2014
DOI: 10.1080/19942060.2014.11083307
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Numerical Study of The Effect of Wall Injection on The Cavitation Phenomenon In Diesel Injector

Abstract: Cavitation has an important effect on the performance of diesel injectors. It influences the nature of the fuel spray and formation of emissions. In contrast, cavitation increases the hydraulic resistance of the nozzle, creates flow instability, produces noise, and erodes the nozzle wall. In the present study, the effect of wall injection on the boundary layer separation in the cavitating and turbulent flow developing inside a diesel injector has been investigated numerically using two-phase mixture model. Sim… Show more

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Cited by 13 publications
(10 citation statements)
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“…Since the existence of non-considerable gases in hydraulic oil is unavoidable in practical conditions, the mixture of liquid and vapor phase has been considered in our study. The mixture is considered as a 'single phase' [35], [36]. Aiming to compute the steady-state cavitation phenomena at the interested locations under different inlet pressures, the set of following equations are solved during the flow field simulations.…”
Section: Model Of Cavitationmentioning
confidence: 99%
“…Since the existence of non-considerable gases in hydraulic oil is unavoidable in practical conditions, the mixture of liquid and vapor phase has been considered in our study. The mixture is considered as a 'single phase' [35], [36]. Aiming to compute the steady-state cavitation phenomena at the interested locations under different inlet pressures, the set of following equations are solved during the flow field simulations.…”
Section: Model Of Cavitationmentioning
confidence: 99%
“…The homogeneous mixture multiphase model was adopted (Hassanzadeh et al, 2014). Water and vapor were set as the primary phase and the second phase, respectively.…”
Section: Turbulence and Cavitation Modelmentioning
confidence: 99%
“…The mixture model is employed, which is considered as a ''single phase'' with its physical properties varying axis transition part according to the local concentration of liquid and vapor. 19,25 The fluid flow is assumed to be pseudounsteady. The continuity and momentum equations, which describe the mixture flow in Cartesian coordinates, are presented as follows 26 ∂r ∂t + ∂ru j ∂x j = 0…”
Section: Multiphase Modelmentioning
confidence: 99%