• 한국태양에너지학회 논문집
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• 제31권3호
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• pp.23-28
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• 2011

In this study, the ejector design was modeled using Fluent 6.3 of FVM(Finite Volume Method) CFD(Computational Fluid Dynamics) techniques to resolve the flow dynamics in the ejector. A vacuum system with the ejector has been widely used because of its simple construction and easy maintenance. Ejector is the main part of the desalination system, of which designs determine the efficiency of system. The effects of the ejector was investigated geometry and the operating conditions in the hydraulic characteristics. The ejector consists mainly of a nozzle, suction chamber, mixing tube (throat), diffuser and draft tube. Liquid is supplied to the ejector nozzle, the fast liquid jet produced by the nozzle entrains and the non condensable gas was sucked into the mixing tube. The multiphase CFD modeling was carried out to determine the hydrodynamic characteristics of seawater-air ejector. Condition of the simulation was varied in entrance mass flow rate (1kg/s, 1.5kg/s, 2kg/s, 2.5kg/s, 3kg/s), and position of driving nozzle was located from the central axis of the suction at -10mm, 0mm, 10mm, 20mm, 30mm.. Asaresult, suction flow velocity has the highest value in central axis of the suction.

• 한국산학기술학회논문지
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• 제15권11호
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• pp.6412-6418
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• 2014

본 논문은 기체-액체 이젝터의 수치해석연구에 초점을 맞추고 있다. 이젝터는 구동유체가 노즐을 통해 고속으로 분출될 때, 구동노즐 출구 주변에 진공압이 형성되어 주변의 기체와 운동량 교환을 통하여 저압의 유체를 보다 높은 압력으로 압축하여 수송하는 장치이다. 기체-액체 이젝터는 상용 소프트웨어 ANSYS-CFX 14.0을 사용하여 다상의 CFD 분석을 통해 연구한다. 구동유체는 물을 사용하여 구동되며, 실제로는 공기가 아닌 오존을 사용하여 배출 된다. 기체-액체 이젝터의 디퓨저의 형상에 따라 성능 차이를 비교한다. 결과 기체-액체 이젝터의 성능에 미치는 다양한 요인을 제공 한다. 그리고 제안 된 수치 모델은 기체-액체 이젝터의의 최적 설계에 매우 도움이 될 것다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2000년도 추계학술대회논문집A
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• pp.856-860
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• 2000

Liquid ejector is widely used for power plant water pump, marine pump and transportation of solid materials. It has high working confidence and simple configuration. However, It is not easy to know performance degradation of ejectors in field. When the geometry of ejector is complicate, the diagnosis of faults is required more skillful method without disassemble. This paper gives numerical method to predict cause of $45^{\circ}$ slurry suction ejector performance degradation.

• 대한기계학회논문집
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• 제12권3호
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• pp.520-527
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• 1988

본 연구에서는 액체용 이젝터의 성능을 결정하는 여러가지 제약인자중 특히 레이놀즈수 변화에 따른 구동노즐의 면적비 및 목부길이가 액체용 이제터성능에 미치 는 영향을 체계적인 실험을 통하여 연구함으로써 기 개발된 CAD용 전산프로그램의 타 당성을 보다 세밀히 검토하고 이에 보완을 가하는데 연구의 목적이 있다.

• Journal of Advanced Marine Engineering and Technology
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• 제14권1호
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• pp.90-98
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• 1990

The liquid ejector, having no moving, lubricating and leaking parts, is widely used as the various pumps because of its high working confidence and simplicity. Previously, computer aided design program for the small-sized liquid ejector was developed based on the one-dimensional flow analysis and the systematical laboratory level experiments. Through the present research, it is confirmed that the previously developed computer program to getermine the main design dimensions and to calculate the expected performance curve is satisfactorily applied to design the large liquid ejectors.

• 대한기계학회논문집B
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• 제39권2호
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• pp.183-190
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• 2015

무동력펌프의 일종인 이젝터는 압력을 갖는 유체를 노즐에서 분사하여 주위의 유체를 흡입 후 혼합유체를 외부 동력 없이 송출하는 장치이다. 구조가 간단하고 고장이 적어 여러 산업분야에서 이용되고 있으며, 자동차 산업에서는 연료주입용으로도 이용되고 있다. 대부분 이젝터는 가스상을 사용하기 때문에, 가스상 이젝터는 오래전부터 연구되어 왔다. 액체상 이젝터는 그 용도에 비해 아직 연구가 활발하지 못하다. 가스상 이젝터와 달리, 액체상 이젝터는 노즐목에서 부분적인 압력강하에의한 공동현상이 발생되고 이러한 공동현상은 부품파손을 유발하며, 소음을 발생시키는 원인이 되고 있다. 본 연구는 액체-액체상 이젝터의 최대 유량비와 공동현상 발생영역 비교를 위해 5가지 인자를 변경하여 2차원 축대칭 전산해석을 진행하였다. 액체 이젝터의 공동현상에서는 특히 노즐각도가 중요한 역할을 하였으며, 유량비 성능 특성은 혼합챔버각도 $35^{\circ}$가 가장 유리한 것으로 판단된다. 이를 통해 공동 현상을 최소화시키면서 성능 최적화를 달성할 수 있는 조합을 얻을 수 있음을 확인하였다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2817-2822
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• 2007

The purpose of this paper is to study the influence of operating condition and ejector geometries on the hydrodynamics and on the mass transfer characteristic of ejector. The CFD results were validated with available experimental data. Flow field analyses and predictions of ejector performance were also carried out. Variation on the operating conditions was made by varying the gas-liquid flow rate ratio in the range of 0.2 to 1.2. The ejector configuration was also varied on the length to diameter ratio of mixing tube ($L_M/D_M$) in the range of 4 to 10. CFD studies show that at $L_M/D_M$ 5.5, the volumetric mass transfer coefficient increases with respect to gas flow rates. Meanwhile, at $L_M/D_M$ 4, the plot of volumetric mass transfer coefficient to gas-liquid flow rates ratio reach maximum at gas-liquid flow rates ratio of 0.6. This study also shows that volumetric mass transfer coefficient decrease with respect to the increase of mixing tube length.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2708-2713
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• 2007

The aim of this paper is further studies to achieve deeper understanding in this field. First investigate the influence of operating conditions and design parameters on the hydrodynamics and the mass transfer properties of a loop reactor. This paper provides a literature review on the ejectors applications in the mixing system. A number of studies are grouped and discussed in several topics such as the background, theory of ejector, mixing characteristics, optimization of the system. Since the high efficiencies reactor using ejector widely used in gas-liquid system, especially in a number of chemical and biochemical processes. This is due to their high efficiency in gas dispersion resulting in high mass transfer rate and low power requirements. Thus ejector has been applied to the mixing system. An investigation on hydrodynamics and mass transfer characteristics of gas-liquid ejector has been carried out using three-dimensional CFD modeling.

• 동력기계공학회지
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• 제18권6호
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• pp.120-125
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• 2014

In this paper, suitable working fluid of 1MW Organic Rankine Cycle(ORC) with liquid-vapor ejector using effluent from power plant is selected. The results of comparison performance of 5 refrigerants are as follows; R600a, R134a, R1270, R236fa, R235fa. The operating parameters considered in this study include the condensation capacity evaporation capacity and efficiency. As a result of comparison of basic ORC system and with liquid-vapor ejector, with ORC system presents the higher system efficiency since the ejector makes the turbine outlet pressure lower than condensation pressure through its pressure recovery. Also, this ejector ORC system is advantageous in miniaturizing the size of components owing to decrease of evaporation capacity and condensation capacity.

• 설비공학논문집
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• 제12권4호
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• pp.345-353
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• 2000

In this study, the performance of five ejectors has been investigated with working fluids of water and water vapor. The diameters of nozzle and mixing tube of five ejectors were 1 and 1.5(ejector A), 1 and 2(ejector B), 1 and 2.5(ejector C), 1 and 3(ejector D), 2 and 4(ejector E) in millimeters. The length of the mixing tube was 8-10 times of its diameter. For each ejector, the ratio of mass flow rate of ejected water to that of entrained water vapor, $\mu$, was evaluated in terms of evaporator pressure, mass flow rate of ejected water, and water temperature. It was found that the performance of an ejector was not stable when the ratio of diameters was too small or too large(ejector A and D) and $\mu$ was almost the same for two ejectors with the same diameter ratio(ejector B and E). It was also found that $\mu$ increased almost linearly with an increase of evaporator pressure and the ratio $\mu$ increased as water temperature decreased. As expected, $\mu$ converged to zero as the water temperature approached the evaporator temperature. Finally, a non-dimensional correlation has been developed to predict$\mu$ terms of evaporator pressure and saturation pressure of ejected water.