• Journal of the Korean Institute of Gas
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• v.2 no.4
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• pp.53-59
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• 1998

Flow pattern of air-water two phase flow depends on the conditions of pressure drop, void fraction, and channel geometry. Drag reduction in the two phase flow can be applied to the transport of crude oil, phase change systems such as chemical reactor, pool and boiling flow, and to present cavitation which occurs in pump impellers. But the research on drag reduction in two phase flow is not intensively investigated. Therefore, experimental investigations have been carried out to analyze the drag reduction produced and void fraction by Co-polymer(A611p) addition in the two phase flow system. We find that the maximum point position of local void friction moves from the wall of the pipe to the center of the pipe when polymer concentration increases. Also we find that the polymer solution changes the characteristics of the two phase flow. And then we predict that it is closely related with the drag reduction.

• Proceedings of the Korean Society for Noise and Vibration Engineering Conference
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• 2003.05a
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• pp.379-382
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• 2003

천공요소는 자동차의 배기 소음기, 공조기의 소음기 등을 포함하는 다양한 소음계에 널리 사용된다. 일반적으로 천공요소 들은 평균 유동과 소음원이 동시에 존재하는 환경에서 사용되며, 평균 유동 및 관 내부의 음압 레벨의 변화가 천공 부근에서의 임피던스에 큰 영향을 미치게 된다. 천공요소의 임피던스의 변화는 소음기의 음향학적 특성에 영향을 미치게 되므로, 유동이나 음압 조건이 임피던스에 미치는 영향에 대한 연구가 중요하다. 본 연구에서는 정밀 계측 및 전산유체역학적 모형을 이용해 천공요소의 임피던스에 영향을 미치는 주요 세 가지 인자 - 스치는 유동, 통과하는 유동, 음압 레벨 - 들을 고려하여 임피던스를 분석하고, 그 상관관계를 밝혔다.

• Proceedings of the SAREK Conference
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• 2004.06a
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• pp.4-4
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• 2004

• The Korean Journal of Rheology
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• v.2 no.2
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• pp.35-44
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• 1990

자유표면 유동을 수반하여 복잡한 구조를 지나는 유동문제를 수치모사할 수 있는 삼차원 유한요소법코드를 개발하였다. 정사각관을 대상으로 하는 삼차원 압출팽창 문제를 등온 뉴톤 유동뿐만아니라 비뉴톤유동 및 비등온 유동문제의 경우까지 다룰수 있도록 확장 하여 수치모사하였다. 삼차원 유한요소법 알고리듬에 pathline approach 방법과 사상방법을 적용시켜 등온 뉴톤 유체의 미동흐름에 대하여 압출 팽창문제를 푼 결과 팽창비가 대칭면에 서 최대 21.0%관의 모서리 부분에서 최소 4.1%로 나타났다 전단박화현상이 있는 비뉴톤 유 동의 경우 뉴톤유동에 비해 팽창이 작게 일어났고 비등온 유동의 경우 관벽온도가 낮은 쪽 이 높은 쪽에 비해 팽창이 크게 일어남을 알수 있었다.

• Proceedings of the Korean Society of Propulsion Engineers Conference
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• 1999.10a
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• pp.14-14
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• 1999

액체 램제트 엔진의 특성은 흡입구를 통해 들어오는 유입공기의 상태에 따라 많이 달라진다. 흡입구에 들어오는 공기의 유입각이 일정각도를 넘어서면 유입공기의 왜곡이 심하여 정상적인 연소가 불가능 할 수 있다. 따라서 다양한 비행조건에 따른 램제트 엔진의 특성을 파악하기 위하여 외부 유입영역, 흡입구, 연소기, 노즐 및 출구 대기 영역을 함께 계산하여 유동 특성과 연소 특성을 파악하고자 하였다. 흡입구는 마하 2.0을 기준으로 설계하고, 4각 덕트에서 완만하게 원형 덕트로 변화되는 확대관의 형상으로 비행체에 붙어 있는 것으로 격자를 구성하였다. 흡입구에서의 유동 조건은 비행체을 지난 유속이 마하 2.0과 2.2의 경우에 대하여 수치 실험을 수행하였으며, 비반응 유동 해석과 연소가 있는 반응 유동해석 결과를 흡입구를 포함하지 않았던 선행 연구 결과들과 비교하였다. 유입각이 영 일 때의 흡입구를 포함한 계산 결과는 흡입구에서 생성되는 충격파에 의한 손실로 총압력이 흡입구를 포함하지 않았던 선행 연구 결과와 차이가 있었으나 유동 특성에는 큰 차이가 없었다. 그러나 유입각이 증가함에 따라 흡입구로 유입되는 공기의 량이 감소하고 그에 따른 유동의 왜곡이 심하여 연소특성에 변화를 보여 주었다.

• The Journal of Engineering Geology
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• v.23 no.4
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• pp.447-455
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• 2013

A micro-mechanical pipe network model with the shape of a cube was developed to simulate the behavior of fluid flow through a porous medium. The fluid-flow mechanism through the cubic pipe network channels was defined mainly by introducing a well-known percolation theory (Stauffer and Aharony, 1994). A non-uniform flow generally appeared because all of the pipe diameters were allocated individually in a stochastic manner based on a given pore-size distribution curve and porosity. Fluid was supplied to one surface of the pipe network under a certain driving pressure head and allowed to percolate through the pipe networks. A percolation condition defined by capillary pressure with respect to each pipe diameter was applied first to all of the network pipes. That is, depending on pipe diameter, the fluid may or may not penetrate a specific pipe. Once pore pressures had reached equilibrium and steady-state flow had been attained throughout the network system, Darcy's law was used to compute the resultant permeability. This study investigated the sensitivity of network size to permeability calculations in order to find out the optimum network size which would be used for all the network modelling in this study. Mean pore size and pore size distribution curve obtained from field are used to define each of pipe sizes as being representative of actual oil sites. The calculated and measured permeabilities are in good agreement.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.34 no.1
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• pp.77-82
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• 2010

Our study aims to understand the flow of liquid in an open-top rectangular microchannel that can be used in micro total analysis systems ($\mu$-TAS) because it has advantages in terms of light transmission and energy efficiency. We measured the liquid velocity using particle tracking technique and conducted a simulation with computational fluid dynamics by altering the area of channel cross section and channel length for the capillary-driven flow in the open-top rectangular microchannel. When liquid water drops to an entrance of the fabricated microchannel with a height of 20 μm and a width of 20 ${\mu}m$, it flows along the microchannel by only capillary force. In the wetting behavior of the liquid, important parameters of this flow are channel size, contact angle and liquid properties such as surface tension and viscosity, which are used to control the flow of liquid in the microchannel.

• Korean Chemical Engineering Research
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• v.56 no.6
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• pp.864-870
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• 2018

The effect of lower bed height on the collapse velocity was investigated for a two-stage bubbling fluidizedbed (0.1 m in diameter, 1.2 m high) connected with a standpipe (0.025 m in diameter) for solid transport. Air was used as fluidizing gas and mixture of coarse (< $1000{\mu}m$ in diameter and $3625kg/m^3$ in apparent density) and fine (< $147{\mu}m$ in diameter and $4079kg/m^3$ in apparent density) particles as solid particles. Mixing ratio of fine particles, height of the lower bed and the distributor of the upper bed were considered as experimental variables. The collapse velocity increased with static height of the lower bed. However, the effect decreased as the mixing ratio of fine particles increased. The effect seemed to be attributed to the increase in height of the dense layer of coarse particles that prevented the gas from flowing into the standpipe, not in pressure drop for the standpipe, as the bed height increased. The collapse velocity decreased a little as the pressure drop of the distributor of the upper bed increased. An improved correlation was proposed for predicting the collapse velocity.

• Proceedings of the KSME Conference
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• 2001.06e
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• pp.748-753
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• 2001

The objective of the present study is to visualize the pulsatile flow fields by using three-dimensional computer simulation and the PIV system. A closed flow loop system was built for the steady and unsteady experiments. The Harvard pulsatile pump was used to generate the pulsatile pressure and velocity waveforms. Conifer powder as the tracing particles was added to water to visualize the flow field. Two consecutive particle images were captured by a CCO camera for the image processing at several cross section. The range validation and the area interpolation methods were used to obtain the final velocity vectors with high accuracy. The finite volume predictions were used to analyze three-dimensional flow patterns in the bifurcation model. The results of the PIV experiment and the computer simulation are in good agreement and the results show the recirculation zones and formation of the paired secondary flow distal to the apex of the bifurcated model. The results also show that the branch flow is pushed strongly to the inner wall due to the inertial force effect and helical motions are generated as the flow proceeds toward the outer wall.

• Journal of Energy Engineering
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• v.18 no.4
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• pp.258-263
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• 2009

Jet Loop Reactor(JLR), in which a two-phase nozzle is installed, is the new design technique for the treatment of high concentration wastewater by accelerating of oxygen contacting between substrate and surrounding bacteria. This numerical study of the two phase jet flow was conducted to find the optimum design of JLR. It was shown that there was a minimum velocity in the nozzle for continuous circulation of wastewater. The optimum location and the size of the draft tube for continuous circulation were examined. It was certain that the smaller the air size is, the more the effect of the mixing increases. The relation between the mixing effect and the turbulence was confirmed.