• 한국소성가공학회:학술대회논문집
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• 한국소성가공학회 2007년도 춘계학술대회 논문집
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• pp.209-212
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• 2007

Rubber compounds have high viscoelastic property. One of the viscoelastic behaviors during profile extrusion is the swelling of extrudate. In this study, die swell of rubber compounds at the capillary die have been investigated through an experiment and computer simulation. They have been performed using fluidity tester in experiment and commercial CFD code, Polyflow in computer simulation. Die swell of rubber compounds for relaxation time at several modes under same conditions with the experiment were predicted using non-linear differential viscoelastic model, Phan-Thien-Tanner (PTT) model. The simulation was analyzed compared with the experiment. Viscoelastic behaviors for pressure, velocity and shear rate distribution were analyzed at the capillary die. It is concluded that the PTT model successfully represented the amount of the optimal die swell of rubber compounds for relaxation time at different modes.

• International Journal of Air-Conditioning and Refrigeration
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• 제8권1호
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• pp.40-49
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• 2000

The capillary tube performance for R-407C is experimentally investigated. The experimental setup is a real vapor-compression refrigerating system. Mass flow rate is measured for various diameter and length while inlet pressure and degree of subcooling are changed. These data are compared with the results of a numerical model. The mass flow rate of the numerical model is about 14% less than the measured mass flow rate. It is found that mass flow rate and length for R-407C are less than those for R-22 under the same condition. Based on this experimental study and the numerical model, a set of design charts for capillary tube of R-407C is proposed.

• 설비공학논문집
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• 제7권3호
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• pp.435-449
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• 1995

In this paper, pressure drop through a capillary tube is modeled to determine the length of a capillary tube for a given set of conditions. HCFC-22 and its alternatives, HFC-134a, R407B, and R410A are used as working fluids. The conditions on which the model is tested are as follows : condensing temperature; 40.0, 45.0, 50.0, $55.0^{\circ}C$, degree of subcooling;0.0, 2.5, $5.0^{\circ}C$, capillary tube exit condition;choked flow, capillary tube diameter;1.2~2.4mm, mass flow rate;5.0~50.0g/sec. The results justify the use of Stoecker's model which yields the results very close to the values in ASHRAE handbook. While McAdams' method yields much better results than Duckler's in calculating the viscosity of the fluid in 2-phase, the friction factor suggested by Stoecker seems to be the best for capillary tubes of large diameter used in residential air conditioners. For each refrigerant, 372 data with various variables are calculated by the model. The results show that capillary tube length varies very uniformly with changes in condensing temperature and degree of subcooling. Based on this fact, regression analysis is performed to determine the dependence of mass flow rate on the length and diameter of a capillary tube, condensing temperature, and degree of subcooling. Thus determined correlation yields a mean deviation of 2.36% for 1,488 data, showing an excellent agreement.

• 한국막학회:학술대회논문집
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• 한국막학회 2001년도 제14회 심포지엄 : 제2회 분리막 표준화(The 2nd Standardization of Membranes)
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• pp.39-50
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• 2001

The performance of membranes is governed their pore struture. Pore structures of porous materials can be determined by a number of techniques. However, The novel technique, capillary folw porometry has a number of advantages. In this technique, the sample is brought in contact with a liquid that fills the pores in the membrane spontaneously. Gas under pressure is used to force the liquid from the pores and increase gas flow. Gas flow rate measured as a function of gas pressure in wet and dry samples yield data on the largest pore size, the mean flow pore size, flow distribution and permeability. Pore characteristics of a number of membranes were measured using this technique. This technique did not require the use of any toxic material and the pressure employed was low. Capillary flow porometry is a suitable technique for measurement of the pore structure of many membranes.

• 대한기계학회논문집B
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• 제27권1호
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• pp.17-24
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• 2003

A mathematical model of the hydrodynamic and heat transfer performances of two-phase flow (gas-liquid) in thin film region of micro channel is proposed. For the formulation of modeling, the flow of the vapor phase and the shear stress at the liquid-vapor interface are considered. In this work, disjoining pressure and capillary force which drive the liquid flow at the liquid-vapor interface in thin film region are adopted also. Using the model, the effects of the variations of channel height and heat flux on the flow and heat transfer characteristics are investigated. Results show that the influence of variation of vapor pressure on the liquid film flow is not negligible. The heat flux in thin-film region is the most important operation factor of micro cooler system.

• 대한화학회지
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• 제38권2호
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• pp.151-159
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• 1994

기체시료 채취기와 짧은 모세관 컬럼(내경 0.32 mm, 길이 3 m), 광이온화 검출기 및 진공펌프로 구성되어, 컬럼의 출구 압력이 대기압보다 낮은 압력에서 조작되는 휴대용 기체 크로마토그래피 시스템을 개발하였다. 컬럼의 규격은 Golay식을 이용한 계산 결과를 기초로 선택하였으며, 조작압력비(컬럼입구와 출구압력비)는 1.03~1.2의 범위가 적절하였고, 이 조건에서 0.87∼4.63 ml/min의 걸럼유량을 얻을 수 있었다. 구경이 다른 3개의 튜브로 구성된 기체시료 채취기는 자동으로 기체시료를 직접 컬럼에 빠른 속도로 반복하여 도입할 수 있으며, 좋은 재현성을 나타내었다. 컬럼출구 압력이 대기압 이하에서 조작되며 짧은 모세관 컬럼을 사용하는 기체 크로마토그래피는 최적 컬럼유량이 일반적인 크로마토그래피보다 커 신속한 분석이 가능하여, 40초 이내에 m-xylene 과 o-xylene의 바탕선 분리가 가능하였다. 시스템의 분리능력에 영향을 주는 인자는 시료 채취시간, 컬럼의 길이와 내경 및 조작압력비였고, 벤젠 유도체들을 사용하여 이들의 영향을 검토하였다.

• 한국식품과학회지
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• 제34권5호
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• pp.787-791
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• 2002

수입자유화이후 유입량이 급증한 농산물중 하나인 율무의 원산지 판별을 위하여 CE의 적용가능성을 검토하였다. 분석을 위한 지표물질의 추출을 위해 30% ethanol을 사용하였으며, $50\;{\mu}m\;I.D.{\times}27\;cm$(20 cm inlet to detector)의 capillary를 이용하여 $45^{\circ}C$, 15 kV로 200 nm에서 detect 하였다. 분석 buffer는 0.1 M phosphate buffer(pH 2.5)에 30% methanol과 26 mM HSA를 첨가하였으며, pressure injection 20초, detector rise time 0.1초로 하였다. 분석시 초기에 증류수와 0.1 M phosphate buffer(pH 2.5)로 각 5분씩 capillary를 rinse하고 분석 buffer로 10분간 equilibration 시킨 후 30분간 분석하고 다시 1 M phosphoric acid로 14분간 rinse하여 다음 시료 분석시의 오차를 줄였다. 이 조건으로 2000년 및 2001년의 국산 및 수입산 율무 총 240점을 분석한 결과 서로를 구분하는 peak JT5의 도출이 가능하였으며 이 peak JT5에 의한 국산 및 수입산 율무의 판별율은 2000년 시료에서는 국산이 총 47점 중 39점(판별율 약 83%), 수입산은 총 48점 중 39점(판별율 약 81%), 2001년 시료는 국산 총 74점 중 60점(판별율 약 81%), 수입산은 총 71점 중 59점(판별율 약 83%)이었으며 전체적으로 약 82%의 판별율을 나타내었다.

• 설비공학논문집
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• 제21권3호
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• pp.140-148
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• 2009

Capillary tubes are widely used as expansion device in small refrigeration systems. The refrigerant flowing in the capillary tube experiences frictional and accelerational head losses and flashing simultaneously. In this paper flow characteristics of adiabatic capillary tubes were simulated with various friction factor models, two-phase viscosity models, and two-phase frictional multiplier models. The predicted pressure distribution and mass flow rate are compared with experimental data reported in literature. It is confirmed that the predicting accuracy with homogeneous model can be improved by employing suitable correlations of friction factor, two-phase viscosity and two-phase frictional multiplier.

• 한국광물학회지
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• 제9권1호
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• pp.17-25
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• 1996

Usual experimental adsorption isotherms as a function of relative humidity were constructed from adsorbed water contents in soils, which were kept more than 2 days in vacuum desiccators with constant humidities controlled by sulfuric acids of various concentrations. From the experimental data, the adsorption surface areas were calculated on the basis of the existing adsorption theory, such as Langmuir, BET, and Aranovich. Based on the Gibbs function describing chemical potential of perfect gas, the relative humidities in the desiccators were transformed into their chemical potentials, which were assumed to be the same as the potentials of equilibratedly adsorbed water in soils. Moreover, the water potentials were again transformed into the equivalent capillary pressures, heads of capillary rise, and equivalent radius of capillary pores, on the basis of Laplace equation for surface tension pressure of spherical bubbles in water. Adsorption quantity distributions were calculated on the profile of chemical potentials of the adsorbed water, equivalent adsorption and/or capillary pressures, and equivalent capillary radius. The suggested theories were proved through its application for the prediction of temperature rise of sulfuric acid due to hydration heat. Adsorption heat calculated on the basis of the potential difference was dependant on various factors, such as surface area, equilibrium constants in Langumuir, BET, etc.

• 한국전산유체공학회지
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• 제14권1호
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• pp.70-77
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• 2009

In this study, time-dependent numerical analysis was carried out to investigate the plasma jet impingement on a flat plate, and a compressible form of two-dimensional inviscid gas dynamics equations were solved using the flux corrected transport algorithm. The mathematical modeling of Joule heating in the polycarbonate capillary bore and the mass ablation from the bore wall was incorporated in the numerical analysis and the series of computation was performed for three cases depending on the distance of the opposing plate from the capillary exit. The computational results reveal that the presence of the opposing plate does not affect the flow conditions inside the capillary when compared to the case of open-air plasma discharge. In the exterior region, the flow structure shows the typical supersonic underexpanded jet which consists of the strong Mach disk in front of the opposing plate and the barrel shock at the side of the jet. It is found that the shock evolution becomes more quasi-steady when the plate distance decreases. Also, the effects of the distance between the capillary bore exit and the opposing plate on the flow conditions along the opposing plate are investigated and the pressure variation on the plate shows more complicated interaction between the plasma discharge and the opposing plate when the location of plate becomes closer to the capillary exit.