1 - 7 |
A model for tracking inertial particles in a lattice Boltzmann turbulent flow simulation Jung S, Phares DJ, Srinivasa AR |
8 - 23 |
Terminal velocities of clean and fully-contaminated drops in vertical pipes Kurimoto R, Hayashi K, Tomiyama A |
24 - 30 |
Effects of T-junction size on bubble generation and flow instability for two-phase flows in circular microchannels Yamamoto K, Ogata S |
31 - 48 |
A pressure correction-volume of fluid method for simulations of fluid-particle interaction and impact problems Lin SY, Chen YC |
49 - 57 |
Gas dispersion in horizontal pulp-fibre-suspension flow Yenjaichon W, Grace JR, Lim CJ, Bennington CPJ |
58 - 69 |
Computations of breakup modes in laminar compound liquid jets in a coflowing fluid Vu TV, Homma S, Tryggvason G, Wells JC, Takakura H |
70 - 77 |
Statistical diagnosis of a gas-solid fluidized bed using Electrical Capacitance Tomography Rautenbach C, Melaaen MC, Halvorsen BM |
78 - 82 |
Minimum fluidization velocities for supercritical water fluidized bed within the range of 633-693 K and 23-27 MPa Lu YJ, Zhao L, Han Q, Wei LP, Zhang XM, Guo LJ, Wei JJ |
83 - 98 |
Adaptive mesh refinement for two-phase slug flows with an a priori indicator Gourma M, Jia N, Thompson C |
99 - 118 |
Characteristics of horizontal liquid-liquid flows in a circular pipe using simultaneous high-speed laser-induced fluorescence and particle velocimetry Morgan RG, Markides CN, Zadrazil I, Hewitt GF |