2018
DOI: 10.1016/j.expthermflusci.2018.05.022
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Droplet generation during liquid jet impingement onto a horizontal plate

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Cited by 19 publications
(9 citation statements)
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“…Herein, C 1 = 9.1×10 -4 C D / D p for water jet, with C D being the dimensionless drag coefficient. Zhan et al [44] experimentally had C D = 0.58 for Re 0 from 2,000 to 10,000. U b represents the jet velocity where jet breakup occurs and can be calculated by substituting l = L b into Eq.…”
Section: Resultsmentioning
confidence: 97%
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“…Herein, C 1 = 9.1×10 -4 C D / D p for water jet, with C D being the dimensionless drag coefficient. Zhan et al [44] experimentally had C D = 0.58 for Re 0 from 2,000 to 10,000. U b represents the jet velocity where jet breakup occurs and can be calculated by substituting l = L b into Eq.…”
Section: Resultsmentioning
confidence: 97%
“…After the jet breakup when l > L b , the air friction acting on the primary drops cannot be neglected due to the much larger surface area of the drops [31] . Zhan et al [44] developed an equation for predicting the velocity U p of the primary drops …”
Section: Resultsmentioning
confidence: 99%
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“…Based on the velocity measurement of the splattered droplets, it has been assumed that the splattering takes place downstream the radial position (also known as the radius of splattering) r s = 5.71 d N [6], where d N denotes the nozzle diameter. Splattering is often quantified by the splattered mass fraction ξ, which is the ratio between the mass flow rates of the splattered liquid and impinging liquid [7][8][9][10][11][12]. Correlations describing the splattered mass fraction can be found in [9] for coherent jets (L/d N < 50) and pipe nozzles, as well as in [11] for disintegrated jets (L/d N ≥ 250).…”
Section: Introductionmentioning
confidence: 99%