(388af) Effect of the Flow Field of An Internally Spout-Fluid Bed On Dispersion of Glass Fibre for Thermoplastic Composites Manufacture

Effect of the Flow Field of  an Internally Spout-fluid
Bed on
Dispersion of Glass Fiber for Thermoplastic Composites Manufacture

Yuan Zong^a, Xiaogang Yang^b, Gance Dai^a, Ling Zhao^a*

^a Department of Chemical
Engineering

East China University
of Science and Technology,
Shanghai 200239 China

^b Institute for Arts, Science and
Technology

Glyndŵr University, Wrexham, LL11 2AW UK

^*Corresponding Author's
E-mails: zhaoling@ecust.edu.cn

Keywords: Fibre
flocs; Dispersion; Spout-fluid
bed; Numerical simulation

Abstract

The mechanical and thermal properties of  glass
fibre-reinforced thermoplastics have close
relationship with the impregnation of glass fiber by high viscosity resin. A novel methodology
of  dispersion and pre-mixing for
components integratedly by applying a modified
spout-fluid bed has been pioneered by State Key Laboratory of Chemical Engineering
(China). The modified spout-fluid bed was mounted draft tube and disk-baffle to
endow it with special flow field. The mechanics of fiber dispersion in the
internally spout-fluid bed  was
investigated using Large Eddy Simulation (LES) modeling and reported in a previous paper (Zong, Yang and Dai, 2011). This study attempts to reveal correlations
between fibre dispersion and the flow field by numerical
simulation. The motion of fibers was modeled by species transport equation, coupled
with the turbulent shear flow in the spout-fluid bed. The
correlation between the fibre concentration and local vorticity was obtained from the simulation. The results showed existence of a
strong correlation between the glass fiber concentration and local vorticity. A
local high vorticity corresponds a relatively high glass fiber concentration.
Due to the addition of the internals (draft tube and disk-baffle) into the
spout-fluid bed, the flow field were significantly altered and has a
characteristics of relatively uniquely distribution of high turbulence, which
was proved to be benefit to the manufacture of  fiber reinforced thermoplastic.

References

1.       Zong, Y.,
Yang, X. and Dai, G. (2011) Design simulation of glass-fiber-loaded flow in an
internally spout-fluidized bed for processing of thermoplastic composites. I.
Flow characterization. Ind. Eng. Chem. Res. 2011, 50(15), pp.
9181-9196 .

Figures                 

                          
    Fig.1. Time-averaged LES velocity
distributions

Fig. 2 Velocity vector in entry region and
impinging region. (a) impinging region; (b) entry region. 

 Fig. 3  Turbulent kinetic energy distribution at
different position( D_N is the diameter of the spouting nozzle). (a ) Along the  centerline; (b)   impinging region z/DN=32.2;(c)
outlet region  z/DN=38.9.

Fig. 4  Axial Reynolds stress along the
centerline. (a) ¦Ñu_z^'2;(b) ¦Ñu_r^'2

Fig. 5 Vorticity
distribution and corresponding fiber distribution inside the reactor.  (a) 
Vorticity distribution ; (b) Fiber concentration distribution

Fig.6  Distribution of correlation coefficient
|¦Ã| at different position.( a) axial distribution
along the centerline;(b) radial distributions at z/D_b=32.2 and z/D_b=38.9
.

Fig.7  Profiles of flocculation intensity (Fl)
at different location. (a)  
axial distribution along the centerline£»(b) radial distributions
at z/D_b=32.2 and z/D_b=38.9 .