Analysis of Two-Phase Homogeneous Bubbly Flows Including Friction and Mass Addition

[+] Author and Article Information
Marat Mor, Alon Gany

  Department of Aerospace Engineering, Technion-Israel Institute of Technology, Haifa 32000, Israele-mail: gany@tx.technion.ac.il

J. Fluids Eng 126(1), 102-109 (Feb 19, 2004) (8 pages) doi:10.1115/1.1637628 History: Received October 25, 2002; Revised September 03, 2003; Online February 19, 2004
Copyright © 2004 by ASME
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Grahic Jump Location
Behavior of pressure ratio as a function of Mach number and air void fraction at stagnation point
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Two-phase homogeneous bubbly flow behavior in nozzle
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Nozzle flow with friction
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fxmax/dϕ2 vs. initial Mach number–analogy of Fanno-line in a two-phase bubbly flow
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Behavior of cross-section dimensionless diameter as a function of location for various ν̄ and Mach number values
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Behavior of cross-section diameter as a function of ν̄ for various locations and Mach number values
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Location of the choking point (xmax) vs. initial Mach number for different mass addition distributions
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Normalized mass flow rate ratio at the choking point vs. initial Mach number for different values of ν and mass addition distributions
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Choking curve vs. air void fraction at stagnation point
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Limit value of Mach number M(α=0.74) for gas volume fraction restriction of α=0.74 as a function of α0
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Numerical solution and analytical approximations for flow through a converging-diverging (Laval) nozzle. Initial conditions: Ain=13.2 cm2,Pin=3.5 atm (0.35 MPa),T=293 K,μ=0.002,Min=0.2. (Relative variation of bubble radius, r/rin, is presented as indication for the case of monodisperse spherical bubbles.)



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