Interfacial area transport equations for gas-liquid flow

被引：5
作者：
Hibiki, Takashi [1 ]
Ishii, Mamoru [1 ]
机构：
[1] School of Nuclear Engineering, Purdue University, West Lafayette, IN 47907-2017
来源：
Journal of Computational Multiphase Flows | 2009年 / 1卷 / 01期
关键词：
Boiling flow; Interfacial area concentration; Interfacial area transport equation; Multiphase flow; Twofluid model;
D O I：
10.1260/175748209787387089
中图分类号：
学科分类号：
摘要：
In relation to the modeling of the interfacial transfer terms in the two-fluid model, the concept of the interfacial area transport equation has been proposed to develop a constitutive relation for the interfacial area concentration. The interfacial area transport equation can replace the traditional flow regime maps and regime transition criteria. The changes in the two-phase flow structure can be predicted mechanistically and the effects of the boundary conditions and flow development are efficiently modeled by this transport equation. A successful development of the interfacial area transport equation can make a significant improvement in the two-fluid model formulation and the prediction accuracy of three-dimensional two-phase flow simulations. In this paper, the basic concept of the interfacial area transport equation and its formulation have been briefly described. Available models of the interfacial area sink and source terms and existing databases have been reviewed and the interfacial area transport equation has been benchmarked using adiabatic bubbly flow and condensation bubbly flow data. Future direction for this research has been suggested.
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页码：1 / 22
页数：21
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  • [1] Bartel M.D., Ishii M., Masukawa T., Mi Y., Situ R., Interfacial area measurements in subcooled flow boiling, Nuc. Eng. Des, 210, pp. 135-155, (2001)
  • [2] Chen J.C., Correlation for boiling heat transfer to saturated fluids in convective flow, Ind. Eng. Chem. Proc. Des. Dev, 5, pp. 322-329, (1966)
  • [3] Fu X.Y., Ishii M., Two-group interfacial area transport in vertical air-water flow, I. Mechanistic Model, Nuc. Eng. Des, 210, pp. 143-168, (2003)
  • [4] Fu X.Y., Ishii M., Two-group interfacial area transport in vertical air-water flow, Ii. Model Evaluation, Nuc. Eng. Des, 210, pp. 169-190, (2003)
  • [5] Grossetete C., Caracterisation Experimentale Et Simulations De L'evolution D'un Ecoulement Diphasique a Bulles Ascendant Dans Une Conduit Vertical, (1995)
  • [6] Hazuku T., Takamasa T., Hibiki T., Ishii M., Interfacial area concentration in annular two-phase flow, Int. J. Heat Mass Transfer, 50, pp. 2986-2995, (2007)
  • [7] Hibiki T., Hogsett S., Ishii M., Local measurement of interfacial area, interfacial velocity and liquid turbulence in two-phase flow, Nuc. Eng. Des, 184, pp. 287-304, (1998)
  • [8] Hibiki T., Ishii M., Experimental study on interfacial area transport in bubbly two-phase flows, Int. J. Heat Mass Transfer, 42, pp. 3019-3035, (1999)
  • [9] T. and Ishii, M., One-group interfacial area transport of bubbly flows in vertical round tubes, Int. J. Heat Mass Transfer, 43, pp. 2711-2726, (2000)
  • [10] Hibiki T., Ishii M., Two-group interfacial area transport equations at bubbly-to-slug flow transition, Nuc. Eng. Des, 202, pp. 39-76, (2000)
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