• 한국수소및신에너지학회논문집
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• 제18권2호
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• pp.189-196
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• 2007

The evaporation heat transfer coefficient and pressure drop of $CO_2$(R-744) in a horizontal tube was investigated experimentally. The main components of the experimental apparatus are a receiver, a variable-speed pump, a mass flow meter, a pre-heater and an evaporator(test section). The test section consists of a horizontal stainless steel tube of 4.57 mm inner diameter. The experiments were conducted at mass flux of $200{\sim}1000\;kg/m^2s$ saturation temperature of $0{\sim}20^{\circ}C$, and heat flux of $10{\sim}40\;kW/m^2$. The test results showed that the heat transfer coefficient of $CO_2$ has a greater effect on nucleate boiling more than convective boiling. Mass flux of $CO_2$ does not affect nucleate boiling too much. In comparison with test data and existing correlations, All of the existing correlations for the heat transfer coefficient underestimated the experimental data. However lung et al.'s correlation showed a good agreement with the experimental data. The evaporation pressure drop of $CO_2$ increases with increasing mass flux and decreasing saturation temperature. When comparison between the experimental pressure drop and existing correlations. Existing correlations failed to predict the evaporation pressure drop of $CO_2$.

• 수산해양교육연구
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• 제14권2호
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• pp.177-190
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• 2002

An experimental study was carried out to make clear heat transfer characteristics in flow boiling of binary mixtures of refrigerants R134a and R123 in a uniformly heated horizontal tube. Experiments were run at a pressure of 0.6 MPa both for pure fluids and mixtures in the ranges of heat flux $10{\sim}50{kW/m}^2$, vapor quality 0~100% and mass flux 150-600 $kg/m^2s$. Heat transfer coefficients of mixtures were reduced compared to the interpolated values between pure fluids both in the low quality region where the nucleate boiling is dominant and in the high quality region where the convective evaporation is dominant. Total pressure drop during two-phase flow boiling in a horizontal tube consists of the sum of two components, that is, the frictional pressure drop and pressure drop due to acceleration. The frictional pressure drop is the most difficult component to predict, and makes the most important contribution to the total pressure drop. On the other hand, the acceleration pressure drop resulting from the variation of the momentum flux caused by phase change is generally small as compared to the frictional pressure drop. There is no significant difference in measured pressure drop between mixtures and pure fluids. The correlation of Martinelli and Nelson predicted most of the present data both for pure and mixed refrigerants within 30%.

• 대한기계학회논문집B
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• 제30권11호
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• pp.1035-1042
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• 2006

An experimental investigation was performed to study two-phase pressure drop of deionized water in a microchannel. Measurement and evaluation of two-phase frictional pressure gradient were carried out using a single horizontal rectangular microchanne1 having a hydraulic diameter of $100{\mu}m$. Tests were performed for mass fluxes of 90, 169, and 267 $kg/m^2$s and heat fluxes of 200-700 $kW/m^2$. Test results showed that the measured two-phase frictional pressure gradient increased with the mass flux and vapor quality. Most macro-channel correlations of two-phase frictional pressure gradient did not provide reliable predictions except under certain limited conditions.

• Journal of Advanced Marine Engineering and Technology
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• 제20권4호
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• pp.70-80
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• 1996

Experimental results for forced convection condensation of R-22 and R-407C inside 7.5mm ID and 4000mm length of horizontal tubes are presented. The experimental data covered total flow rate from 114.3 to 267.1kg/($m^2$.s) and quality from 0 to 1. The vapor temperature and pressure drop along the tube were measured. The pressure drop for R-407C increased with flow rate similar to that of R-22. The experimental data compared with the available perdictions for pressure drop. Based on the data a prediction method was presented for the calculation of pressure drop of R-22 alternative refrigerants.

• 한국철도학회:학술대회논문집
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• 한국철도학회 2008년도 추계학술대회 논문집
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• pp.964-972
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• 2008

In the retaining wall design process, track and train loads are usually considered as uniform surcharge loads and strip loads. In this paper, the lateral(horizontal) earth pressure on retaining structures caused by track and train load are calculated using the Boussinesq solution. And also total horizontal force per unit length and the location of the resultant force were estimated with the changes of loading locations and widths of the loadings. The maximum horizontal earth pressure and the location of it for high-speed train load were 11.83kPa and 1.7m at the loading condition 2m away from retaining walls.

• 한국산학기술학회논문지
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• 제18권1호
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• pp.1-7
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• 2017

RAR(Reinforced Abutment for Railways)은 뒤채움을 선 시공하고, 교대를 후 시공하여 접속부의 침하와 교대 수평토압 및 변위를 저감할 수 있는 교대 구조로 교대 구체 및 저판의 사이즈와 말뚝의 설치 수를 줄인 경제적인 교대 구조이다. 본 논문에서는 말뚝 설치 수에 따른 RAR의 성능을 수치 해석을 이용하여 평가하였다. 말뚝의 설치 수를 1~4열을 적용한 RAR을 지반 변형계수를 달리한 조건에 대하여 수치 해석을 수행하고, 그 결과를 동일한 지반 조건에서 기존 교대의 수치해석결과와 비교, 분석하였다. 해석결과 말뚝 설치 수를 증가시키는 경우 접속부 침하저감 효과는 비교적 크지 않았고, 교대수평변위 및 토압 저감에 더 효과적인 것으로 나타났다. 말뚝 설치 열 수가 1~4열로 변할 때 RAR의 수평변위는 기존교대의 26~37%, 수평토압은 59~83%수준으로 말뚝 설치수가 증가할수록 기존교대(말뚝5열)에 비해 수평변위와 토압을 크게 저감할 수 있는 것으로 나타났다. 또한 RAR의 수평 토압은 보강재, 말뚝, 기초저판, 원지반 강성 등의 영향을 복합적으로 받는 것으로 평가되었다.

• 산업기술연구
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• 제21권A호
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• pp.293-301
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• 2001

This paper is experimental results of investigating the efficiency of horizontal vacuum drainage system. Effects of size and shape of drain on horizontal vacuum drainage were studied. Model tests in the laboratory with soft marine clay were carried out with drain pipe of having three different diameters and PBD (Plastic Board Drain) of strip shape so that consolidation settlement of soft clay due to applied vacuum pressure, amount of discharge, ground settlement and distributions of pore pressure and undrained shear strength were measured during testing. From results of model test, amount of discharge due to vacuum pressure was increased with the diameter of pipe drain whereas the drain efficiency of pipe in per unit area of drain surface was decreased with diameter of pipe. The rate of discharge per unit time was reduced very fast with diameter of pipe. Settlement of ground surface with time was increased with diameter of pipe as a result of increase of discharge to drain pipe.

• 대한토목학회논문집
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• 제38권1호
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• pp.63-71
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• 2018

본 연구에서는 베인에 작용하는 수평응력과 토크를 측정한 다음 이를 이용하여 모래의 마찰각을 구하는 연구를 수행하였다. 건조한 낙동강모래를 원통형 셀에 느슨하거나 조밀한 상태로 성형한 다음 상부에서 공기압 실린더로 상재하중(overburden pressure)을 25, 50, 75 또는 100kPa 가하여 베인(직경 5cm, 높이 10cm) 회전 시 주변에 작용하는 수평응력과 토크를 실시간으로 측정하였다. 베인 회전에 따른 최대 토크값은 느슨한 모래는 3.5~9.5Nm, 조밀한 모래는 7.4-17.6Nm 사이로 상재하중이 증가할수록 최대 토크값도 증가하였다. 조밀한 정도에 관계없이 $14-20^{\circ}$ 회전 시 최대 토크값에 도달하였으며, 베인날과 토압계의 초기 위치에 따른 최대값의 차이는 나지 않았다. 상재하중에 따라 베인에 작용하는 초기 수평응력비($K_0$)는 평균 0.33-0.35 사이이며, 베인 회전에 따라 수평응력이 전반적으로 증가하다가 모래 입자가 교란되면서 다시 감소하는 경향을 보였다. 실시간으로 측정된 수평응력과 토크를 이용하여 계산된 마찰각은 상재하중이 증가함에 따라 감소하는 경향을 보였으며, 느슨한 모래는 직접전단시험 결과와 유사한 마찰각을 보였다. 하지만, 조밀한 모래의 마찰각은 다소 과대평가하는 경향을 보였다.

• 한국산학기술학회논문지
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• 제20권12호
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• pp.519-524
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• 2019

본 연구에서는 대풍량 곡물건조기에 사용되는 수평형 집진기의 집진효율 향상과 최적화를 위한 연구의 선행과정으로 Computational Fluid Dynamics(CFD)를 이용하여 집진기 내부의 유동 특성 분석과 원뿔형 허브의 각 변화가 집진기의 집진성능에 미치는 영향을 해석하였다. 최근 집진기 입구에 원뿔형 허브와 고정 베인을 설치하여 선회유동(Swirl Flow)을 발생시켜 이물질을 공기와 분리시키는 수평형 사이클론 집진기(Horizontal type Cyclone Dust collector)가 개발되었다. 이 집진기는 크기가 비교적 작고 설치가 용이하고 비교적 배압이 낮아 추가 동력을 필요로 하지 않으며 베인의 선회력을 이용하기 때문에 대풍량 배습용 송풍기에도 적용할 수 있는 장점을 가지고 있다. 그러나 수평형 집진기 형상으로 인해 발생하는 집진기 내부의 배압 문제와 분진 퇴적 문제를 해결하기 위해서 3차원 유동해석을 이용하여 집진기 내부 형상 변화에 따른 유동 특성에 관한 연구를 진행하였다. 실제 곡물건조기에 적용 가능한 수평형 집진기 설계를 위한 기초 자료를 제공하였으며, 향후 연구 예정인 고정 베인 설계, 주분리관 및 중간분리관의 설계에 적용하고자 한다.

• 조명전기설비학회논문지
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• 제29권1호
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• pp.64-69
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• 2015

This study investigates the Horizontal surface discharge characteristics of solid insulators by varying their materials, and the dew-point of dry-air. The methodology of this study is that a quasi-uniform field is first applied to a test chamber. Then, the chamber is filled with dry-air as an insulation gas which pressure is varied from 1 to 6atm while applying an AC voltage to the chamber. The used solid insulators are teflon, polyethlene and polyurethane. As the dew-point is lower and the pressure of dry-air is higher, the flashover voltage of all solid insulators increases more. When each characteristic of the solid insulators is compared under the same gas pressure, the flashover voltage of teflon is the highest. Then, the flashover voltage of polyethlene is higher than that of polyurethane. Moreover, it is observed that the flashover voltage increases as the horizontal distance between the electrodes of each solid insulator become larger, respectively. However, as the pressure is increased, flashover voltage of the solid insulators is saturated. Therefore, selection of cost-effective insulation is needed in order to appropriate pressure.