SAE Technical Paper Series 1999
DOI: 10.4271/1999-01-0518
|View full text |Cite
|
Sign up to set email alerts
|

Cavitation in Two-Dimensional Asymmetric Nozzles

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
24
0
1

Year Published

2000
2000
2016
2016

Publication Types

Select...
6
4

Relationship

0
10

Authors

Journals

citations
Cited by 72 publications
(25 citation statements)
references
References 10 publications
0
24
0
1
Order By: Relevance
“…In contrast, single-fluid cavitation models, which are sometimes referred to as homogeneous Eulerian models, treat the fluid as a continuous mixture of liquid and vapor solving a single set of constitutive equations characterized by average mixture properties, such as mixture density and mixture viscosity. Although not necessary, the void fraction can be transported separately as with Volume-of-Fluid (VOF) methods, 25 allowing for inclusion of non-equilibrium phase transition effects as proposed by Kunz et al 26 or Yuan et al 27 Assuming the liquid and gaseous phases to be in thermal and mechanical equilibrium, Schmidt et al 28,29 and Schnerr et al 30 developed a model in which the two phases are uniformly distributed within each cell without slip between the liquid and vapor phases, neglecting surface tension and buoyancy effects. Thermodynamic equilibrium models exhibit an intrinsic length-scaling capability 31 and thus are particularly suitable for application to complex flows in conjunction with subgrid-scale (SGS) models for non-resolved flow scales.…”
Section: -2 öRley Et Almentioning
confidence: 99%
“…In contrast, single-fluid cavitation models, which are sometimes referred to as homogeneous Eulerian models, treat the fluid as a continuous mixture of liquid and vapor solving a single set of constitutive equations characterized by average mixture properties, such as mixture density and mixture viscosity. Although not necessary, the void fraction can be transported separately as with Volume-of-Fluid (VOF) methods, 25 allowing for inclusion of non-equilibrium phase transition effects as proposed by Kunz et al 26 or Yuan et al 27 Assuming the liquid and gaseous phases to be in thermal and mechanical equilibrium, Schmidt et al 28,29 and Schnerr et al 30 developed a model in which the two phases are uniformly distributed within each cell without slip between the liquid and vapor phases, neglecting surface tension and buoyancy effects. Thermodynamic equilibrium models exhibit an intrinsic length-scaling capability 31 and thus are particularly suitable for application to complex flows in conjunction with subgrid-scale (SGS) models for non-resolved flow scales.…”
Section: -2 öRley Et Almentioning
confidence: 99%
“…During the last two decades, the focus of research in quantifying nozzle flow and spray characteristics was on diesel injectors [3][4][5][6][7][8][9][10][11][12] using both experimental and CFD techniques capable of visualizing, measuring and calculating the internal flow characteristics of injectors and, in particular, describing the cavitation process which is associated with the local pressure distribution inside the sac volume and adjacent holes. Different types of cavitation have been identified: (i) geometrically induced cavitation which occurs in flow areas with sharp corners such as at the entrance into the nozzle holes, (ii) 'string' or 'vortex' type cavitation [3,9,12] which is the main source of instability in the sprays exiting the nozzle holes and (iii) 'needle' cavitation [13] which initiates in the vicinity of the needle and extends to the opposite nozzle hole when it is fully developed.…”
Section: Introductionmentioning
confidence: 99%
“…For high pressure injection systems cavitation may occur in the injectors [31]. Cavitating sprays have characteristics significantly different from the non cavitating ones.…”
Section: Modified Turbulence Induced Atomization Modelmentioning
confidence: 99%