2017
DOI: 10.1016/j.jcp.2017.06.008
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An immersed boundary method for fluid–structure interaction with compressible multiphase flows

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Cited by 93 publications
(66 citation statements)
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References 70 publications
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“…Without loss of generality, a flexible plate immersed in the two-dimensional fluid is used as an example to introduce the structure dynamics. The plate is assumed to be elastic and its dynamics is governed by the following nonlinear equation [22,42,30]…”
Section: Methodsmentioning
confidence: 99%
See 2 more Smart Citations
“…Without loss of generality, a flexible plate immersed in the two-dimensional fluid is used as an example to introduce the structure dynamics. The plate is assumed to be elastic and its dynamics is governed by the following nonlinear equation [22,42,30]…”
Section: Methodsmentioning
confidence: 99%
“…Validations of the present solver for fluid-structure interactions including flow over a stationary cylinder, structure dynamics, deformation of a flexible panel induced by shock waves in a shock tube, an inclined flexible plate in a hypersonic flow, and shock-induced collapse of a cylindrical helium cavity in the air have been conducted in our previous work [30]. Here, we focus on validations of acoustics modelling including acoustic waves scattered from a stationary cylinder in a quiescent flow, sound generation by a stationary and a rotating cylinder in a uniform flow, sound generation by an insect in hovering flight, deformation of a red blood cell induced by acoustic waves and acoustic waves scattered by a stationary sphere.…”
Section: Validationsmentioning
confidence: 99%
See 1 more Smart Citation
“…They used the arbitrary Lagrangian-Eulerian method to track interfaces and applied a two-pressure model for a single fluid. Wang et al 11 used the ghost fluid method to simulate compressible multiphase flows. The ghost fluid method can easily handle discontinuities in the dependent variables across material interfaces.…”
Section: Introductionmentioning
confidence: 99%
“…Present 0.182 1.258 0.375 Patnana et al (Patnana et al, 2009) 0.180 1.180 -Tian et al 0.188 1.179 0.367 1.0 Present 0.164 1.415 0.349 Patnana et al (Patnana et al, 2009) 0.164 1.341 0.325 0.160 1.430 0.360 Wang et al (Wang et al, 2017) 0.161 1.450 0.310 1.4 Present 0.159 1.546 0.345 Patnana et al (Patnana et al, 2009) 0.150 1.497 -Tian et al 0.161 1.523 0.356 Table 2. Averaged Nusselt number (N u) for forced convection heat transfer from a stationary cylinder to power-law fluids at Pr = 1.0.…”
Section: Non-newtonian Power-law Fluid Flow and Heat Transfer Around mentioning
confidence: 99%