• Journal of Mechanical Science and Technology
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• 제14권12호
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• pp.1365-1375
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• 2000

Two phase flows have been numerically calculated to analyze plume characteristics and liquid circulation in gas injection through a porous plug. The Eulerian approach has been for formulation of both the continuous and dispersed phases. The turbulence in the liquid phase has been modeled using the standard $textsc{k}$-$\varepsilon$ turbulence model. The interphase friction coefficient has been calculated using correlations available in the literature. The turbulent dispersion of the phase has been modeled by the "dispersion Prand시 number". The predicted mean flows is compared well with the experimental data. The plume region area and the axial velocities are increased with the gas flow rate and with the decrease in the inlet area. The turbulent intensity also shows the same trend. Also, the space-averaged turbulent kinetic energy for various gas flow rates and inlet areas has been obtained. The results are of interest in the design and operation of a wide variety of materials and chemical processing operations.

• 항공우주기술
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• 제8권1호
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• pp.17-25
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• 2009

복사전달식에서 흡수 계수의 정확한 계산은 액체 엔진 저부의 단열재 설계의 입력 값으로 사용되는 플룸의 복사 열전달을 예측하는데 매우 중요하다. 이를 위해서 가스 흡수 계수를 직접 모델링 할 수 있는 WNB 모델을 중요 인자의 선정을 위주로 설명하였고, 그 결과를 비교적 정확한 기준 값을 제공하는 SNB의 결과와 비교하였다. 비교 인자들은 총 방사율, 좁은밴드 복사강도 및 총 복사강도이며, 결과적으로 방사율의 경우 주어진 조건에서 3.1% 이내, 총 복사 강도역시 5%이내의 계산결과를 보여 이 모델의 타당성을 확인할 수 있었다. 추가적으로, 액체 엔진의 연소가스들의 성분비를 예측하고 이 조건에 대한 가스모델링 인자를 계산하여 데이터베이스를 구축하였다.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2006년도 제26회 춘계학술대회논문집
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• pp.57-60
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• 2006

액상의 환경으로 고속의 기체가 분사될 때 기체-액체 표면에서 일어나는 불안정성에 대해 점성전위 유동의 이론을 이용하여 분석하였다. 기체의 속도가 낮을 경우 액상으로 기포로 형성되지만 속도가 증가하면서 기체는 제트의 형태로 변하게 되는데, 천음속 구간에서 제트로 변하게 되는 것으로 알려져 있다. 본 연구에서는 주로 액체 제트를 해석하는데 사용된 점성전위유동이론을 기체 제트의 불안정성 해석에 응용하였다. 천음속 구간에서 기체 제트의 성장률이 변하는 것을 확인하였다. 초음속 구간으로 가면서 성장률이 감소하는 것을 확인하였다. 그리고 이를 레이놀즈수와 같은 무차원수에 대해 기체 제트의 성장률의 변화에 대해 알아보았다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2002년도 학술대회지
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• pp.393-396
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• 2002

Submerged gas-injected system can be applied to various industrial field such as metallurgical and chemical processes, So this study aims at presenting the relevant relationship between gas phase and liquid phase in a gas-injected bath. In a cylinderical bath, local gas volume fraction and bubble frequency were measured by electroconductivity probe and oscilloscope. The temperature of each phase was measured using thermocouple and data acquisition system. In vertical gas injection system, gas-liquid two phase plume was formed, being symmetry to the axial direction of injection nozzle and in a shape of con. Lacal gas-liquid flow becomes irregular around the injection nozzle due to kinetic energy of gas and the flow variables show radical change at the vicinity of gas(air) injection nozzle As most of the kinetic energy of gas was transferred to liquid in this region, liquid started to circulate. In this reason, this region was defined as 'developing flow region' The Bubble was taking a form of churn flow at the vicinity of nozzle. Sometimes smaller bubbles formed by the collapse of bubbles were observed. The gas injected into liquid bath lost its kinetic energy and then was governed by the effect of buoyancy. In this region the bubbles which lost their kinetic energy move upward with relatively uniform velocity and separate. Near the gas nozzle, gas concentration was the highest. But it started to decrease as the axial distance increased, showing a Gaussian distribution.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2003년도 제20회 춘계학술대회 논문집
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• pp.266-269
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• 2003

액체로켓 엔진 연소 시 발생하는 연소 가스는 고온, 고속의 유동특성을 갖는다. 이러한 유동특성에 견딜 수 있는 연소시험 화염유도로 제작에 필요한 기초 자료를 얻고자 본 실험을 수행하였고, 연소 가스에 물을 분사하여 냉각된 연소가스의 온도 및 압력을 측정하였다. 동시에 열화상 카메라장비를 통해 온도를 측정하고 센서측정 데이터와 비교 분석한 결과 화염유도로에 적용 가능한 온도데이터를 획득하였고 물분사기 성능과 설치를 위한 구조적 강도를 예측할 수 있었다.

• 대한기계학회논문집B
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• 제23권10호
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• pp.1327-1339
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• 1999

Characteristics of two-phase flow and heat transfer were numerically investigated in a submerged gas Injection system. Effects of both the gas flow rate and bubble size were investigated. In addition, heat transfer characteristic and effects of heat transfer were investigated when temperature of the injected gas was different from that of the liquid. The Eulerian approach was used for the formulation of both the continuous and the dispersed phases. The turbulence in the liquid phase was modeled by the use of the standard $k-{\varepsilon}$ turbulence model. The interphase friction and heat transfer coefficient were calculated by means of correlations available in the literature. The turbulent dispersion of the phases was modeled by introducing a "dispersion Prandtl number". The plume region and the axial velocities are increased with increases in the gas flow rate and with decreases in the bubble diameter. The turbulent flow field grows stronger with the increases in the gas flow rate and with the decreases in the bubble diameter. In case that the heat transfer between the liquid and the gas is considered, the axial and the radial velocities are decreased in comparison with the case that there is no temperature difference between the liquid and the gas when the temperature of the injected gas is higher than the mean liquid temperature. The results in the present research are of interest in the design and the operation of a wide variety of material and chemical processes.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2003년도 춘계학술대회
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• pp.2105-2108
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• 2003

The characteristics of upward bubble flow were experimentally investigated in a liquid bath. In the present study, a thermal-infrared camera and high speed CCO camera were used to measure their temperature and local rising velocity, respectively. Heat transfer from bubble surface to water is largely completed within z=10mm from the nozzle, and then the temperature of bubble surface reaches that of water rapidly. The rising velocity of bubble was calculated for two different experimental conditions: 1) bubble flow without kinetic energy 2) with kinetic energy. Bubble flow without kinetic energy starts to undergo the effect of inertia force 10cm away from the nozzle. Whereas, kinetic energy is dominant before 30 cm away from the nozzle in bubble flow, but after this point, kinetic energy and inertial force are applied on bubble flow at the same time.

• 설비공학논문집
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• 제11권6호
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• pp.824-834
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• 1999

Characteristics of two-phase flow and heat transfer were numerically investigated in a submerged gas injection system when temperature of the injected gas was different from that of the liquid. The Eulerian approach was used for both the continuous and dispersed phases. The turbulence in the liquid phase was modeled using the standard $k-\varepsilon$$\varepsilon$ turbulence model. The interphase friction and heat transfer coefficient were calculated from the correlations available in the literature. The turbulent dispersion of the phases was modeled by a "dispersion Prandtl number". In the case with heat transfer where the temperature of the injected gas is higher than the mean liquid temperature, the axial and the radial velocities are lower in comparison with the case of homogeneous temperatures. The results in the present research are of interest in the design and operation of a wide variety of material and chemical processes.

• 한국산학기술학회논문지
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• 제21권10호
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• pp.317-324
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• 2020

천연가스를 연료로 사용하는 복합화력발전소는 석탄화력 대비 기동 및 정지가 용이하고 오염물질의 배출에 대한 부하가 적어 국내 발전설비 중 차지하는 비중이 꾸준히 상승하고 있다. 그러나 복합화력발전소는 가스터빈의 기동초기 및 저부하 운전 영역에서 황연현상을 일으키는 이산화질소(NO2)의 농도가 높은 특성을 가지고 있어 민원의 원인이 되며, 이의 제어 기술로서 황연제거설비가 2000년대 중반에 개발되어 운영되어 지고 있었다. 하지만 이 기술은 가스터빈 냉간기동 조건에서 기동초기 약 10~20분 동안은 기화시스템의 예열이 충분하게 이루어 지지 않아 황연현상을 제어할 수가 없는 실정이었다. 이에 본 연구에서는 환원제를 기화기를 사용하지 않고 액상의 상태로 가스터빈 Exhaust Duct에 직접 분사하여 황연현상을 제어하는 기술의 도출을 위해 CFD 해석 및 실증시험을 수행하였다. 가스터빈 Exhaust Duct에 위치에 있는 Diffuser에 의해 Duct의 외곽으로 형성된 배기가스에 액상의 환원제를 직분사하는 방안으로 배기가스 조건에 따라 5가지 Case로 분류하여 CFD를 수행하였으며, 그 결과 5가지 Case 모두에서 RMS가 15%이하로 양호한 혼합도를 보였다. 이를 바탕으로 실증설비를 설치 및 시험을 실시한 결과, 기존 기상주입방식에서 제어할 수 없었던 기동 초기 약 10~20분 구간의 황연현상도 완벽하게 제어할 수 있었다.

• 한국응용과학기술학회지
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• 제28권4호
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• pp.455-463
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• 2011

The average sulfur content of crude oil is 2.2%. Coal is about 0.3 to 4.0 percent of the sulfur gases or particles being discharged into the atmosphere through the chimney as 1 to 2% $SO_3$(Sulfur trioxide) and about 95% of the $SO_2$ is reported. $SO_3$ gas, which has many different causes of, as the combustion of sulfur containing fuel during the air due to the excess $SO_2$ gas is oxidized to $SO_3$ gas. Sulfur trioxide emitted from high sulfur heavy oil fired boiler caused white plume in stack and high temperature and cold end corrosion of facilities. So, in order to control sulfur trioxide concentration of Fuel gas in boiler, various of additives are used in other foreign. They are injected to Fuel Oil and consumed in boiler and reduce ash and the conversion rate of sulfur trioxide. In domestic, MgO compounds are used as additives but the total volume of them are made from other foreign company. In this study, MgO compounds were developed with liquid MgO compounds and field application was accomplished. The effect of newly developed chemicals and process were nearly equal to foreign products. In Consequent, the chemicals and process produced by newly developed technology can be substituted for foreign products and reduce the cost of plant operation.