Unified stability condition for particulate and aggregative fluidization—Exploring energy dissipation with direct numerical simulation--颗粒学报PARTICUOLOGY

Wei, M., Wang, L., & Li, J. (2013). Unified stability condition for particulate and aggregative fluidization—Exploring energy dissipation with direct numerical simulation. Particuology, 11(2), 232–241. https://doi.org/10.1016/j.partic.2012.10.002

Unified stability condition for particulate and aggregative fluidization—Exploring energy dissipation with direct numerical simulation

Min Wei ^{a b}, Limin Wang ^a *, Jinghai Li ^a

a The EMMS Group, State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
b University of Chinese Academy of Sciences, Beijing 100049, China

10.1016/j.partic.2012.10.002

Volume 11, Issue 2, April 2013, Pages 232-241

Received 30 December 2011, Revised 9 October 2012, Accepted 14 October 2012, Available online 26 January 2013.

E-mail: lmwang@home.ipe.ac.cn

Highlights

► DNS of both particulate and aggregative fluidization is performed using LBM–TDHS model.

► Stability criterion in EMMS/bubbling model is verified.

► Energy dissipation as a unified stability condition for particulate and aggregative fluidization.

Abstract

Fully resolved simulations of particulate and aggregative fluidization systems are performed successfully with the so-called combined lattice Boltzmann method and time-driven hard-sphere model (LBM–TDHS). In this method, the discrete particle phase is described by time-driven hard-sphere model, and the governing equations of the continuous fluid phase are solved with lattice Boltzmann method. Particle–fluid coupling is implemented by immersed moving boundary method. Time averaged flow structure of the simulated results show the formation of core-annulus structure and sigmoid distribution of voidage in the axial direction, which are typical phenomena in fluidization systems. Combining the results of the simulation, the energy consumption N_stfor suspending and transporting solids is calculated from the direct numerical simulation (DNS) of fluidization, and the stability criterion N_st/N_T=min proposed in EMMS/bubbling model is verified numerically. Furthermore the numerical results show that the value of N_st/N_T in particulate fluidization is much higher than that in aggregative fluidization, but N_st/N_T=min is effective for both particulate and aggregative fluidization.

Graphical abstract

Keywords

Direct numerical simulation; Fluidization; Stability condition; Lattice-Boltzmann method; Time-driven hard-sphere model

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