TY - JOUR
T1 - Stable mesh-free moving particle semi-implicit method for direct analysis of gas-liquid two-phase flow
AU - Natsui, Shungo
AU - Takai, Hifumi
AU - Kumagai, Takehiko
AU - Kikuchi, Tatsuya
AU - Suzuki, Ryosuke O.
N1 - Funding Information:
This research was supported by Advanced Low Carbon Technology Research and Development Program of Japan Science and Technology Agency “JST–ALCA”. And, author S. Natsui was partially supported by the Mazda Foundation research promotion in Japan.
PY - 2014/5/24
Y1 - 2014/5/24
N2 - In a metallurgical process, gas-liquid flow plays an important role in increasing the efficiency by stirring liquid mechanically or by injecting a gas. Owing to the difficulty of direct observation in a high-temperature system or real furnace experiment, numerical analysis is useful and widely studied. However, flexible treatment of complicated free surface behavior such as fragmentation and coalescence of liquids is still a difficult problem. This paper presents a new particle-based simulation scheme for gas-liquid flow. We improved the numerical stability, which is generally a problem with the particle method, and verified the model's accuracy for fundamental gas-liquid flow analysis.Because all the phases were discretized as particles in Moving Particle Semi-implicit (MPS) method, the proposed model can track the movement of both the gas and liquid phases directly. A large difference in the real density between the gas and liquid phases makes the gas-liquid interface behavior unstable. This study proposed an optimization of the weakly compressible Poisson equation, an initial particle arrangement, and a smoothed interface density in order to stabilize the multi-density flow analysis. This model guarantees conservation of the fluid volume even for a high-density-ratio flow like that at a gas-liquid interface. Therefore, a gas-liquid interface has been represented with high accuracy. We believe that this scheme is also applicable to phenomena in an actual process that includes many dispersal phases.
AB - In a metallurgical process, gas-liquid flow plays an important role in increasing the efficiency by stirring liquid mechanically or by injecting a gas. Owing to the difficulty of direct observation in a high-temperature system or real furnace experiment, numerical analysis is useful and widely studied. However, flexible treatment of complicated free surface behavior such as fragmentation and coalescence of liquids is still a difficult problem. This paper presents a new particle-based simulation scheme for gas-liquid flow. We improved the numerical stability, which is generally a problem with the particle method, and verified the model's accuracy for fundamental gas-liquid flow analysis.Because all the phases were discretized as particles in Moving Particle Semi-implicit (MPS) method, the proposed model can track the movement of both the gas and liquid phases directly. A large difference in the real density between the gas and liquid phases makes the gas-liquid interface behavior unstable. This study proposed an optimization of the weakly compressible Poisson equation, an initial particle arrangement, and a smoothed interface density in order to stabilize the multi-density flow analysis. This model guarantees conservation of the fluid volume even for a high-density-ratio flow like that at a gas-liquid interface. Therefore, a gas-liquid interface has been represented with high accuracy. We believe that this scheme is also applicable to phenomena in an actual process that includes many dispersal phases.
KW - Dispersion
KW - Gas-liquid flow
KW - Incompressible flow
KW - Material processing
KW - Moving particle semi-implicit method
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U2 - 10.1016/j.ces.2014.02.038
DO - 10.1016/j.ces.2014.02.038
M3 - Article
AN - SCOPUS:84896512673
SN - 0009-2509
VL - 111
SP - 286
EP - 298
JO - Chemical Engineering Science
JF - Chemical Engineering Science
ER -