• 한국대기환경학회:학술대회논문집
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• 한국대기환경학회 1999년도 추계학술대회 논문집
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• pp.469-470
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• 1999

본 연구는 가스 중에 포함되어 있는 입자들을 fabric filter를 이용하여 집진할 때 형성되는 dust filter cake의 구조 및 압력강하가 입자간의 부착력(adhesion force), 마찰계수(friction coefficient)등의 여러 관련변수에 따라 변화되는 양상을 전산모사를 통해 예측하고자 하는 것이다.(중략)

• 설비공학논문집
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• 제15권6호
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• pp.510-517
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• 2003

An experimental study on the pressure drop during flow boiling for pure refrigerants R134a and Rl23, and their mixture was carried out in a uniformly heated horizontal tube. Tests were run at a pressure of 0.6 MPa and in the ranges of heat flux 5~50 kW/m$^2$, vapor quality 0~100 percent and mass velocity of 150~600 kg/m$^2$s. Generally, the two-phase frictional multiplier is used to predict the frictional pressure drop during the two-phase flow boiling. The obtained results have been compared to the existing various correlations for the two-phase multiplier. Also, the frictional pressure drop was compared to a few available correlations; The Lockhart-Martinelli correlation considerally overpredicted the frictional pressure drop data for mixture as well as pure components in the entire mass velocity ranges employed in the present study, while the Chisholm correlation underpredicted the present data. The Friedel correlation was found to satisfactorily correlate the frictional pressure drop data except for a low quality region.

• 설비공학논문집
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• 제18권1호
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• pp.38-46
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• 2006

The characteristics about the pressure drop in microtubes have been investigated. The test tubes are the circular, seamless, stainless steel tubes with an inner diameter of 0.244, 0.430, and 0.792 mm, respectively. R-l34a was used as a test fluid. Early flow transition which has been reported in some previous studies is not found in single-phase flow pressure drop tests. The conventional theory between friction factor and Reynolds number predicted the experimental friction factors within an absolute average deviation of $8.9\%$. The two-phase flow pressure drop increases for higher quality and mass flux, and for reduced inner diameter. The existing correlations fail to predict the experimental data. A new correlation to predict the two-phase flow pressure drop is developed in the form of the Lockhart-Martinelli correlation. The effects of the tube diameter and the surface tension were considered, and the correlation predicted the experimental data within an average absolute deviation of $8.1\%$.

• 대한기계학회논문집B
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• 제25권9호
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• pp.1219-1226
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• 2001

Pressure drops were measured for the flow boiling process within horizontal rectangular channels. The gap between the upper and the lower plates of each channel ranges from 0.4 to 2mm while the channel width being fixed to 20mm. Refrigerant 113 was used as the test fluid. The mass flux ranges from 50 to 200kg/㎡s and the channel walls were uniformly heated up to 15kW/㎡. The quality range covers from 0.15 to 0.75. The present experimental conditions coincide with the operating conditions of compact heat exchangers in which the liquid and gas flows are laminar and turbulent. The measured results were well represented by the two-phase frictional multiplier of Lee (2001) which has been developed for air-water two-phase flows within the deviation of $\pm$20%.

• 대한기계학회논문집B
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• 제23권5호
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• pp.637-645
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• 1999

Horizontal two-phase flow pressure drop within rectangular channels with small gap heights have been examined experimentally. The gap heights range from 0.4mm to 4mm corresponding to aspect ratios(the channel height divided by the width) from 0.02 to 0.2. Water and air were used as the test fluids with the superficial velocity ranges being 0.03-2.39m/s and 0.05-18.7m/s, respectively. The experimental results In rectangular channels were compared with the Lockhart-Martinelli correlation, which are widely used for conventional round tube. The Lockhart-Martinelli correlation turned out to be Inappropriate to represent the present experimental data. In this respect, considering the aspect ratio and gap-height effects, an empirical correlation on two-phase flow pressure drop was proposed. The proposed correlation successfully covers the bubbly, plug, slug and annular flow regimes.

• 동력기계공학회지
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• 제11권4호
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• pp.44-49
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• 2007

Generally, the economic concept of optimized design and operating conditions in fluidized bed heat exchangers can hardly be realized. Because the lack of fundamental knowledge about the particle flows, the optimum design of the fluidized bed heat exchanger is rather limited. In the present work, measurements are made on pressure drops and friction factors in the horizontal circular tube with solid particles in the circulating water. Two different solid particles of diameters of 3mm and 4mm are covered. The Reynolds numbers are ranged from 10,000 to 45,000. It is concluded that the friction factors for the particles of 4mm diameter are much higher than those for the particles of 3mm diameter. And at the lower particle concentration, the friction factors are strongly influenced by the fluid velocity rather than the particle concentration; However, the effect of the particle concentration on friction factors is also significantly higher at a higher particle concentration operating condition.

• 한국산학기술학회논문지
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• 제16권4호
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• pp.2891-2898
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• 2015

전자기장 효과를 이용한 준설토 장거리 이송기술이 개발되었다. 개발 기술의 효과를 정량적으로 평가하기 위해 계측 시스템을 이용하여 측정한 유속분포와 압력강하를 중심으로 전자기장 도입으로 인한 효과를 판단하였다. 대체 물질에 의한 실내실험과 실제 준설현장에서 장거리 이송기술을 적용해본 결과, 펌프만 사용하여 이송하는 경우보다 평균유속은 물론, 특별히 마찰층에서 속도증가가 있는 것을 확인하였다. 준설토 이송시, 이송관에 전자기장을 인가시켜줌으로써, 마찰층에서의 이송 저항을 감소시켜 전체적으로 속도를 증가시킴으로 인해 파이프에 의한 장거리 이송시 관내 압력강하를 줄이고, 유속을 증가시켜서 15km이상의 장거리 이송이 가능할 것으로 판단된다.

• Journal of Advanced Marine Engineering and Technology
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• 제37권4호
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• pp.316-323
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• 2013

평판형 태양열 집열기의 성능을 향상시키기 위하여 다양한 형태의 형상과 크기의 인공 거칠기가 가장 일반적이고 효과적으로 사용된다. 본 연구에서는 다양한 형상의 립을 삽입한 사각 채널에서의 열전달 특성 및 압력강하에 대하여 수치해석을 수행하였다. 사각 채널의 윗 평판에 일정한 열유속을 가하였다. 삽입된 립의 형상은 rib $90^{\circ}$, groove $90^{\circ}$, groove $60^{\circ}$, baffle $90^{\circ}$, baffle $60^{\circ}$, wave $90^{\circ}$, wave $60^{\circ}$ 모델이다. 작동유체는 공기이며 Reynolds 수는 3200~17800의 범위이다. 다양한 형태의 립 형상에 따른 시스템의 성능을 예측하기 위하여 Nusselt 수와 마찰인자를 고찰하였다. 모든 형태의 립에서 속도가 증가할수록 Nusselt 수와 압력강하는 증가하였다. 열전달 향상과 압력강하가 가장 높은 모델은 baffle $90^{\circ}$ 모델이지만, 열전달 특성과 압력강하를 고려하여 나타낸 성능계수에서는 groove $60^{\circ}$ 모델이 가장 크게 나왔다. 따라서 평판형 태양열 집열기에서는 열전달 향상과 압력강하를 항상 동시에 고려한 설계가 필요하다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2001년도 춘계학술대회논문집E
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• pp.398-403
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• 2001

Pressure drop at a helical square duct orifice is numerically evaluated. The orifice is installed at the entrance of a once-through steam generator tube to suppress flow instabilities. The calculated results are compared with the available experimental correlations, and showed good agreement. Effects of curvature ratio and characteristics of the secondary flow with Reynolds number are reported. Through the numerical simulations, pressure drop mechanisms were well understood inside the compact and complicated orifice geometry.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2000년도 춘계학술대회논문집B
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• pp.25-30
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• 2000

Plate and shell heat exchanger(P&SHE) has been applied to the refrigeration and air conditioning systems as evaporators or condensers fur their high efficiency and compactness. The purpose of this study is to analyze the characteristics of pressure drop in plate and shell heat exchanger. An experiment for single phase (low pressure drop in plate and shell heat exchanger was performed. Also numerical work was conducted using the FLUENT code for $ {\kappa}-{\varepsilon}$ model. The dependence of friction factor on geometrical Parameters was numerically investigated. The study examines the internal flow and the pressure distribution in the channel of plate and shell heat exchanger. The results of CFD analysis compared with experimental data, and the difference of frictor factor in plate side and shell side are 10% and 12%, respectively. Therefore, the CFD analysis model is effectively predict the performance of plate and shell heat exchanger.