Abstract

Bubble coalescence and breakup play important roles in physical-chemical processes and bubbles are treated in two groups in the interfacial area transport equation (IATE). This paper presents a review of IATE for bubble coalescence and breakup to model five bubble interaction mechanisms: bubble coalescence due to random collision, bubble coalescence due to wake entrainment, bubble breakup due to turbulent impact, bubble breakup due to shearing-off, and bubble breakup due to surface instability. In bubble coalescence, bubble size, velocity and collision frequency are dominant. In bubble breakup, the influence of viscous shear, shearing-off, and surface instability are neglected, and their corresponding theory and modelling are rare in the literature. Furthermore, combining turbulent kinetic energy and inertial force together is the best choice for the bubble breakup criterion. The reviewed one-group constitutive models include the one developed by Wu et al., Ishii and Kim, Hibiki and Ishii, Yao and Morel, and Nguyen et al. To extend the IATE prediction capability beyond bubbly flow, two-group IATE is needed and its performance is strongly dependent on the channel size and geometry. Therefore, constitutive models for two-group IATE in a three-type channel (i.e., narrow confined channel, round pipe and relatively larger pipe) are summarized. Although great progress in extending the IATE beyond churn-turbulent flow to churn-annual flow was made, there are still some issues in their modelling and experiments due to the highly distorted interface measurement. Regarded as the challenges to be addressed in the further study, some limitations of IATE general applicability and the directions for future development are highlighted.

Highlights

  • interfacial area concentration (IAC) is an essential parameter of the phase interaction terms in the two-phase model, and its dynamic prediction has been realized by interfacial area transport equation (IATE) [9]

  • Of these numerous studies pertaining to bubble coalescence and breakup for bubbly flow, the main phenomenon and mechanism have been summarized: (a) bubble breakup due to turbulent impact (TI); (b) bubble coalescence due to random collision (RC); (c) bubble coalescence due to wake entrainment (WE)

  • For the sink term and source term concerning the bubble coalescence and breakup mechanism are the main components of IATE, the constitutive models of bubble coalescence, and breakup which are usually established from experimental data based on various flow conditions is largely dependent on the performance of IATE

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Summary

Introduction

Flow is distributed in the liquid phase as variable size, deformable bubbles moving upward, and undergo a transition to slug flow when the gas superficial velocity increases due to the corresponding rise in the volume fraction and the coalescence of bubbles. It is readily acknowledged that the formation and motion of bubbles and interaction mechanisms of bubbles are very complicated and the gas-liquid interfacial area is the deciding factor in controlling mass and heat transfer in gas-liquid two-phase flow. 1D system codes are frequently used for the description of two-phase flow, which is based on the empirical work and can predict the gas-liquid flow in the case of the given volume flow rates of liquid and gas.

Transition of Bubbly to Churn-Turbulent Flows
Bubbly to Slug Transition
Slug to Churn Transition
One-group IATE for Bubble Coalescence and Breakup
Two-Group IATE for Bubble Coalescence and Breakup
Identification of Bubble Coalescence and Breakup Interaction Mechanisms
Bubble Coalescence Mechanisms
Bubble Breakup Mechanisms
Breakup due to Turbulent Impact
Breakup due to Shearing-Off
Breakup due to Viscous Shear Forces
Breakup due to Surface Instability
Breakup Frequency Models
Coalescence Frequency Models
Constitutive Models for the One-Group IATE
Bubble Coalescence due to RC
Bubble Breakup due to TI
Constitutive Models for the Two-Group IATE
Conclusions and Outlook
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