• 한국유체기계학회 논문집
• /
• 제19권2호
• /
• pp.36-42
• /
• 2016

Mass flow amplifier, which is an aerodynamic device, makes air flow increased by ejecting small amount of compressed air with $Coand{\breve{a}}$ effect. In this study, the flow characteristics of a mass flow amplifier were studied with various flow conditions and geometrical configurations. In order to improve the performance of mass flow amplifier, various values of clearance, diffuser angle and the aspect ratio of induced flow inlet to outlet were considered as design parameter. Furthermore, four different pressure conditions of compressed air were also considered. Numerical study was performed using the commercial CFD code, ANSYS CFX 14.5 with shear stress transport(SST) turbulent model. The results of pressure and velocity distributions were graphically depicted with different geometrical configurations and operating conditions.

• 설비공학논문집
• /
• 제13권5호
• /
• pp.398-410
• /
• 2001

The flow and heat transfer characteristics for three-dimensional mixed convection flows in a radiator flat tube with U--shaped grooves are analyzed numerically. The flow and temperature fields are calculated by using the modified SIMPLE algorithm for irregular geometry. One tube specification among the various flat tube exchangers is recommended by considering the heat transfer and pressure drop. The effects of variation of coolant flow conditions and external air conditions on the flow and the thermal characteristics for the selected tube are investigated. the results show that inlet velocity of coolant flow is the very important factor in heat transfer and pressure drop, and top side is better position than the others as fin cleave to tube.

• 비파괴검사학회지
• /
• 제31권5호
• /
• pp.479-486
• /
• 2011

의료영상을 기반으로 한 경동맥 분기부 혈류유동장 전산유체역학 해석의 수행에 있어 입구부 경계 조건 도출을 위한 환자 특정 시간 변동 상세 유속 분포를 얻는 것은 일반적으로 쉽지 않다. 그러므로 대부분의 경우 계측된 혈류량을 바탕으로 이상적인 축대칭 완전발달 유속 분포를 적용하게 된다. 그러나 MRI로 직접 계측한 총경동맥 혈류 유속분포를 적용한 기존의 연구에서 입구부 유속분포 경계 조건이 경동맥 분기부 혈류 유동장 해석 결과에 중요한 영향을 미친다는 것을 보였으며, 특히 계측된 혈류 유속분포가 전형적인 Dean type 유동과 다른 독특한 형태를 가진다는 것을 보고하였다. 본 연구에서는 이러한 독특한 형태의 유속 분포가 경동맥 입구부 형상의 이차곡률에 의해 생성됨을 보이고, 직접 경동맥 분기부 유동장 CFD 해석의 경계 조건으로 적용하여 이의 영향을 조사하였다. 이를 통하여 충분한 길이의 실제 경동맥 입구부 형상을 적용 할 경우, 입구부 경계 조건의 영향이 의료영상으로 부터 혈관 형상을 도출하는 과정에서 불가피하게 유기되는 영상 처리 오차에 의한 영향에 비해 상대적으로 크지 않음을 알 수 있었다.

• 대한기계학회논문집
• /
• 제12권6호
• /
• pp.1399-1406
• /
• 1988

본 연구에서는 수로의 폭이 작고(W=74mm) H$_{w}$/H$_{g}$가 5.0~16.7의 범 위인 경우에 레이져 유속계를 이용하여 주어진 유동조건, 예컨대, 유입유속, 입구게이 크(gate)의 높이, 수위, 배플의 유. 무및 높이, 그리고 배플의 위치등에 따라서 액체 속도의 분포가 어떻게 변화하는가를 정성적으로 관찰해 보고자 하는데 주안점을 두었 다. 본 실험 결과는 차후에 계속될 후래시 증발현상에 관한 실험및 해석적 접근에 관한 기초 자료로서 활용하는데에도 그 목적이 있다.다.

• 한국해안·해양공학회논문집
• /
• 제31권1호
• /
• pp.9-16
• /
• 2019

유속의 크기와 블레이드의 기하학적 형상 변화에 따라 발생하는 조류발전용 쉬라우드 시스템 내 유속 변화를 분석하기 위하여 수리모형실험과 수치해석적 방법을 이용하였다. 모형실험을 통해 시스템의 유입부에서 유속 변화와 블레이드 형상변화에 따른 고유 회전수를 계측하였으며, 수치해석을 통해 쉬라우드내 유속 변화를 분석하였다. 실험 유속이 약 28% 증가하고, 익형의 형상을 적용하였을 때, 쉬라우드 유입부에서 계측된 유속은 최대 약 56% 증가하는 경향을 보였다. 한편, 익형 형상을 적용한 블레이드가 설치된 경우 유입부에서의 유속은 일반 블레이드에 비해 최대 14% 증가하는 경향을 보였으며, 회전수 역시 동일 조건에서 가장 높은 수치를 보였다. 수리실험과 수치해석 결과는 약 13%의 오차를 보였으며, 각각의 결과에서 보이는 유속 변화에 대한 경향은 유사하다. 쉬라우드 내 유속 변화를 수치해석으로 분석한 결과 유입부 대비 블레이드 앞부분에서 유속은 최대 1.7배 증가하는 경향을 보였다. 본 연구를 통해 얻은 시스템 내 유속 변화 분석 결과는 효율적인 조류발전용 쉬라우드 시스템 개발에 필요한 기초 자료를 제시할 수 있을 것으로 판단된다.

• 한국연소학회:학술대회논문집
• /
• 한국연소학회 2002년도 제24회 KOSCO SYMPOSIUM 논문집
• /
• pp.85-94
• /
• 2002

Computational flow dynamics(CFD) has been frequently applied to the waste incinerators to understand the flow performance for various design and operating parameters. Though it needs many simplifications and complicated flow models, the reasonability of its results is not fully evaluated. For example, the inlet condition is calculated from an arbitrarily assumed properties of combustion gas release from the waste bed, since the combustion in the bed is difficult to be predicted. In this study, the computational modeling and calculation procedures of CFD for the grate type waste incinerator were evaluated using comparative simulations. Though the assumption method on the generation of the combustion gas directly affected the temperature and gas species concentrations, the overall flow pattern was dominated by the secondary air jets. The gaseous reaction could be included by assuming the release of the products of incomplete combusion from the bed. However, the reaction effficiency cannot not be directly evaluated from the species concentration, since it is not possible to simulate the actual co-existence of fuel rich or oxygen rich puffs over the bed. In predicting the turbulence, the higher order model, such as Reynolds stress model, gave difference shape of local recirculation zones, but similar results was acquired from the standard $k-{\varepsilon}$ model. Introducing radiation model was required for accurate temperature prediction, but it also caused heat imbalance due to the fixed temperature of the inlet, i.e. the waste bed. Thus, the computational modeling procedures on incinerators and the analysis of the predicted results should be progressed carefully. Though not validated experimentally, current simulation method is capable of comparative evaluation on the flow-related parameters such as the furnace shape and secondary air injection using identical inlet conditions. Quantitative analysis using measures of the residence time and mixing is essential to compare the flow performance efficiently.

• 한국지열·수열에너지학회논문집
• /
• 제13권1호
• /
• pp.1-6
• /
• 2017

In this paper, the flow characteristics of water in the water supply pipes of a WBC array were evaluated. We simulated the flow velocities and pressures for a standard pipe, an expansion pipe with a concentric reducer, and an expansion pipe with an eccentric reducer using computational fluid dynamics. In the case of the standard pipe, when the inlet flow velocities were 0.5 m/s and 2.0 m/s, the maximum flow velocities at the center of the WBC array were 0.54 m/s and 2.74 m/s, respectively, which were the greatest values among those of all the pipe models considered. In the case of the expansion pipe, the maximum flow velocities at the center of the WBC array were almost the same under the same conditions regardless of the type of reducer. The pressure losses in the pipe due to the concentric and eccentric reducers were found to be (165.09 ${\times}$ inlet $velocity^{1.6677}$) and (210.98 ${\times}$ inlet $velocity^{1.6478}$), respectively. The coefficient of determination at this time was greater than 0.99 and was the same for both the models. As a simulation result, it was found that in order to reduce the pressure loss when pipe with WBC array is connected with a conventional pipe, diameter of the pipe with WBC array at that section should be enlarged by one step, and then connected to the conventional pipe with a concentric reducer.

• 한국전산유체공학회지
• /
• 제10권2호
• /
• pp.30-37
• /
• 2005

To evaluate LBM we performed the simulation of the unsteady two dimensional flow over a square cylinder in a channel in moderate Reynolds number range, $100\~500$ by using LBM and Fractional-Step method. Frist of all we compared LBM solution of Poiseuille flow applied Farout and periodic boundary conditions with the analytical solution to verify the applicability of the boundary conditions. For LBM simulation the calculation domain was formed by structured 500x100 grids. Prescribed maximum velocity and density inlet and Farout boundary conditions were imposed on the in-out boundaries. Bounceback boundary condition was applied to the channel and the cylinder waifs. The flow patterns and vortex shedding strouhal numbers were compared with previous research results. The flow patterns by LBM were in agreement with the flow pattern by fractional step method. Furthermore the strouhal number computed by LBM simulation result was more accurate than that of fractional step method through the comparison of the previous research results.

• 대한기계학회논문집
• /
• 제19권3호
• /
• pp.834-845
• /
• 1995

An experimental study is made in a nearly two-dimensional 90.deg. curved duct to investigate the effects of interaction between streamline curvature and mean strain on turbulence. The initial shear at the entrance to the curved duct is varied by an upstream shear generator to produce five different shear conditions ; a uniform flow (UF), a positive weak shear (PW), a positive strong shear(PS), a negative weak shear (NW) and a negative strong shear(NS). With the mean field data of the case UF, variations of the momentum thickness, the shape factor and the skin friction over the convex(inner) surface and the concave (outer) surface are scrutinized quantitatively in-depth. It is found that, while the pressure loss due to curvature is insensitive to the inlet shear rates, the distributions of wall static pressure along both convex and concave surfaces are much influenced by the inlet shear rates.

• 한국정밀공학회:학술대회논문집
• /
• 한국정밀공학회 2003년도 춘계학술대회 논문집
• /
• pp.1022-1025
• /
• 2003

Although the globe is the most typical valve to control high pressure drop in piping system, it is very hard to figure out the characteristics of flow field in the globe valve caused by its complex geometry. So there is very few studies to find out flow characteristics of globe valve. In this study, numerical analysis for flow field in the globe valve is carried out using the Fluent code which is commercial CFD program. Pressure drop through the globe valve is also measured to verify the results come from numerical analysis. Comparing experiment with numerical analysis, two results are very close to each other. Also finite element method is employed to evaluate the safety of globe valve using the results coming from the flow analysis to make the boundary conditions for FEM analysis. Maximum stress appears on the inlet channel of valve where inlet flow runs against. Because the maximum stress between 11.7 MPa to 3.6 MPa is within 3.4% of yield stress. the structural safety of valve is considered to be very sound