• 제목/요약/키워드: Local pressure coefficient

검색결과 144건 처리시간 0.024초

헬리컬 코일형 가스냉각기 내 CO2의 냉각 열전달 특성 (Cooling Heat Transfer Characteristics of CO2 in Helical Coil Type Gas Coolers)

  • 손창효;전민주;오후규
    • Journal of Advanced Marine Engineering and Technology
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    • 제31권6호
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    • pp.699-706
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    • 2007
  • The cooling heat transfer coefficient and pressure drop of $CO_2$(R-744) in helical coil copper tubes were investigated experimentally The main components of the refrigerant loop are a receiver, a variable-speed pump, a mass flow meter. a pre-heater and a inclined helical coil type gas cooler (test section). The test section consists of a smooth copper tube of 2.45 and 4.55mm inner diameter The refrigerant mass fluxes were varied from 200 to $600 [kg/m^2s]$ and the inlet pressures of 9as cooler were 7.5 to 10.0 [MPa]. The heat transfer coefficients of $CO_2$ in helical coil tubes increase with the increase of mass flux and gas cooling pressure of $CO_2$. The pressure drop of $CO_2$ in the gas cooler shows a relatively food agreement with those Predicted by Ito's correlation developed for single-phase in helical coil tubes. Though a few correlation available with the data. the local heat transfer coefficient of $CO_2$ agrees well with those presented by Pitla et al. among the predictions. However at the region near pseudo-critical temperature. the experiment data indicate higher values than the Pitla et al. correlation.

원주 후미에 부착된 와동발생기의 영각 변화에 따른 유동 및 열전달 특성 (Flow and Heat Transfer Characteristics due to the Variations of the Angle of Attack at the Vortex Generators located behind a Circular Cylinder)

  • 하홍영;홍철현;양장식;이기백
    • Journal of Advanced Marine Engineering and Technology
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    • 제26권4호
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    • pp.439-449
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    • 2002
  • Experimental investigations of the flow structure and heat transfer enhancement in a channel with a built-in circular cylinder and a wing-let type vortex generator are presented. Without any vortex generators, relatively low heat transfer takes place in the downstream of the circular cylinder where is a recirculation region with low velocity fluid is formed. However with a wing-let type longitudinal vortex generator in the wake region behind the cylinder, heat transfer in the region can be enhanced. In order to control the strength of longitudinal vortices, the angle of attack of the vortex generators is varied from $20^{circ} to 45^{\circ}$, but spacings between the vortex generations are fixed to be 5 mm. The 3-dimensional mean velocity field downstream of the vortex generator is measured by a five-hole pressure probe, and the hue-capturing method using thermochromatic liquid crystals has been used to provide the local distribution of the heat transfer coefficient. The vorticity field and streamwise velocity contour are obtained from the velocity field. Streamwise distributions of averaged Stanton number on the measurement planes show very similar trends for all the experimental cases($\beta=20^{circ}, 30^{circ} and 45^{\circ}$). Circulation strength and heat transfer coefficient have the maximum values when the angle of attack($\beta$) is $30^{\circ}$.

관경별 탄화수소계 냉매의 증발 열전달에 관한 특성평가 (Study on Evaporating Heat Transfer of HCs Refrigerants by Changing of Tube Diameter)

  • 이광배;이호생;문춘군;김재돌;윤정인
    • 한국마린엔지니어링학회:학술대회논문집
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    • 한국마린엔지니어링학회 2005년도 후기학술대회논문집
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    • pp.41-42
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    • 2005
  • The experimental apparatus has been set-up as a conventional vapor compression type heat pump system. The test section is a horizontal double pipe heat exchanger. A tube diameter of 12.70 mm, 9.52 mm, 6.35 mm with 1.78 mm,1.52 mm,1.4 mm wall thickness each is used for this investigation. The local evaporating heat transfer coefficients of hydrocarbon refrigerants were superior to that of R-22. and the maximum increasing rate of heat transfer coefficient was found in R-1270. The average evaporating heat transfer coefficient increased with the increase of the mass velocity and it showed the higher values in hydrocarbon refrigerants than R-22. The highest evaporating heat transfer coefficient of all refrigerants was shown in a tube diameter of 6.35 mm with same mass flux.

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Prediction of Extreme Sloshing Pressure Using Different Statistical Models

  • Cetin, Ekin Ceyda;Lee, Jeoungkyu;Kim, Sangyeob;Kim, Yonghwan
    • Journal of Advanced Research in Ocean Engineering
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    • 제4권4호
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    • pp.185-194
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    • 2018
  • In this study, the extreme sloshing pressure was predicted using various statistical models: three-parameter Weibull distribution, generalized Pareto distribution, generalized extreme value distribution, and three-parameter log-logistic distribution. The estimation of sloshing impact pressure is important in design of liquid cargo tank in severe sea state. In order to get the extreme values of local impact pressures, a lot of model tests have been carried out and statistical analysis has been performed. Three-parameter Weibull distribution and generalized Pareto distribution are widely used as the statistical analysis method in sloshing phenomenon, but generalized extreme value distribution and three-parameter log-logistic distribution are added in this study. Additionally, statistical distributions are fitted to peak pressure data using three different parameter estimation methods. The data were obtained from a three-dimensional sloshing model text conducted at Seoul National University. The loading conditions were 20%, 50%, and 95% of tank height, and the analysis was performed based on the measured impact pressure on four significant panels with large sloshing impacts. These fittings were compared by observing probability of exceedance diagrams and probability plot correlation coefficient test for goodness-of-fit.

원전 Mixing Tee에서의 고주기 열피로 평가 (Evaluation of High Cycle Thermal Fatigue on Mixing Tee in Nuclear Power Plant)

  • 이선기
    • 한국압력기기공학회 논문집
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    • 제16권1호
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    • pp.22-29
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    • 2020
  • In nuclear power plants, there is a risk of thermal fatigue in equipment and piping affecting system soundness because the temperature change of the system accompanies in every operation and shutdown. Therefore, in order to prevent the excess of the fatigue limit during the lifetime of plants, the fatigue limit of each piping material is determined in the designing stage. However, there are many cases where equipment or piping is locally subjected to thermal fatigue that is not considered in the design, resulting in damage to the equipment and piping, and failure during operation. Currently, local thermal fatigue generation mechanisms that are not taken into account in the design stage are gradually being identified. In this paper, the effects of the fluid temperature fluctuations on the piping soundness due to the mixing of hot and cold water, one of the local thermal fatigue generating mechanisms, were evaluated.

와동간의 상호작용이 경계층 및 열전달에 미치는 영향에 관한 연구 ( I ) - Common flow down에 관하여 - (An Experimental Study on the Effects of the Boundary Layer and Heat Transfer by Vortex Interactions ( I ) - On the common flow down -)

  • 홍철현;양장식;이기백
    • 대한기계학회논문집B
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    • 제24권2호
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    • pp.288-297
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    • 2000
  • This paper describes the results of an experimental investigation of the flow characteristics and the heat transfer rate on a surface by interaction of a pair of vortices. The test facility consists of a boundary-layer wind tunnel with a vortex introduced into the flow by half-delta wings(vortex generators) protruding from the surface. In order to control the strength of the two longitudinal vortices, the angles of attack of the vortex generators are varied from 20 degree to 45 degree, but spacings between the vortex generators are fixed to 4 cm. The 3-dimensional mean velocity downstream of the vortex generators is measured by a five-hole pressure probe, and the hue-capturing method using the thermochromatic liquid crystals has been used to provide the local distribution of the heat transfer coefficient. By using the method mentioned above, the following conclusions are obtained from the present experiment. The boundary layer is thinned in the regions where the secondary flow is directed toward the wall and thickened where it is directed away from the wall. The peak augmentation of the local heat transfer coefficient occurs in the downwash region near the point of minimum boundary-layer thickness. Streamwise distributions of averaged Stanton number on the measurement planes show very similar trends for all the cases(${\beta}=20^{circ},\;30^{\circ}\;and\;45^{\circ}$).

채널의 분기 및 병합이 있는 액체로켓 연소기 재생냉각 유로에서의 수력학적 특성 (Hydraulic Characteristics of Branching and Merging of Channels in Regenerative Cooling Passage in Liquid Rocket Combustors)

  • 김홍집;김성구;최환석
    • 한국항공우주학회지
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    • 제36권11호
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    • pp.1087-1093
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    • 2008
  • 고성능 로켓엔진용 연소기에서 열적 건전성을 확보하기 위해 적용되는 재생냉각 채널은 채널의 분기/병합, 방향 전환과 같이 복잡한 유동구조를 포함한다. 냉각유로에서 발생하는 압력 손실을 마찰과 국소유동저항으로 나눠, 각각의 유동조건에 따라 경험적으로 제시된 문헌상의 계수를 적용함으로써, 재생냉각유로 설계에 효과적으로 적용할 수 있도록 수력학적 자료를 구하였다. 해석의 타당성을 검증하기 위하여 실물형 연소기의 냉각유로 설계안에 적용하였다. 먼저, 물을 사용하였을 때 모사시제를 사용한 수류시험 결과와 비교하였다. 정량적으로 타당한 결과를 얻은 것으로 확인되어, 실유체인 케로신을 사용한 수력해석을 수행하여 CFD 결과와 비교하여 수력해석 방법의 타당성을 확인할 수 있었다.

냉각제들에 따른 불연속 발열체의 냉각성능 연구 (Study on the cooling performance of discrete heat sources using coolants)

  • 최민구;조금남
    • 설비공학논문집
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    • 제11권2호
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    • pp.224-235
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    • 1999
  • The present study investigated the effects of the experimental parameters on the cooling characteristics of the multichip module cooled by the indirect liquid cooling method using water, PF-5060, and paraffin slurry. The experimental parameters were coolants including Paraffin slurry with mass fraction of 2.5~7.5%, heat flux of 10~40W/$\textrm{cm}^2$ for the simulated VLSI chips and Reynolds numbers of 3,000~20,000. The size of paraffin slurry was constant as 10~40${\mu}{\textrm}{m}$ before and after the experiment. The chip surface temperatures for paraffin slurry were lower than those for water and PF-5060. The local heat transfer coefficients for the paraffin slurry were larger than those for water and the local heat transfer coefficients reached a row-number-independent and thermally-fully-developed value approximately after the third row. The local Nusselt numbers for paraffin slurry with a mass fraction of 7.5% were larger by 20~38% than those for water. The paraffin slurry with a mass fraction of 5% shelved the best thermal and hydrodynamic characteristics when local heat transfer and pressure drop were considered simultaneously.

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공랭형 수직평판 흡수기 액막에서의 열 및 물질전달에 관한 수치적 연구 (A Numerical Study on Heat and Mass Transfer in a Falling Film of Vertical Plate Absorber Cooled by Air)

  • 김선창;오명도;이재헌
    • 대한기계학회논문집
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    • 제19권4호
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    • pp.1071-1082
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    • 1995
  • Numerical analyses have been performed to obtain the absorption heat and mass transfer coefficients and the absorption mass flux from a falling film of the LiBr aqueous solution which is cooled by cooling air. Heat flux at the wall is specified in terms of the heat transfer coefficient of cooling air and the cooling air temperature. Effects of operating conditions, such as the heat transfer coefficient, the cooling air temperature, the system pressure and the solution inlet concentration have been investigated in view of the local absorption mass flux and the total mass transfer rate. Effects of film thickness and film Reynolds number on the heat and mass transfer coefficients have been also estimated. Analyses for the constant wall temperature condition have been also carried out to examine the reliability of present numerical method by comparing with previous investigations.

원주 주위의 비정상 층류유동과 열전달에 대한 수치해석 (Numerical Analysis for the Unsteady Laminar Flow and Heat Transfer Around a Circular Cylinder)

  • 조석호;남청도;부정숙
    • Journal of Advanced Marine Engineering and Technology
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    • 제15권2호
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    • pp.64-72
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    • 1991
  • The unsteady, two-dimensional laminar flow and heat transfer of an incompressible, constant-property fluid flowing around a circular cylinder are numerically analyzed. The Navier-Strokes equation and the energy equation are solved by the finite difference method. The range of the Reynolds number is 10 to 100 and the Prandtl number considered is 0.7. The contours of the flow pattern, equi-vorticity line and isotherm pattern around a circular cylinder are shown. Also, numerical solutions of the surface vorticity, pressure coefficient, drag coefficient, local Nusselt number and mean Nusselt number are obtained. The numerical results for the final time fo calculation are compared with the other available experimental and theoretical results for the steady state and are found to be in good agreement with them.

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