• 대한기계학회논문집
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• 제14권6호
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• pp.1613-1620
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• 1990

본 연구에서는 일반적인 레이저 유속계를 사용하여 광전 증폭관내에 핀흘 대 신에 슬릿(slit)을 장치하고 광전증폭관을 측정영역에 90˚가 되도록 설치하여 in-situ calibration을 수행함으로써 분무의 입경과 속도를 동시에 계측할수 있다는 Yoon의 결과를 이용하고 모든 입자들의 궤적은 동일한 확률을 갖는다는 Yule와 Holve, Self의 가정을 기초로한 수학적인 Deconvolution에 의하여 계측방법에 발생되는 모순 점을 해결하였다. 일반적으로 분무특성해석을 위해서는 분무를 지배하는 기하학적인 변수, 입경분포, 액적의 속도분포, 밀도분포, 입경과 속도의 상관계수, 입자의 증발율 등이 규명 되어야하는데 본 연구에서는 이상류 동축노즐을 제작하고 이의 분무특성을 해석하기위하여 액적의 속도분포, 입경분포, 입경과 속도의 상관계수, 수밀도분포 등 을 계측하였다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2000년도 춘계학술대회논문집B
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• pp.83-89
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• 2000

This paper presents a pressure drop correlation for evaporation and condensation of alternative refrigerant with oil in micro-fin tubes. The correlation was developed from a data base consisting of oil-free pure and mixed refrigerants in micro-fin tube; Rl25 R134a. R32 R410a(R32/R125 50/50% mass), R22, R407c(R32/R125/R134a, 23/25/52% mass) and R32/R134a(25/75% mass). The micro-fin tube used in this paper had 60 0.2mm high fins with a 18 helix angle. The cross sectional flow area $(A_c)$ was $60.8 mm^2$ giving an equivalent smooth diameter$(D_e)$ of 8.8mm. The hydraulic diameter $(D_h)$ was estimated to the 5.45mm. The new correlation was obtained by replacing the friction factor and the tube-diameter in Bo Pierre correlation by a friction factor derived from pressure drop data for a micro-fin tube and the hydraulic diameter, respectively. This correlation was also used to predict some pressure data with a lubricant after using a mixing viscosity rule of lubricants and refrigerants. As a result, the new correlation was also well predicted to the measured data within a mean deviation of 19.0%.

• 한국해양공학회지
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• 제25권5호
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• pp.15-20
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• 2011

This study carried out a series of experiments involving impact tests (Drop Weight type & Charpy type with a standard specimen and newly designed I-type specimen), hardness tests, and fracture surface observations of French-made roll shell steel (F), abnormal roll shell steel (M), reheated roll shell steel (R), and S25C steel under heat treatment conditiAn experimental study was carried out to study the solid-liquid mixture upward hydraulic transport of solid particles in vertical and inclined annuli with a rotating inner cylinder. The lift forces acting on a fluidized particle play a central role in many important applications such as the removal of drill cuttings in horizontal drill holes, sand transport in fractured reservoirs, sediment transport, the cleaning of particles from surfaces, etc. In this study a clear acrylic pipe was used to observe the movement of solid particles. Annular velocities varied from 0.4 to 1.2 m/s. The effect of the annulus inclination and drill pipe rotation on the carrying capacity of a drilling fluid, particle rising velocity, and pressure drop in a slim hole annulus were measured for fully-developed flows of water and aqueous solutions of CMC (sodium carboxymethyl cellulose) and bentonite. The rotation of the inner cylinder was efficient at carrying particles to some degree. For a higher particle volume concentration, the hydraulic pressure loss of the mixture flow increased because of the friction between the wall and solids or between solids.

• 대한기계학회논문집B
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• 제20권1호
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• pp.266-274
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• 1996

An experimental work was conducted to investigate the characteristics of the onset of flooding in vertical annuli with a direct injection mode using air and water. The onset of flooding was determined by means of pressure drop measurement while the air velocity was increased gradually under fixed liquid flow rates. Data of the onset of flooding were collected for various combinations of the tube size and the nozzle number. A theoretical analysis of the onset of flooding was also performed based on an envelope theory. The result shows that the onset of flooding in small-scale annuli can be predicted relatively well by the theory. A modified Wallis parameter was used to investigate the scaling effect of flooding phenomena in the annuli, indicating a relatively reasonable result. The number of nozzle has no effect on the flooding velocity when liquid was injected through 2, 3, 4 and 6 nozzles but the initiation of flooding was significantly expedited when 12 nozzles were employed for liquid injection.

• 대한기계학회논문집B
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• 제24권5호
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• pp.699-708
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• 2000

To make compact evaporator, experiments that show characteristics of evaporating heat transfer and pressure drop in the helically coiled small diameter tube were taken in this research. The experiments were performed with HCFC-22 in the helically coiled small diameter tube; inner diameter=1.0(mm), tube length=2.0(m), and curvature diameter=31, 34, 46.2(mm). The experiments were also carried out with the following test conditions; saturation pressure=0.588(MPa), mass velocity=$150{\sim}500(kg/m^2s)$, and heat flux=$1{\sim}5(kW/m^2)$. The experiment results are that the empirical correlation to predict heat transfer coefficient for single phase flow in helically coiled small diameter tube was obtained. It was found that dry-out is occurred at low-quality region for evaporation heat transfer because of breaking of annular liquid film. The friction factor of single phase flow of helically coiled tube was agreed with Prandtl's correlation. Finally, It was proposed for correlation that can precisely predict the friction factor of two phase flow of helically coiled tube.

• 대한기계학회논문집B
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• 제24권7호
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• pp.938-944
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• 2000

Recently, micro fin tube is widely used to heat exchanger for high performance. And, as the alternative refrigerants for R-22, hydrocarbons such as R-290, R-600 and R-600a are very promising because of their low GWP and ODP. Thus, R-290 was used as working fluid in this study. Most design of heat exchanger had been based on heat transfer characteristics of pure refrigerant although refrigerant oil exists in the refrigeration cycles. So, the influence of oil on heat transfer characteristics have to be considered for investigating exact evaporation heat transfer characteristics. But, this is an unresolved problem of refrigeration heat transfer. Therefore the influence of the refrigeration oil to the evaporation heat transfer characteristics of R-290 were conducted in a horizontal micro tin tube. The mineral oil was used as refrigeration oil. The experimental apparatus consisted of a basic refrigeration cycle and a system for oil concentration measurement. Test conditions are as the follows; evaporation temperature $5^{\circ}C$, mass velocity 100 $kg/m^2s$, heat flux 10 $kW/m^2$, oil concentration 0, 1.3, 3.3, 5.7 wt.%, and quality $0.07{\sim}1.0$. When refrigeration oil was entered, oil foaming was observed at the low quality region. And, very small bubbles were observed as quality was increased. Pressure drop and heat transfer coefficient increased as the concentration of refrigeration oil increased to 5 wt.%.. The performance index of heat exchanger was the highest near 3.3 wt.%.

• 청정기술
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• 제18권4호
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• pp.410-418
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• 2012

선택적 촉매환원(selective catalytic reduction, SCR) 시스템에서 사용되는 환원제의 효용성을 극대화하기 위해 적용되는 암모니아주입관(ammonia injection gun, AIG) 성능은 유량의 분배, 공기분배다기관(air distribution manifold, ADM)의 배치 그리고 노즐의 배열 및 형상 등에 의해 영향을 받는다. 본 연구에서는 전산유체역학(computational fluid dynamics, CFD) 기법을 이용하여 AIG 성능의 지표가 되는 토출 유량 균일도를 통계적인 수치로 표현하여 관련된 설계인자들과 SCR 시스템의 성능 사이의 상관관계를 평가하고자 하였다. 관내 유동에서 일어나는 유체역학적인 현상의 영향으로 AIG에 대한 공급유량이 증가할 때 각 노즐에서의 토출 유량의 균일도는 감소하는 해석결과를 얻었으며 헤더로부터 가까울수록 분지관으로의 유량분배율이 낮아짐과 동시에 헤더에 가까운 노즐일수록 토출유량이 적어지는 현상을 파악하였다. 각 분지관에 대해 유입 면적대비 노즐의 총 면적비가 0.5 미만일 때 토출 유량의 균일도와 분지관의 유량분배가 매우 균일해지는 것으로 파악되었다.

• 한국자동차공학회논문집
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• 제6권6호
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• pp.113-131
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• 1998

The objective of the present study is to investigate the characteristics of the dividing flow in the laminar flow region. Using glycerine water solution(wt43%) for Newtonian fluid and the polymer of viscoelastic fluid(500wppm) for non-Newtonian fluid, this research investigates the flow state of the dividing tube in steady laminar flow region of the two dimensional dividing tube by measuring the effect of Reynolds number, dividing angle, and the flow rate ratio on the loss coefficient. In T- and Y-type tubes, the loss coefficients of the Newtonian fluid decreases in constant rate when the Reynolds number is below 100. The effect of the flow rate ratio on the loss coefficients is negligible. But when the Reynolds number is over 100, the loss coefficient with various flow rate ratios approach an asymptotic value. The loss coefficient of the non-Newtonian fluid for different the Reynolds number shows the similar tendency of the Newtonian fluid. And when the Reynolds number is over 300, the loss coefficient is approximately 1.03 regardless of flow rate ratio or the dividing angle. The aspect ratio does hardly influence the reattachment length and the loss coefficient of both Newtonian and non Newtonian fluid. The loss coefficient decreases as the Reynolds number increases. The loss coefficient of Newtonian fluid is larger than that of non-Newtonian fluid.

• 한국산학기술학회논문지
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• 제14권3호
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• pp.1003-1010
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• 2013

본 연구에서는 식료품의 진열과 보관에 사용되며 전시효과가 우수한 냉기 강제순환식 쇼케이스의 성능을 예측하는 프로그램을 개발하였다. 압축기의 성능해석에는 제조사에서 제공한 성능선도를 사용하였고 모세관 내 압력손실은 균질유동 모델을 사용하여 계산하였다. 증발기와 응축기는 미소체적으로 구분하여 에너지 균형을 고려하였고 관내측과 공기측 열전달계수는 적절한 상관식으로부터 구하였다. 압축기로 3/4 마력급 왕복동식 2개를 사용하고, 팽창장치로는 내경 1.6 mm의 모세관을, 응축기와 증발기로는 상호 공유형태의 핀-튜브 열교환기를 적용한 쇼케이스 시제품에 대해 성능시험을 수행하고 시험결과와 비교했을 때, 본 프로그램은 시제품의 증발 온도와 응축 온도를 적절히 예측함을 확인하였다.

• 한국화재소방학회논문지
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• 제29권1호
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• pp.53-59
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• 2015

배관시스템의 불안정한 유동에 의해 생성되는 수격현상은 관내 압력의 과도한 변화, 진동 및 소음을 일으킬 수 있다. 이러한 수격현상은 관로, 펌프 및 밸브등의 시설물에 기계적인 사고를 유발시키는 원인이 되기도 한다. 한편, 국내에서는 수격현상으로 인한 피해를 최소화하기 위하여 수격흡수기를 제조 및 사용하여 왔으며, 그동안 별도의 기준이 없어 저가 위주로 생산 및 설치되어 왔다. 따라서, 본 연구에서는 수격흡수기 성능에 대한 최소 가이드라인을 제시하기 위하여, 하나의 배관으로 검증 가능한 시험방법, 수계소화설비에서 수격발생을 가정한 시험방법, 개방충격압과 차단충격압으로 구분한 흡수시험 방법, 배관을 분기한 시험시설 구성 방법 등의 다양한 방법들을 통하여 수격흡수기의 성능을 기준화 할 수 있는 방법등에 대하여 고안하였다. 그리고, 최종적으로는 U자형 배관과 시험용 추를 이용한 간단한 기계적 방식으로 수격흡수기의 수격압 흡수성능을 검증할 수 있는 실험 장치를 최초로 고안하여, 소방용 수격흡수기의 인정기준이 제정되었다.