Interfacial area measurement with new algorithm for grouping bubbles by diameter

Author:

Mills C. S. L.,Schlegel J. P.

Publisher

Springer Science and Business Media LLC

Reference25 articles.

1. Calderbank, P. H., Moo-Young, M. B. 1961. The continuous phase heat and mass-transfer properties of dispersions. Chem Eng Sci, 16: 39–54.

2. Delhaye, J. M., Achard, J. L. 1976. On the averaging operators introduced in two-phase flows modeling. In: Proceedings of the OECD/NEA Specialists Meeting on Transient Two-Phase Flow.

3. Fu, X. Y., Ishii, M. 2003. Two-group interfacial area transport in vertical air–water flow: I. Mechanistic model. Nucl Eng Des, 219: 143–168.

4. Hibiki, T., Ishii, M. 2000. Two-group interfacial area transport equations at bubbly-to-slug flow transition. Nucl Eng Des, 202: 39–76.

5. Ishii, M., Kim, S. 2001. Micro four-sensor probe measurement of interfacial area transport for bubbly flow in round pipes. Nucl Eng Des, 205: 123–131.

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