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\section{Aerosols  and coagulation}
 [Refs]: 

 Present, {\bf Kinetic Theory of Gases}

Fuchs, {\bf  Mechanics of Aerosols}

Friedlander, {\bf Smoke, Dust and Haze}

Seinfeld, {\bf Atmospheric Chemistry and
 Physics of Air Pollution}

 Levich: {\bf Physio-Chemical Hydrodynamics}
\subsection{Brownian diffusion  of particles} 

Particles of sub-micrometer size collide with air molecules 
randomly. and behave collectively as a gas. 

 Let $n(z)=$ number of particles per unit volume, i.e, the number
density of Brownian particles in air.    By the perfect gas law, 
\be p = nkT,  
\label{perfect gas law}\ee where $k$ is Boltzmann's constant
\[ k =R/L,\]
  \[ R=\mbox{Universal gas constant}  = 8.317\times 10^{7}
\mbox{ergs/degree/mole}\]
and \[L= \mbox{Avogadro's number} = 6.025 \times 10^{23}
\mbox{molecules /mole} = 2 \mbox{calories /degree /mole} \]
When the cloud of particles is  in
hydrostatic equilibrium,  
\be {dp\over dz}=-\rho g = -{ nmg}  \ee 
where $m$ is the mass per particle. Combining the preceding two
equations, 
\be  - {dp\over p} = {mg\over kT} dz\] hence, \[ p(z)=p(0)\exp
\left(- {mgz\over kT}\right)\label{static press}\ee and
\be n(z)=n(0) \exp \left( -{mgz\over kT}\right)\label{static
number}\ee which is Bolzmann's law.


Alternatively,  random collisions on the microscale give rise to
diffusion on the macroscale. At the  equilibrium state, diffusion and
gravitational convection must balance each other so that,  
\be -D{dn\over dz} - nV =0\label{(3)}\ee  where $V=$ fall  velocity.
Equating Stokes drag with the particle weight 
$ 6\pi \mu aV = mg$,  we get 
\be V={mg\over 6 \pi\mu a}\label{(4)} \ee
 Solving (\ref{(3)}) and using (\ref{(4)}),  
\be n(z)=n(0) \exp \left( -\f{mgz}{D6\pi \mu a}\right)\label{static
number'}\ee
 Upon comparison with (\ref{static number}), the Brownian diffusivity can be identified
\be
D={kT\over 6\pi\mu a}\label{Brownian diffusivity}\ee
 This formula, due to Einstein (1905) and Smoluchowski (1906),  is valid  if $2 a
$ is smaller than the mean free path $\ell$ of air molecules.  Otherwise
Cunningham's empirical correction is needed,
\be D=C_c\left({kT\over 6\pi\mu a}\right)\ee where \be
C_c=1+{\ell\over a} \left[ 1.257 + 0.4\exp \lp  -\f{1.1a}{
\ell}\rp\right] \ee is the correction factor. 

For aerosol particles in air under normal temperature,  the diffusivity is 
\be D\approx \f{1\times 10^{-3}}{2a}\f{10^{-2}}{0.15\times 10^{-3}}=\f{0.325\times 10^{-11}}{a}\ee
As a rough order-estimate (Levich), we use Eistein's formula for water  at room temperature, the Brownian diffusivity for colloidal particles is
\be D\approx \f{0.55 \times 10^{-13}}{a}\ee

In the following table taken from   Seinfeld, p. 325, $D$ and $\nu$ are
compared.  For gases, the mean free path is typically $\ell =
10^{-5}\sim 10^{-6}$ cm.  
\vspace{0.2in}


\begin{tabular}{|c|c|c|}\hline 
  2 a\,\, ($\mu$ m)  &   D \,\, ($cm^2/s \,\,(T=20^\circ$)  & 
$ V$ \,\, (cm/sec) ($\rho_s = 1g/cm^3)$ \\
 \hline
   0.001 & 5.14 $\times 10^{-2}$ &\\
 0.01 & 5.25 $\times 10^{-4}$ &\\  
 0.1 & 6.75 $\times 10^{-6}$ & 8.62 $\times 10^{-5}$\\  
  1 & 2.77 $\times  10^{-7}$ & 3.52 $\times 10^{-3}$\\
 10 &  & 3.07 $\times 10^{-3}$\\
 100 && 30.3 \\ \hline
\end{tabular}

\subsection{ Coagulation due to Brownian diffusion}
When small particles are bounced  around randomly by
surrounding fluid molecules, they may come so close to one another that
Van der Waals force  binds them together. This is 
coagulation. In a moving fluid   additional factors such as  fluid shear and  Columb
forces may intervene. A simple model (by Smoluchowski) for a stationary fluid with  
 identical spherical 
   particles of  radius $a$ is as follows .
\begin{figure}[h]\begin{center}
\includegraphics[scale=0.75]{coagulation.eps}
\label{fig:coagulation} \end{center}
\caption{Left: A spherical shell. Right: Two spherical particles in collision.}
\end{figure}

Let us focus   attention on a fixed particle. Consider a spherical shell 
from $ r $ to  $ r+dr$, Figure \ref{fig:coagulation}-left. The  rate of increase of particles inside the
shell is
\[{\partial n\over \partial t}\ 4\pi r^2 dr\]
which must be equal to the  net influx through the two
surfaces of the shell  
\[ - {\partial \over\partial r}\left(-4 \pi r^2 D{\partial
n\over\partial r}\right)dr\]
thus, 
\be {\partial n\over \partial t} = \f{D}{ r^2}\f{\partial}{ \p r}
\left(r^2 \f{\partial n}{\partial r}\right)\label{(11)} \ee 
Assume that whenever two particles come into contact they stick to each other and become
one. Therefore the spherical surface of radius $2a$ concentric with
the stationary   particle acts as a sink, on which $n = 0$, i.e.,  
\be  n  =0\qquad r =2a\label{(12 )}\ee 
\be n  \to n_\infty \qquad  r \to
\infty\label{(13)}\ee 
See Figure \ref{fig:coagulation}-right. The initial condition   is 
\be n= n_\infty,\quad 2a<r<\infty \quad t= 0\label{(14)}\ee

Th solution can be facilitated by introducing
\be  w = \f{n_\infty -n}{ n_\infty}\left(\f{r}{
2a}\right)\label{(15)}\ee
and 
\be  x = \f{r-2a}{ 2a} \label{(16)}\ee
it is shown in Appendix A that  \be  \f{\p w}{\partial t} =D'
 \f{\partial^2 w}{ \partial x^2}\label{(17)}\ee
where
 \be   D' = \f{D}{(2a)^2} \label{(18)}\ee
The boundary conditions become, 
\be    
w=1, \quad x = 0, \label{(19)}\ee
while 
\be  w=0,  \quad x=\infty \label{(10)}\ee
The initial condition is  
\be w = 0, \quad  t= 0, x>0 
\label{(111)}\ee



  The solution,  which can be obtained by the  similarity method (see Appendix B), is:
\be  w=1- \mbox{erf}\lp \f{x}{2\sqrt{Dt}} \rp= 1
-\sqrt{\f{2}{\pi}}\int_0^{\f{x}{2\sqrt{Dt}}}e^{-z^{2}}dz \ee
or, \[ \f{n_\infty - n(r,t)}{ n_\infty} =1-\sqrt{\f{2}{\pi}}\int_0^{\f{r-2a}{2\sqrt{Dt}}}e^{-z^{2}}dz \]
or \[
 1-\f{n}{ n\infty}=1-\f{2a}{ r}\left[1-\sqrt{\f{2}{
\pi}}\int_0^{\f{r-2a}{2\sqrt{Dt}}}e^{-z^{2}}dz\right]\]
Finally, the number concentration near a fixed particle is 
\be \f{n(r,t)}{ n_\infty}=1-\f{2a}{ r}+\f{2a}{r}\sqrt{\f{2}{
\pi}}\int_o^{\f{r-2a}{2\sqrt{Dt}}}e^{-z^{2}}dz =1-\f{2a}{ r}+ \f{2a}{ r}\,
 \hbox{erf} 
\left(\f{r-2a}{ 2Dt}\right)\label{(23)}\ee


 

We now use this information to find the rate of coagulation when all particles are moving, by calculating  the number density of particles in the process of collision.   Starting from one particle, the rate of flux of particle across the sphere of radius $r=2a$ is
\be J(t) =4\pi r^2 D\lb\f{\p n}{\p r}\rb_{r=2a}= 4\pi D(2a)
n_\infty
\lp 1 + \f{2a}{\sqrt{\pi D t }} \rp\ee
When \[ t \gg \f{(2a)^2}{D}\] we get the steady state limit,
\be J(\infty) = 4\pi D(2a)n_\infty = 8 \pi Da n_\infty \ee
Let us estimate  $D=10^{-4} \, cm^2/sec$, and $2a= 10^{-6} cm$,  then the  time to steady state is
$\f{(2a)^2}{D} = 10^{-8} sec$ and is very short. 

Each stationary particle will be hit by,  hence coagulate with, $8 \pi D\
a\ n_\infty$ particles per second.   Since all particles are moving, 
the steady rate of collision (coagulation) must be doubled, i.e., $16 \pi D a\ni $.
As the consequence,    the number density of particles.
must decrease.   Each collision
reduces the number of particles by 1. Hence
\be {d \ni\o dt}=-16 \pi a D \ni^2\ee
Thus
\[ \f{d \ni}{ dt}=-16\pi a D \ni^2\quad\mbox{where}\quad D=\f{kT}{ 6
\pi\mu a}\]
or 
\[\f{d\ni}{ \ni^2}=-16\pi aD dt \]
which may integrated to 
\[-\left[\f{1}{ \ni}-\f{1}{ \ni(0)}\right]=- 16\pi aDT\qquad \]
Note that 
\[ 16\pi aD = \f{16\pi
akT}{6\pi \mu a} =\f{8}{
3}\f{kT}{\mu} \]
Finally,
\be \ni(t) = \f{\ni(0)}{1+[16\pi a D]\ni(0) t} 
 =\f{\ni(0)}{1+K_o \ni(0) t}\ee
where
\be 
 K_o= 16 \pi aD = \f{8}{ 3} \f{kT}{ \mu}\ee 
is the  coagulation constant while 
\be T_{coag}=\f{1}{K_o\ni(0)}\ee
 is the coagulation time.
 
From Fuchs, Table 28, p 291. \vspace{0.2in}

\begin{tabular}{|c|ccccc|} \hline
   a\,(cm)  & $10^{-7}$  &
$10^{-6}$  & $10^{-5}$  & $10^{-4}$
 & $10^{-3}$\\ \hline
 $ K_o \times 10^{10}$    ($ cm^3/  sec$) &
323  & 34  & 5.56  & 3.19
 & 2.98\\ \hline
\end{tabular}
 \vspace{0.2in}

 How long does it take for $\ni(t)$ to drop to one-tenth of its initial
value? 
\be t=\f{{\ni(0)\o \ni} -1}{ K_o \ni(0)}\ee
where
\[ K={4\o 3} {kT\o \mu}\]

 It can be estimated that 
$ t_{{1\o 10}}\sim 125 $ sec, 
if $ 2a=0.1\mu m$,  and $T=293^\circ K$. 

\subsection{Appendix A: Proof of (\ref{(17)})} 

\[ {\p w\o \p t} = -{r\o 2a} {1\o n_\infty} {\p n\o\p t}\]
\[{\p w\o\p x} = {\p w/\p r\o\p x/\p r} = 2a {\p w\o\p r} = 2 a \left[
{1\o 2a}{n_\infty -n\o n_\infty} - {r\o 2a} {1\o \ni} {\p n\o\p
r}\right]\]
\[= {n_\infty -n\o n_\infty} - {r\o n_\infty} \f{\p n}{ \p r}\]
\[{\p^2 w\o\p x^2} = 2a\left[ -{1\o n_\infty} {\pnpr}-{1\o
n_\infty}{\pnpr}-{r\o n_\infty}{\p^2n\o\p r^2}\right]  = -{2a\o n_\infty} r \left[ {2\o r} {\pnpr} + {\p^2 n\o\p
r^2}\right]\]
Substituting these results in   (\ref{(17)}),  we get
\be {\p n\o\p t} = D^\prime(2a)^2 \left({\p^2 n\o\p r^2} + {2\o
r}\f{\p n}{\p r}\r)={D\o r^2} {\p\o\p r}\left(r^2\f{\p n}{\p
r}\rp \ee 
 with
\[  D = D'(2a)^2\]



\subsection{Appendix B: Solution of  (\ref{(17)}) by the method of similarity} 
 

  Let us seek a   transformation
\[ x = \lambda^a x'\quad t =\lambda^bt'\quad
w=\lambda^c w' \] 
such that the initial-boundary-value problem
retains the same form.
\[{d\o\p t}\rightarrow{\p\o\p t^\'}\ \lambda^{-b}\qquad{\p\o\p
x}\rightarrow{\p\o\p x^\'}\ \lambda^{-a}\]
\[\f{\p w}{\p t}=D'{\p^2 w\o\p x^2}\ra\l^{-b+c}\lp{\p w'\o\p
t'}\rp=D'\l^{-2a+c}\lp\f{\p^2 w'}{\p x'^2} \rp \]
For invariance
we  require, $-2a = -b,\ a=b/2$. Clearly 
\[\xi=\f{x}{2\sqrt{D' t}}  =\f{\l^{b/2}x}{ 2\sqrt{D'  \lambda ^{b'}
t'}}=\f{x'}{2\sqrt{D' t'}} \]  satifies the requirement.
  From the boundary conditions,  
\[x^\'\l^a=0\qquad \l^cw^\'=1\] which requires that \be  c = 0\ee
The initial condition as well as the
boundary conditon at  $x'\l^a=\infty$ are trivially satisfied. 

 The similarity solution is 
\[w=w(\xi) =w\left({x\o 2\sqrt{D^\' t}}\r)\]
Some algebra:
\[ \f{\p w}{\p t} = w'\f{\p \xi}{\p t} = w'\f{x}{2\sqrt{D'}}\lp
-\f{1}{2t^{2/3}}\rp=
 -\f{w'\xi}{ 2
t} \]
\[ D'\f{\p^2 w}{\p x^2} = D'\f{w''}{ 4D' t}  = \f{w''}{
4 t'} \]
hence \[- {w'\xi\o 2}={w''\o 4} \]
or
\[{w''\o w'}=-2\xi\]
\[{d\log w'\o d\xi}=-2\xi\]
Integrating
\[\log(w')=-\xi^2+ \mbox{Const},\]
and \[ w'=c
e^{-\xi^{2}}={dw\o d\xi}\]
Thus \[ w = -c\int_z^\infty e^{-z^{2}}dz\]
 so that $w(\infty) = 0$. Since 
\[ w=1, \ \xi=0\]
\[
1=-c {\int_0^\infty e^{-z^{2}}dz}\]
The integral is $\sqrt{\pi}/2$. Hence 
\[ c = -\sqrt{{2\o
\pi}}\]
\[w=\sqrt{{2\o\pi}}\int^\infty_\xi
e^{-z^{2}}dz=\sqrt{2\o\pi}\left[\int_0^\infty-\int_0^\xi
e^{-z^{2}}dz\r]\]
\[=1-\sqrt{2\o\pi}\int_o^{{x\o
2\sqrt{Dt}}}e^{-z^{2}}dz\]
\end{document}