Numerical simulation of the gas-solid flow in a fluidized bed by combining discrete particle method with computational fluid dynamics

被引:1190
作者
Xu, BH
Yu, AB
机构
[1] Sch. of Mat. Science and Engineering, University of New South Wales, Sydney
关键词
fluidization; gas-solid flow; numerical simulation; discrete particle method;
D O I
10.1016/S0009-2509(97)00081-X
中图分类号
TQ [化学工业];
学科分类号
0817 [化学工程与技术];
摘要
The gas-solid flow in a fluidized bed is modelled by a combined approach of discrete particle method and computational fluid dynamics (DPM-CFD), in which the motion of individual particles is obtained by solving Newton's second law of motion and gas flow by the Navier-Stokes equation based on the concept of local average. The coupling between DPM and CFD is achieved directly by applying the principle of Newton's third law of motion to the discrete particle and continuum gas which are modelled at different length and time scales. The equations of motion for a system of particles are solved by a collision dynamic model developed in this work which, in conjunction with the predictor-corrector method, allows stiff particles (K = 50,000 Nm(-1)) to be used with a reasonable computational time step (1.5 x 10(-5) s) while conserving the energy and momentum. The gas-phase equations are solved by the conventional SIMPLE method facilitated with the Crank-Nicolson scheme to give the second order accuracy in the time discretization. The proposed model shows its capacity of simulating the gas fluidization process realistically from a fixed to fully fluidized bed via an incipient fluidization stage. This is done by a series of numerical tests to reproduce the experimental procedures in determining the minimum fluidization velocity of 2400 particles (rho(p) = 2700 kg m(-3), D = 4 x 10(-3) m) in a pseudo-three-dimensional central jet fluidized bed of dimensions 0.9 x 0.15 x 0.004 m. The hysteretic feature of bed pressure drop vs superficial gas velocity curve is obtained for the first time realistically from first principles, with the predicted minimum fluidization velocity in good agreement with experiment. It is demonstrated that the proposed model is able to capture the gas-solid flow features in a fluidized bed from the largest length and time scales relevant to the processing equipment down to the smallest ones relevant to the individual particles. (C) 1997 Elsevier Science Ltd.
引用
收藏
页码:2785 / 2809
页数:25
相关论文
共 44 条
[1]
A FLUID MECHANICAL DESCRIPTION OF FLUIDIZED BEDS [J].
ANDERSON, TB ;
JACKSON, R .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1967, 6 (04) :527-&
[2]
FLOW REGIME DIAGRAMS FOR GAS-SOLID FLUIDIZATION AND UPWARD TRANSPORT [J].
BI, HT ;
GRACE, JR .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1995, 21 (06) :1229-1236
[3]
Bideau D., 1993, DISORDER GRANULAR ME
[4]
Bird R. B., 1960, TRANSPORT PHENOMENA, DOI 10.1002/aic.690070245
[5]
LARGE PARTICLE FLUIDIZATION [J].
CRANFIELD, RR ;
GELDART, D .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (04) :935-947
[6]
A COROTATIONAL ELEMENT TIME-INTEGRATION STRATEGY FOR NONLINEAR DYNAMICS [J].
CRISFIELD, MA ;
SHI, J .
INTERNATIONAL JOURNAL FOR NUMERICAL METHODS IN ENGINEERING, 1994, 37 (11) :1897-1913
[7]
DISCRETE NUMERICAL-MODEL FOR GRANULAR ASSEMBLIES [J].
CUNDALL, PA ;
STRACK, ODL .
GEOTECHNIQUE, 1979, 29 (01) :47-65
[8]
Davidson J.F., 1985, FLUIDIZATION, V2nd
[9]
THE VOIDAGE FUNCTION FOR FLUID PARTICLE INTERACTION SYSTEMS [J].
DIFELICE, R .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1994, 20 (01) :153-159
[10]
COMPARISON OF EXPERIMENTAL AND SIMULATED GRAIN FLOWS [J].
DRAKE, TG ;
WALTON, OR .
JOURNAL OF APPLIED MECHANICS-TRANSACTIONS OF THE ASME, 1995, 62 (01) :131-135