• 한국분무공학회지
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• 제7권1호
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• pp.29-35
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• 2002

This study describes the external spray characteristics of deflector nozzle such as the breakup procedures of liquid sheet, spray angle, breakup length and bubble behaviors of spray at deflector nozzle. In order to visualize the spray behaviors shadow graphy technique were used. According to the increase injection pressure, deveopment of the spray passes through the dribbling, distoted jet, closed bubble due to the contraction by form a conical sheet like as the simplex swirl atomizer. As trying the analysis of the ratio of bubble length and width it was found that the ratios is comparable. Spray cone angle was nearly $90^{\circ}$.

• 한국추진공학회지
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• 제2권2호
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• pp.24-29
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• 1998

Duplex Type의 2-유체 공기충돌형 Swirl 인젝터의 분무특성을 파악하고자 유체공급압력 0~13kg/$\textrm{cm}^2$ 범위에서 유량계수, 등가 분산각, 질량분포를 실험적으로 구하였다. 일반적으로 기체의 총 유량이 증가할수록 미립화는 촉진되나 반경방향 유량이 많은 경우에 분무형상은 비교적 안정적이었으며, 축방향 보다는 반경방향 선회기가 미립화에 미치는 영향이 컸다. 3kg/$\textrm{cm}^2$을 제외하고는 물 유량이 증가함에 따른 등가 분산각의 변화는 미소하였고, 기체의 유량증가도 마찬가지였다. Patternator를 사용한 질량 분포는 반경방향 기체유량이 증가함에 따라 분포곡선의 최대점은 낮아지면서 더 넓은 영역에 걸쳐 분포하였고, 물 유량의 증가에 따른 질량중심점의 위치는 변화가 없었다.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 1999년도 제13회 학술강연논문집
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• pp.27-27
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• 1999

To illustrate the global variation of the droplet mean diameters and the turbulent flow characteristics in counterflowing internal mixing pneumatic nozzle, the experimental measurements at five axial downstream locations(i.e., at Z=30, 50, 80, 120, and 170mm) were made using a PDPA(Phase Doppler Particle Analyzer) under the different air injection pressures ranging from 40 ㎪ to 120 ㎪. A nozzle with axi-symmetric tangential-drilled four holes at an angle of 15$^{\circ}$ has been designed and manufactured. The distributions of velocities, turbulence intensities, turbulence kinetic energy, turbulent correlation coefficients, spray angle, droplet mean diameters, volume flux, number density are quantitatively analyzed. It is possible to discern the effects of increasing air pressure. It indicates that the strong axial momentum in spite of more or less disparity between the velocity components means more reluctant to disperse radially, and that axial fluctuating velocities are substantially higher than those of radial and tangential ones, suggesting that the disintegration process is enhanced under higher air assist. The larger droplets are detected in the spray centerline at the near stations and smaller ones are generated due to further subsequent breakup at farther axial locations are attributed to the internal mixing type nozzle characteristics. Despite of the strong axial momentum, the poor atomization around the centre close to the nozzle exit is attributed to the lower rates of spherical particles which are not subject to instantaneous breakup. As it goes downstream, however, substantial increases in SMD(Sauter Mean Diameter) from the central part toward spray periphery are understandable because the droplet relative velocity is too low to bring about any subsequent disintegration.