Title of article
Modeling of cluster structure-dependent drag with Eulerian approach for circulating fluidized beds
Author/Authors
Shuai، نويسنده , , Wang and Huilin، نويسنده , , Lu and Guodong، نويسنده , , Liu and Zhiheng، نويسنده , , Sheng and Pengfei، نويسنده , , Xu and Gidaspow، نويسنده , , Dimitri، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2011
Pages
13
From page
98
To page
110
Abstract
Flow behavior of gas and solids is simulated in combination the gas–solid two-fluid model with a cluster structure-dependent (CSD) drag coefficient model. The dispersed phase is modeled by a Eulerian approach based upon the kinetic theory of granular flow (KTGF) including models for describing the dispersed phase interactions with the continuous phase. The drag forces of gas–solid phases are predicted from the local structure parameters of the dense and dilute phases based on the minimization of the energy consumed by heterogeneous drag. The cluster structure-dependent (CSD) drag coefficients are incorporated into the two-fluid model to simulate flow behavior of gas and particles in a riser. Simulation results indicate that the dynamic formation and dissolution of clusters can be captured with the cluster structure-dependent drag coefficient model. Simulated solid velocity and concentration of particles profiles are in reasonable agreement with experimental results.
Keywords
Cluster structure-dependent drag coefficient model , Kinetic theory of granular flow , Numerical simulation , Computational fluid dynamics , Riser
Journal title
Powder Technology
Serial Year
2011
Journal title
Powder Technology
Record number
1700057
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