the second iasted international conference on environmental
TRANSCRIPT
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COAGULATION AND ATMOSPHERIC
DISPERSION OF POLYDISPERSE
AEROSOLS
Ana T. Celada Murillo
Alejandro Salcido Gonzlez
Instituto de Investigaciones Elctricas, Mxico
The Second IASTED International Conference on Environmental Modelling and Simulation 2006
November 2006
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Transport
Dispersion
Chemical reactions
Condensation / evaporation
Nucleation
Coagulation
Gravitational sedimentation
The study of environmental impacts of atmospheric aerosols
(damages to the human health, climate changes, degradation ofvisibility, acid rain precursors , etc).
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Coagulation
Union of two aerosol particles after a collision
between them
November 2006
Accumulation mode
(0.100 - 1 m)
Nuclei mode
(0.001 0.100 m)
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Motivation
Transport and dispersion are
modeled with the gaussian
model or with Reynolds
average of mass balance
equation.
These models do not reflect the
fluctuating and random nature of
turbulent dispersion,
Smooth space-time
concentration distributions
November 2006
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Some models of transport and
dispersion of aerosols dontinclude the coagulation process
in their estimations
Concentration of smallestaerosol particles is
overestimated
Polydisperse coagulation istwice more rapid than
monodisperse.
Mistakes in the estimationsof number concentrations
Smoluchowsky's theory describes
the coagulation process with
monomers.
November 2006
Motivation
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Coagulation and dispersion model of polydisperse
aerosols
++= R
s
s RRR
dVtrdVtQdAtdVtdt
d),()(),(),(),( xxxxnxJx
=iC
i dVtFV
tF ),(1
),( xr
Lx
LzLy
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),(),(),(),(),( trtQttdt
di
s
issii rrxxrr ++=
+++=+ ),(),(),(),(),(),( trtQttttt is issiii rrxxrrr
Aerosol Production Model by
coagulation
Particle Flux
Model
= iCi dAtVt nxJr ),(
1
),( = iCi dVtrVtr ),(1
),(xr
http://modelocoag1.ppt/http://modelocoag1.ppt/http://modelocoag1.ppt/http://modelocoag1.ppt/ -
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Initially monodisperse
aerosol
Smoluchowsky Theory Spheric particles
All collisions coagulation
Binary collisions
Volume and mass are
conserved in each collision.
MFC model
Polidisperse aerosol
Aerosol Production model by Coagulation
0
200
400
600
800
1000
1200
Ni
I n t e r v a l o d e d i m e t r o s
nk(#/cm
3)
1 2 3 4 5 6
k
0
200
400
600
800
1000
1200
Ni
I n t e r v a l o d e d i m e t r o s
nk(#/cm
3)
1 2 3 4 5 61 2 3 4 5 6
kk
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A particle in the interval will be formed depending
on three factors:
K
P
Q
The probability of one collision happens
in the system
The probability that the collision
happens between particles of theintervals and
Collision result will be a new
particle in the interval
=
Aerosol production model by coagulation
http://pij.ppt/http://pij.ppt/http://pij.ppt/http://pij.ppt/http://pij.ppt/http://pij.ppt/http://pij.ppt/http://pij.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://qijk.ppt/http://pij.ppt/http://pij.ppt/http://pij.ppt/ -
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Aerosol production model by coagulation
=
= 1, )1(21
),(i
i QPQPtrr
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Particle Flux Model
ri
),(),(),( ttt ioutput
i
input
i rrr =
Lx
LzLy
++=z
iz
y
iy
x
ix
ii
output
L
tv
L
tv
L
tvtt ),(),(),(),(),( rrrrr
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e1e2
e3
riri - e1Lx ri + e1Lx
ri + e3Lz
ri - e3Lz
[ ]{[ ]}),(),(),(
1
2
tvtvt
Lkkkkkk
k
i
qqq ++=
),(),(),(1
),(
3
1 tvtvtt
kkkkk
input pppr +=
kkikkkik LL erqerp +==
Lx
Lz
Ly
Particle Flux Model
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Aerosol Dispersion Model
),(),(),( trwtrutrv iii +=
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Simulation results Coagulation and Dispersion Model
General characteristics of emission source [Buckholtz,
1980]
Emission velocity:
Stack diameter:
Stack height:
Effluent temperature:
Effective height of the
plume:
Air temperature:
Atmospheric pressure:Mean wind speed:
Cloudiness:
Atmospheric stability:
Aerosol:Density:
Diameter interval:
16.76 m/s
8.23 m
76.20 m
393.15 K
483 m
283.15 K
1 atm2.10 m/s
Sunny day without clouds
A class (Pasquill)
Aluminosilicates2.40 g cm-3
0.01-64.44 m
1.E+00
1.E+02
1.E+04
1.E+06
1.E+08
1.E+10
0.01 0.1 1 10 100
Diameter (m)
Num
berdensity
(#cm-3)
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0 1000 2000 3000 4000
Time (s)
0x100
4x107
8x107
1x108
2x108
Nu
mberdensity(#
cm-3)
Mean diameter 0.01 m
0 1000 2000 3000 4000
Time (s)
0x100
4x107
8x107
1x108
2x108
Nu
mberdensity(#
cm-3)
Mean diameter 0.12 m
With emission, dispersion and coagulation
With emission and dispersion
0 1000 2000 3000 4000
Time (s)
0x100
1x106
2x106
3x106
4x106
Numberdensity(#cm-3)
Mean diameter 0.96 m
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X=80 m
0.0E+00
3.0E+06
6.0E+06
9.0E+06
1.2E+07
-800 -400 0 400 800
Distance Z direction, (m)
Numberde
nsity(#cm
-3)
X=320 m
0.0E+00
4.0E+06
8.0E+06
1.2E+07
1.6E+07
2.0E+07
-800 -400 0 400 800
Numberdensity
(#cm
-3) n1 - 0.010 m
n2 - 0.030 m
n3 - 0.060 m
n4 - 0.120 m
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0.0E+00
2.5E+05
5.0E+05
7.5E+05
-800 -400 0 400 800
Distance Z direction, (m)
N
umberdensity
(#cm
-3)
n1 - 0.010 m
n2 - 0.030 m
n3 - 0.060 m
n4 - 0.120 m
X=3840 m
CONCLUSIONS
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CONCLUSIONS
Simulation results showed the coagulation as the main mechanism inthe consumption of the nuclei particles (diameters between 0.01 and
0.12 m) near of the source.
The coagulation produces accumulation of the particles with mean
diameters between 0.12 and 0.96 m.
Qualitatively, these results are in agreement with the observed onesby Zhu et al. in relation with aerosols of traffic emissions in two
highways at California.
Coagulation is an important mechanism in the transfer of the finest
aerosol particles.
REFERENCES
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REFERENCES
http://rmf.fciencias.unam.mx/pdf/rmf/51/4/51_4_379.pdf
http://rmf.fciencias.unam.mx/pdf/rmf/54/6/54_6_422.pdf