### Abstract

The Eulerian-Eulerian two-fluid model (EE) is a powerful general model for multiphase flow computations. However, one limitation of the EE model is that it has no ability to estimate the local bubble sizes by itself. In this work, we have combined the discrete phase model (DPM) to estimate the evolution of bubble sizes with the EE model. In the DPM, the change of bubble size distribution is estimated by coalescence, breakup, and volumetric expansion modeling of the bubbles. The time-varying bubble distribution is used to compute the local interface area between gas and liquid phase, which is then used to estimate the momentum interactions such as drag, lift, wall lubrication, and turbulent dispersion forces for the EE model. In this work, this newly developed hybrid model Eulerian-Eulerian discrete-phase model (EEDPM) is applied to compute an upward flowing bubbly flow in a vertical pipe and the results are compared with previous experimental work of Hibiki et al. (2001, "Axial Interfacial Area Transport of Vertical Bubbly Flows," Int. J. Heat Mass Transfer, 44(10), pp. 1869-1888). The EEDPM model is able to reasonably predict the locally different bubble size distributions and the velocity and gas fraction fields. On the other hand, the standard EE model without the DPM shows good comparison with measurements only when the prescribed constant initial bubble size is accurate and does not change much. Parametric studies are implemented to understand the contributions of bubble interactions and volumetric expansion on the size change of bubbles quantitatively. The results show that coalescence is larger than other effects, and naturally increases in importance with increasing gas fraction.

Original language | English (US) |
---|---|

Article number | 101202 |

Journal | Journal of Fluids Engineering, Transactions of the ASME |

Volume | 140 |

Issue number | 10 |

DOIs | |

State | Published - Oct 1 2018 |

### Fingerprint

### ASJC Scopus subject areas

- Mechanical Engineering

### Cite this

*Journal of Fluids Engineering, Transactions of the ASME*,

*140*(10), [101202]. https://doi.org/10.1115/1.4039793

**A Hybrid Eulerian-Eulerian Discrete-Phase Model of Turbulent Bubbly Flow.** / Yang, Hyunjin; Vanka, Surya Pratap; Thomas, Brian G.

Research output: Contribution to journal › Article

*Journal of Fluids Engineering, Transactions of the ASME*, vol. 140, no. 10, 101202. https://doi.org/10.1115/1.4039793

}

TY - JOUR

T1 - A Hybrid Eulerian-Eulerian Discrete-Phase Model of Turbulent Bubbly Flow

AU - Yang, Hyunjin

AU - Vanka, Surya Pratap

AU - Thomas, Brian G.

PY - 2018/10/1

Y1 - 2018/10/1

N2 - The Eulerian-Eulerian two-fluid model (EE) is a powerful general model for multiphase flow computations. However, one limitation of the EE model is that it has no ability to estimate the local bubble sizes by itself. In this work, we have combined the discrete phase model (DPM) to estimate the evolution of bubble sizes with the EE model. In the DPM, the change of bubble size distribution is estimated by coalescence, breakup, and volumetric expansion modeling of the bubbles. The time-varying bubble distribution is used to compute the local interface area between gas and liquid phase, which is then used to estimate the momentum interactions such as drag, lift, wall lubrication, and turbulent dispersion forces for the EE model. In this work, this newly developed hybrid model Eulerian-Eulerian discrete-phase model (EEDPM) is applied to compute an upward flowing bubbly flow in a vertical pipe and the results are compared with previous experimental work of Hibiki et al. (2001, "Axial Interfacial Area Transport of Vertical Bubbly Flows," Int. J. Heat Mass Transfer, 44(10), pp. 1869-1888). The EEDPM model is able to reasonably predict the locally different bubble size distributions and the velocity and gas fraction fields. On the other hand, the standard EE model without the DPM shows good comparison with measurements only when the prescribed constant initial bubble size is accurate and does not change much. Parametric studies are implemented to understand the contributions of bubble interactions and volumetric expansion on the size change of bubbles quantitatively. The results show that coalescence is larger than other effects, and naturally increases in importance with increasing gas fraction.

AB - The Eulerian-Eulerian two-fluid model (EE) is a powerful general model for multiphase flow computations. However, one limitation of the EE model is that it has no ability to estimate the local bubble sizes by itself. In this work, we have combined the discrete phase model (DPM) to estimate the evolution of bubble sizes with the EE model. In the DPM, the change of bubble size distribution is estimated by coalescence, breakup, and volumetric expansion modeling of the bubbles. The time-varying bubble distribution is used to compute the local interface area between gas and liquid phase, which is then used to estimate the momentum interactions such as drag, lift, wall lubrication, and turbulent dispersion forces for the EE model. In this work, this newly developed hybrid model Eulerian-Eulerian discrete-phase model (EEDPM) is applied to compute an upward flowing bubbly flow in a vertical pipe and the results are compared with previous experimental work of Hibiki et al. (2001, "Axial Interfacial Area Transport of Vertical Bubbly Flows," Int. J. Heat Mass Transfer, 44(10), pp. 1869-1888). The EEDPM model is able to reasonably predict the locally different bubble size distributions and the velocity and gas fraction fields. On the other hand, the standard EE model without the DPM shows good comparison with measurements only when the prescribed constant initial bubble size is accurate and does not change much. Parametric studies are implemented to understand the contributions of bubble interactions and volumetric expansion on the size change of bubbles quantitatively. The results show that coalescence is larger than other effects, and naturally increases in importance with increasing gas fraction.

UR - http://www.scopus.com/inward/record.url?scp=85046711703&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=85046711703&partnerID=8YFLogxK

U2 - 10.1115/1.4039793

DO - 10.1115/1.4039793

M3 - Article

AN - SCOPUS:85046711703

VL - 140

JO - Journal of Fluids Engineering, Transactions of the ASME

JF - Journal of Fluids Engineering, Transactions of the ASME

SN - 0098-2202

IS - 10

M1 - 101202

ER -