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  • 8/14/2019 The Second IASTED International Conference on Environmental

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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