2017
DOI: 10.1007/s10494-017-9806-1
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Effect of Nozzle Exit Turbulence on the Column Trajectory and Breakup Location of a Transverse Liquid Jet in a Gaseous Flow

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Cited by 16 publications
(5 citation statements)
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“…% only, the dynamics observed for water are comparable to the actual feedstock used for deposition and other low concentration feedstock in general, as their liquid columns have comparable momenta. The graphs showing the feedstock penetration into the jet have been carried out tracing the upstream side of the liquid column [18] using ImageJ (NIH, USA); the images were first converted to black and white by applying the same threshold of 90% to each image.…”
Section: In-flight Measurementsmentioning
confidence: 99%
“…% only, the dynamics observed for water are comparable to the actual feedstock used for deposition and other low concentration feedstock in general, as their liquid columns have comparable momenta. The graphs showing the feedstock penetration into the jet have been carried out tracing the upstream side of the liquid column [18] using ImageJ (NIH, USA); the images were first converted to black and white by applying the same threshold of 90% to each image.…”
Section: In-flight Measurementsmentioning
confidence: 99%
“…Lb is measured through laser-induced fluorescence (LIF) (Charalampous et al 2009a,b) or is estimated photographically (Jiang et al 2019;Sridhara and Raghunandan 2010). There are several prediction equations for Lb presented in literature based on experimental investigations (Broumand et al 2017;Engelbert et al 1995;Eroglu et al 1991;Lasheras et al 1998;Leroux et al 2007;Porcheron et al 2002). Although a satisfactory agreement with the specific experimental data is demonstrated in each case, these equations cannot be used for the prediction of other spraying configurations.…”
Section: Introductionmentioning
confidence: 99%
“…On the one hand, it is the imbalance between the pressure gradient and the density gradient caused by the disturbance of the liquid column surface at the nozzle outlet, namely the Rayleigh-Taylor (RT) instability mechanism [5,6] ; on the other hand, the Kelvin-Helmholtz (KH) instability is caused by the tangential velocity gradient at the gas-liquid interface [7,8] . The R-T instability and the K-H instability or the instability effect produced by the coupling of the two have an important influence on the breaking length of the liquid jet, the droplet size distribution, and the subsequent atomization characteristics in Figure 1 [9] . Based on the above instability principle, it is found that under high gas Weber number, the transverse jet will be subjected to the azimuthal shear effect on the lateral surface to cause surface cracking [10] , which can be divided into primary crushing and secondary crushing according to different crushing mechanisms.…”
Section: Introductionmentioning
confidence: 99%