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    Investigation of High-Temperature Printed Circuit Heat Exchangers for Very High Temperature Reactors 

    Source: Journal of Engineering for Gas Turbines and Power:;2009:;volume( 131 ):;issue: 006:;page 62905
    Author(s): Sai Mylavarapu; Xiaodong Sun; Justin Figley; Noah Needler; Richard Christensen
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Very high-temperature reactors require high-temperature (900–950°C) and high-integrity heat exchangers with high effectiveness during normal and off-normal conditions. A class of compact heat ...
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    Interfacial Area Transport Equation and Implementation Into Two-Fluid Model 

    Source: Journal of Thermal Science and Engineering Applications:;2009:;volume( 001 ):;issue: 001:;page 11005
    Author(s): Mamoru Ishii; Seungjin Kim; Xiaodong Sun; Takashi Hibiki
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: A dynamic treatment of interfacial area concentration has been studied over the last decade by employing the interfacial area transport equation. When coupled with the two-fluid model, the ...
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    Phase Distribution in the Cap Bubble Regime in a Duct 

    Source: Journal of Fluids Engineering:;2006:;volume( 128 ):;issue: 004:;page 811
    Author(s): Martin Lopez de Bertodano; Xiaodong Sun; Mamoru Ishii; Asim Ulke
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: The lateral phase distribution in the cap-bubbly regime was analyzed with a three-dimensional three-field two-fluid computational fluid dynamics (CFD) model based on the turbulence model for bubbly ...
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    Local Liquid Velocity in Vertical Air-Water Downward Flow 

    Source: Journal of Fluids Engineering:;2004:;volume( 126 ):;issue: 004:;page 539
    Author(s): Xiaodong Sun; Joseph M. Kelly; Sidharth Paranjape; Seungjin Kim; Hiroshi Goda; Mamoru Ishii
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: This paper presents an experimental study of local liquid velocity measurement in downward air-water bubbly and slug flows in a 50.8 mm inner-diameter round pipe. The axial liquid velocity and ...
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