• Title/Summary/Keyword: Pipe diameter

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Flow Characteristics and Optimal Design for RDT Sparger (원자로배수탱크내 Sparger에 대한 유동특성 및 최적설계)

  • Kim, Kwang-Chu;Park, Man-Heung;Park, Kyoung-Suk;Lee, Jong-Won
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.23 no.11
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    • pp.1390-1398
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    • 1999
  • A numerical analysis for ROT sparger of PWR(Pressurized Water Reactor) is carried out. Computation is performed to investigate the flow characteristics as the change of design factor. As the result of this study, RDT sparger's flow resistance coefficient is K=3.53 at the present design condition if engineering mar&in is considered with 20%, and flow ratio into branch pipe is $Q_s/Q_i=0.41$. Velocity distribution at exit is not uniform because of separation in branch pipe. In the change of inlet flow rate and section area ratio of branch pipe for main pipe, flow resistance coefficient is increased as $Q_s/Q_i$ decreasing, but in the change of branch angle and outlet nozzle diameter of main pipe, flow resistance coefficient is decreased as $Q_s/Q_i$ decreasing. As the change rate of $Q_s/Q_i$ is the larger, the change rate of flow resistance coefficient is the larger. The change rate of pressure loss is the largest change as section area ratio changing. The optimal design condition of sparger is estimated as the outlet nozzle diameter ratio of main pipe is $D_s/D_i=0.333$, the section area ratio is $A_s/A_i=0.2$ and the branch angle is ${\alpha}=55^{\circ}$.

Explicit Equations of Normal Depth for Drainage Pipes (하수관 등류수심 양해법 산정식)

  • Yoo, Dong-Hoon;Rho, Jung-Soo
    • Journal of Korea Water Resources Association
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    • v.38 no.7 s.156
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    • pp.527-535
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    • 2005
  • The computation of normal depth is very important for the design of channel and the analysis of water flow. Drainage pipe generally has the shape of curvature like circular or U-type, which is different from artificial triangular or rectangular channel. In this case, the computation of normal depth or the derivation of equations is very difficult because the change of hydraulic radius and area versus depth is not simple. If the ratio of the area to the diameter, or the hydraulic radius to the diameter of pipe is expressed as the water depth to the diameter of pipe by power law, however, the process of computing normal depth becomes relatively simple, and explicit equations can be obtained. In the present study, developed are the explicit normal depth equations for circular and U-type pipes, and the normal depth equation associated with Hagen (Manning) equation and friction factor equation of smooth turbulent flow by power law is also proposed because of its wide usage in engineering design.

Study on Pullout Behavior of Pipe Anchor (파이프형 앵커의 인발거동에 대한 연구)

  • Bae, Wooseok;Lee, Bongjik;Kwon, Youngcheul;Lee, Jundae
    • Journal of the Korean GEO-environmental Society
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    • v.9 no.1
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    • pp.5-10
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    • 2008
  • In this study, laboratory model test was performed to estimate pullout behavior of pipe type anchor with surface roughness, embedment and diameter. The design of buried pipe anchors in areas of vertical ground movement is governed, in part, by magnitude of the forces imposed on the pipe and displacements at which they are developed. In this paper, uplift resistance and displacement characteristics of pipe anchors caused by ground condition and embedment ratio, surface roughness, pipe diameter through the analysis of pipe anchor model test were compared and analyzed. The test results of the buried pipe showed that as the relative density increases, ultimate uplift resistance increase in 20%. When pipe anchor is failed with the relative density of the ground, the change of surface roughness, it was shown that the deformation increases as the ratio of penetration increases from 2 to 8 in five times approximately. And most anchor-based theories overestimate the breakout factor.

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Performance Analysis of Ground Thermal Conductivity by Ground Heat Exchanger (지중열교환기의 지중열전도도 성능 분석)

  • Kim, Young-Jun;Choi, Jae-Sang;Kang, Yong-Tae
    • Proceedings of the SAREK Conference
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    • 2005.11a
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    • pp.161-166
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    • 2005
  • The objectives of this paper are to estimate the ground thermal conductivity by ground heat exchangers in two different places - Chooncheon and Wonjoo, and to analyze the effect of ground thermal conductivity on the ground thermal diffusivity and the size of the ground heat exchanger. In Chooncheon area, a single-U type HDPE pipe (25mm diameter) with borehole diameter of 150mm, length of 150m is installed. In Wonjoo area, a single-U type HDPE pipe (40mm diameter) with borehole diameter 150mm, length of 200m is installed. It is found that the ground thermal conductivities are estimated as 2.69 $W/m^{\circ}C$ and 2.99 $W/m^{\circ}C$ in Chooncheon and Wonjoo, respectively. It is also found that the ground heat exchanger size is reduced by 8.6% with 25% increase of ground thermal conductivity, and increase by 11.8% with 25% decrease of ground thermal conductivity.

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Unsteady Heat Transfer Analysis of Radiant Heating Panel (복사 난방 패널의 과도 열전달 해석)

  • Lee, T.W.;Kim, H.Y.
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.4 no.3
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    • pp.191-203
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    • 1992
  • To analyze the unsteady heat transfer phenomena in radiant heating panel, a mathematical model was considered. Numerical analysis for solving the governing equations was conducted by using the finite difference method with boundary-fitted meshes. Transient temperature distributions and thermal responses in heating panel were obtained for various design parameters such as pipe pitches, pipe diameters and pipe depths. Experimental results were also obtained to verify the results of calculation.

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A Study on the Pipe Inner Coating by Plasma Processing (원자력 발전용 냉각수 파이프 내부 보호막 코팅기술의 개발에 관한 기초연구)

  • Sung, Y.M.;Park, H.K.;Kim, G.S.;Shin, J.H.;Cho, J.S.;Park, C.H.
    • Proceedings of the KIEE Conference
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    • 1995.07c
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    • pp.1290-1292
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    • 1995
  • A cylindrical-post magnetron sputtering system was designed for pipe inner coating. The discharge condition was depended on the gas pressure, magnetic field and pipe diameter. At given discharge current, discharge voltage increased a little with pipe diameter. The electron temperature and floating potential increased with magnetic field. The impact ion energy on the pipe increased with bias voltage. The TiN thin-film of $2{\mu}m$ thickness was formed by cylindrical-post magnetron sputtering system under the conditions of the pressure of 5mTorr, the applied voltage of 700V, the discharge current of 500mA, the magnetic field of 300G, and the bias voltage of -100V.

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A study on the residual stresses in circumferential welds of the pipes (파이프 원주방향 용접부의 잔류응력 연구)

  • 남궁재관;홍재학
    • Transactions of the Korean Society of Mechanical Engineers
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    • v.15 no.2
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    • pp.693-702
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    • 1991
  • The existence of residual stress in the circumferential butt welded pipes is one of the most important problems concerning stress corrosion cracking in service. In this paper, the residual stress distributions in three kinds of circumferential butt welded pipes were measured by the hole drilling strain gage method and calculation using finite element method is performed and its results are compared with the experiments. At the inner surface of the pipe region near the center line of welding is under high tensile residual stress. However, as the distance from the center line of welding increases, the tensile component decreases and finally becomes compressive residual stress at region far away from the center line of welding. The longitudinal residual stress at the outer surface is compressive regardless of the diameter of pipe and the circumferential stress is changed rom compressive to tensile as pipe diameter increases. The results also demonstrate that the residual stress is mainly caused by self restraint bending force in the pipe welding.

Pipe Network Analysis according to Friction Factor of Commercial Pipe (상용관 마찰계수에 따른 관망해석)

  • Yoo, Dong-Hoon;Wun, Yoo-Seung;Yoon, Kye-Sup
    • Water for future
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    • v.29 no.5
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    • pp.161-172
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    • 1996
  • Studied are the existing equations of Hazen-Williams and Colebrook-White, and the equations of Yoo's (1995) mean zero velocity point and mean friction factor developed for the estimation of commercial pipe friction factor. Simple arrangements of pipe network are devised by changing the diameter, flow discharge and length, and the characteristics of four equations are investigated by comparing the computed results of pressures at each node. Three groups of pipe diameter, small, medium, large, are considered in the comparison, and various problems of existing equations are discussed based on the computed results of pressures and velocities.

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Effect of Air Gap Thickness on Top Heat Loss of a Closed-loop Oscillating Heat Pipe Solar Collector

  • Nguyen, Kim-Bao;Choi, Soon-Ho;Yoon, Doo-Ho;Choi, Jae-Hyuk;Oh, Cheol;Yoon, Seok-Hun
    • Journal of Advanced Marine Engineering and Technology
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    • v.33 no.7
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    • pp.994-1002
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    • 2009
  • In this paper, effect of air gap thickness between absorber plate and glass cover on top heat loss of a closed loop oscillating heat pipe (CLOHP) solar collector was investigated. The CLOHP, which is made of copper with outer diameter of 3.2mm and inner diameter of 2.0mm, comprises 8 turns with heating, adiabatic and cooling section. The heating section of the heat pipe was attached to absorber plate which heated by solar simulator simulated by halogen lamps. The cooling section of the heat pipe was inserted into collector's cooling section that made of transparent acrylic. Temperatures of absorber plate, glass cover, and ambient air measured by K-type thermocouple and were recorded by MV2000-Yokogawa recorder. Top heat loss coefficients and top heat loss of the collector corresponding to some cases of air gap thickness were determined. The result of experiment shows the optimal air gap thickness for minimum top heat loss of this solar collector.

Heat Transfer Characteristics of Liquid-Solid Suspension Flow in a Horizontal Pipe

  • Ku, Jae-Hyun;Cho, Hyun-Ho;Koo, Jeong-Hwan;Yoon, Suk-Goo;Lee, Jae-Keun
    • Journal of Mechanical Science and Technology
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    • v.14 no.10
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    • pp.1159-1167
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    • 2000
  • Particles in liquid-solid suspension flow might enhance or suppress the rate of heat transfer and turbulence depending on their size and concentration. The heat transfer characteristics of liquid-solid suspension in turbulent flow are not well understood due to the complexibility of interaction between solid particles and turbulence of the carrier fluid. In this study, the heat transfer coefficients of liquid-solid mixtures are investigated using a double pipe heat exchanger with suspension flows in the inner pipe. Experiments are carried out using spherical fly ash particles with mass median diameter ranging from 4 to $78{\mu}m$. The volume concentration of solids in the slurry ranged from 0 to 50% and Reynolds number ranged from 4,000 to 11,000. The heat transfer coefficient of liquid-solid suspension to water flow is found to increase with decreasing particle diameter. The heat transfer coefficient increases with particle volume concentration exhibiting the highest heat transfer enhancement at the 3% solid volume concentration and then gradually decreases. A correlation for heat transfer to liquid-solid flows in a horizontal pipe is presented.

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