A computational (DEM) study of fluidized beds with particle size distribution, APT2003 Tagami &...
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![Page 1: A computational (DEM) study of fluidized beds with particle size distribution, APT2003 Tagami & Horio](https://reader034.fdocuments.in/reader034/viewer/2022051112/557c83b5d8b42a8a208b486c/html5/thumbnails/1.jpg)
19th/12/2003 N.Tagami and M.Horio 1
A Computational Study of Fluidized
beds with Particle Size Distribution
N. Tagami and M. Horio
Tokyo University of Agriculture and Technology
Department of Chemical Engineering
Tokyo, Japan
Presented at:
The Second Asian Particle Technology Symposium (APT 2003)
17th-19th December 2003, Penang, Malaysia
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19th/12/2003 N.Tagami and M.Horio 2
Contents
1. Introduction
2. Modifications of fluid drag calculation
3. Calculation results
4. Conclusions
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19th/12/2003 N.Tagami and M.Horio 3
Introduction
With our code SAFIRE, we have
demonstrated that the discrete element
method (DEM) can be a powerful tool for
industrial chemical reactor design issues.
However, so far, most of the work in the literature
has limited within uniformly sized particles.
There is insufficient consideration about the
effect of particle size distribution (PSD)
present in a fluidized bed
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19th/12/2003 N.Tagami and M.Horio 4
What happens with the introduction of
PSD ?
(1) Fluid drag acting on each
particle should be assigned
depending on relative velocity
and particle size.
(2) Three dimensional calculation
becomes inevitable
(3) Drag force is assigned to each
particle depending on the
particle alignment
In this work SAFIRE was
modified in terms of (1) and (2).
(2) 2D → 3D
(1) non-even
fluid drag
(3) fluid drag
dependency
on alignment
thickness
2D → 3D
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19th/12/2003 N.Tagami and M.Horio 5
Pressure drop in a dense phase is given by
Ergun(1952)
Determination of CD from fixed bed data
vuvu1.75ρ
d
με1150
d
ε-1
LgρΔPΔP
fp
f
p
f
*
densityFluid:ρ
fractionVoid:ε
diameterParticle:d
areaProjected:A
f
p
p
Drag coefficient defined with mean diameter:
2
f
2p
pf
D
vuρd
F8C
Equation of fluid motion for 1D steady flow:
0gερFnΔL
ΔPε fpf /6dπ/ε1n
3p
2.33
vuερd
με1200C
fp
fErgunD,
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19th/12/2003 N.Tagami and M.Horio 6
Approximate expression for CD
corresponding to Ergun correlation
2.33
vuερd
με1200C
fp
fErgunD,
2.33
vuερd
με1200C
fp
fErgunD,
extension for individual particle
extension to a system with a wide PSD
2.33
ε
ε1
vuρd
200μC
fp
fErgunD,
effect of could be different in the mixed particle
system, but let’s use the same expression
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19th/12/2003 N.Tagami and M.Horio 7
Dense phase
2.33vuερd
με1200C
fp
fErgunD,
Drag coefficients
Wen-Yu(1966) correlation
sD,
3.7
WYD, CεC
where
700Re0.44
700Re0.15Re1Re
24C 0.687
sD,
0.40.6
0.8
1.0
1
10
100
1000
10000
0.0 0.4 0.8 1.2 1.6
Single particle
From Ergun Eq.
From Wen-Yu Eq.
Ap
pa
ren
t d
rag
co
effic
ien
t [-
]
Interstitial fluid velocity [m/s]
Void
age [-]
Dilute phase
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19th/12/2003 N.Tagami and M.Horio 8
Governing equations Translational motion of particle
Rotational motion of particle
Equation of continuity for fluid
Equation of motion for fluid
gFFFFv
mdt
dm fpcohesionpwcollision,ppcollision,
wallfpcohesionpwcollision,ppcollision,dt
dI MMMMMω
0
t
ε
t
ε
u
gFσuu
fpff ερnx
εx
ut
ερ
velocityAngular
tensorStress
fractionVoid
particleaofVelocityv
fluidofVelocityu
particleaofMassm
MomentM
inertiaofMomentI
ForceF
:
:
:
:
:
:
:
:
:
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19th/12/2003 N.Tagami and M.Horio 9
Objectives of the present
computation
To
•confirm the present fluid-particle interaction
treatment satisfy Ergun correlation
macroscopically for systems with PSD.
•analyze the effect of PSD on macroscopic
fluidized bed behavior for cases with the same
mean particle size (dpsv) and total bed volume.
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19th/12/2003 N.Tagami and M.Horio 10
dp1/dp2 [mm/mm] Number of particles
1.00 30000
1.10 / 0.917 (1.20) 11270 / 19474
1.20 / 0.857 (1.40) 8681 / 23819
1.50 / 0.750 (2.00) 4444 / 35556
][00.12
3
mmdN
dN
p
p
The average surface to
volume diameter is identical
for each calculation as
The total volume and surface
area of the particles are also
held constant
][1043.9
][1057.1
22
35
mS
mV
total
total
Computational Conditions
(continued)
dpsv=
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19th/12/2003 N.Tagami and M.Horio 11 Air
(continued)
App. 54mm
50mm
10mm
200mm
0
0.5
1.122
1.0 Time[s] S
up
erf
icia
l ve
locity [m
/s]
Linear Spring Spring constant : 800N/m
Linear dashpot Restitution coefficient : 0.9
Particle density : 2650 kg/m3
Friction coefficient : 0.3
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19th/12/2003 N.Tagami and M.Horio 12
Calculation results
1.00mm 30000 1.10mm 11270
0.917mm 19474
1.20mm 8681
0.857mm 23819 1.50mm 4444
0.750mm 35556
dp1/dp2= 1.2 1.4 2.0
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19th/12/2003 N.Tagami and M.Horio 13
Comparison of fluid drag force
acting on each fluid cell Blue zone: fluid drag force numerically determined
agrees with Ergun correlation + 20% in each fluid cell
(Fdrag coefficitent) / (FErgun,fluid cell)
dp1/dp2= 1.2 1.4 2.0
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19th/12/2003 N.Tagami and M.Horio 14
Total translational kinetic energy increases
as the difference in particle size increases
Total translational kinetic energy
0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 0.0
0.2
0.4
0.6
0.8
Uniform system
Binary system
dp1/dp2=1.2
dp1/dp2=1.4
dp1/dp2=2.0
To
tal tr
ansla
tional kin
etic e
nerg
y [
mJ]
Time [s]
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19th/12/2003 N.Tagami and M.Horio 15
0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.00
5000
10000
15000
20000
25000
30000
0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.00
5000
10000
15000
20000
25000
30000
0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.00
5000
10000
15000
20000
25000
30000
Cumulative number of collisions
Uniform system
dp=1.00mm
Binary system
dp=1.10mm Binary system
dp=0.917mm
Cum
ula
tive n
um
ber
of colli
sio
ns [
#]
Time [s] (continued)
Ten particles are
traced in each
component
dp1/dp2
= 1.2
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19th/12/2003 N.Tagami and M.Horio 16
0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.00
5000
10000
15000
20000
25000
30000
dp1/dp2
= 1.4
0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.00
5000
10000
15000
20000
25000
30000
0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.00
5000
10000
15000
20000
25000
30000
0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.00
5000
10000
15000
20000
25000
30000
Binary system
dp=1.50mm
Binary system
dp=1.20mm
Binary system
dp=0.857mm
Binary system
dp=0.750mm
Cum
ula
tive n
um
ber
of colli
sio
n [
#]
(continued)
Time [s]
dp1/dp2
= 2.0
0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.00
5000
10000
15000
20000
25000
30000
Uniform system
dp=1.00mm In the binary system
momentum transportation
between particles is
emphasized
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19th/12/2003 N.Tagami and M.Horio 17
Conclusions
To achieve the DEM simulation with PSD,
modification of fluid drag force calculation is needed.
In the present study, the drag force is
computed using the drag coefficient combined
with Ergun correlation.
The calculation results show that reasonable fluid
drag force is calculated for each fluid cell.
The bed motion activity increases due to
the existence of particle size distribution