2013
DOI: 10.1139/cjce-2012-0199
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CFD analysis of the effect of nozzle stand-off distance on turbulent impinging jets

Abstract: Three-dimensional steady Reynolds Averaged Navier-Stokes simulations have been carried out to investigate the effect of the nozzle stand-off distance on the mean and turbulence characteristics of jets impinging vertically on flat surfaces. As part of the study, the performance of different turbulence models such as Realizable k–ε, k–ω SST, and Reynolds Stress Model (RSM) were evaluated. Based on comparisons with experimental data, RSM was chosen to further evaluate the characteristics of impinging jets. The Re… Show more

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Cited by 15 publications
(16 citation statements)
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“…The commercial CFD code discretizes Equations 4 and 5 using a finite volume method, where a second order convection scheme was selected in the segregatedflow solver. Two turbulence models were selected for comparison, namely the realizable k-e turbulence model (ReaKEps) and the shear stress transport k-x turbulence model (SST), following a previous study on incompressible impinging air jets (Shademan, Balachandar, and Barron 2013).…”
Section: Methodsmentioning
confidence: 99%
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“…The commercial CFD code discretizes Equations 4 and 5 using a finite volume method, where a second order convection scheme was selected in the segregatedflow solver. Two turbulence models were selected for comparison, namely the realizable k-e turbulence model (ReaKEps) and the shear stress transport k-x turbulence model (SST), following a previous study on incompressible impinging air jets (Shademan, Balachandar, and Barron 2013).…”
Section: Methodsmentioning
confidence: 99%
“…This means that the ratio between inertia and viscous forces (Reynolds number) is similar, and therefore previous work may be used for validation and calibration purposes. Poreh, Tsuei, and Cermak (1967) 8 -24 1.11 Â 10 6 -5.00 Â 10 6 Floating element (air) Orifice Kataoka & Mizushina (1974) 3.86-8.24 9.60 Â 10 3 -3.62 Â 10 4 Electro-chemical (water) Convergent Beltaos & Rajaratnam (1974) 21.2-65.7 3.89 Â 10 4 -8.04 Â 10 4 Preston tube (air) Convergent Giralt, Chia, and Trass (1977) 3.0-25.0 3 Â 10 4 -8 Â 10 4 Not determined (air) Convergent Hanson, Robinson, and Temple (1990) 16.5 2.3 Â 10 4 -8.4 Â 10 4 Hot-film sensor (water) Convergent Alekseenko & Markovich (1994) 2 -8 4.16 Â 10 4 Electrochemical (water) Convergent Phares, Smedley, and Flagan (2000) 3 -20 3.7 Â 10 3 -1.15 Â 10 4 Particle resuspension (air) Short pipe Shademan, Balachandar, and Barron (2013) 2 -18.5 1 Â 10 5 RANS Uniform inlet Ghaneeizad, Atkinson, and Bennett (2015) 24.7 2.3 Â 10 4 -3.4 Â 10 4 PIV (water) JET nozzle Shademan et al (2016) 20 2.8 Â 10 4 LES, PIV (water) Convergent RANS, Reynolds-averaged Navier-Stokes; LES, large eddy simulation; PIV, particle image velocimetry; JET, jet erosion test. Depending on the working fluid, usually air or water, different experimental techniques have been used in the past for determining the tangential component of wall surface forces, ie the wall shear stress (Table 1).…”
Section: Review On Round Immersed Impinging Jetsmentioning
confidence: 99%
“…1 from Shademan et al 2013). For H/D < 6 it has been found that the core of the jet is still developing on reaching the plate surface (Nishino et al 1996;Hadziabdic and Hanjalic 2008).…”
mentioning
confidence: 98%
“…For H/D < 6 it has been found that the core of the jet is still developing on reaching the plate surface (Nishino et al 1996;Hadziabdic and Hanjalic 2008). For larger impingement heights (H/D > 8), Rajaratnam (1974, 1977) Shademan et al 2013). As a result, each region has specific characteristics and the objective of the study was to best capture the features in all the regions with a single turbulence model.…”
mentioning
confidence: 99%
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