow volume. The mass, momentum, and energy conservation equations are obtained from the general time-volume averaged equations. The advantages of the present model are explained by comparing it with Ishii's model (1) and Banerjee's model (2). Finally, the assumptions and approximate terms of the equations of the THERMIT-6S are clarified.

• Transactions of the Korean Society of Mechanical Engineers
• /
• v.15 no.6
• /
• pp.1948-1966
• /
• 1991

Two-phase cross-flow exists in many shell-tube heat exchangers such as condensers, reboilers and nuclear steam generators. To avoid problems due to excessive vibration, information on vibration excitation in two-phase cross-flow is required. Fluid-elastic instability is discussed in this paper. Four tube bundle configurations were subjected to increasing flow up to the onset of fluid-elastic instability. The tests were done on bundles with one flexible tube surrounded by rigid tubes. The fluid-elastic instability behavior is different for intermittent flows than for bubbly flows. For bubbly flows, the observed instabilities satisfy the relationship V/fd=K(2.pi..zeta. m/rho. $d^{21}$)$^{0.51}$ in which the minimum instability factor K was found to be 2.3 for bundles of p/d=1.22. The lowest critical velocities for fluid-elastic instability were experienced with parallel-triangular tube bundles. For intermittent flow, the observed instabilities did not follow the forgoing relation-ship. Significantly lower flow velocities were required for instability..

• Journal of the KSME
• /
• v.30 no.4
• /
• pp.341-357
• /
• 1990

기존의 원자력발전소의 설계 및 안전한 운전과 가상되는 중대사고 진행과정을 해석하여 더욱 안전한 원자로를 건설하기 위해서는 2상유동에 관련된 현상을 보다 잘 이해하여야 함이 명확하다. 지금까지의 실험적 연구를 더욱 확장하여 현재 사용하고 있는 실험식이 도출된 실험들의 스케일 효과를 규명하고, 2상유동의 측정방법의 개발이 더욱 진행되어 보다 정확한 실험결과를 도출하여야 한다. 한편으로, 2상유동을 수치적으로 해석하고자 하는 노력도 계속되어야 한다. 특히 원자력공학에서는 비등 및 응축과 같은 상변화 및 비등 열전달과 같이 열의 전달현상이 중요한 역할을 하므로 이에 대한 연구 필요성이 계속될 것이다.

• Journal of Advanced Marine Engineering and Technology
• /
• v.22 no.4
• /
• pp.505-514
• /
• 1998

Flow pattern of air-water two phase flow depends on the conditions of pressure void fraction and channel geometry. We classify the flow pattern by measuring the output signal of the conductivity probe. under the classified flow pattern we mount a visualization equipment on the test section and take pictures. We vary the concentration of pure solvent and polymer to measure local void fraction. We know that the maximum point position of local void fraction distribution move from the center of the pipe to the wall of the pipe as JSL increase when JSA is constant in two phase flow. But we find that the maximum point position of local void friction move from the wal of the pipe to the center of the pipe when polymer concentration increase.