Particle Formation Handout
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Transcript of Particle Formation Handout
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Aerosol Particle Formation:Kelvin effect
Dr. Alexandra Teleki
[email protected]: 044 632 39 52ML F 18
Particle Technology Laboratory,Department of Mechanical and Process EngineeringETH Zurich, www.ptl.ethz.ch
Materials Properties and Characterization
2
Motion in Gases
Air molecules are in continuous motion
They collide among themselves because of their translational energy
The translational energy is proportional to the air temperature
Hinds, W. C., Aerosol technology: properties, behavior, and measurement of airborne particles, Wiley, New York (1999).
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Distribution of molecular velocities (Maxwell-Boltzmann distribution)
( )1 2 2
exp2 2
xx x x
mcmf c dc dckT kTπ
⎛ ⎞−⎛ ⎞= ⎜ ⎟⎜ ⎟⎝ ⎠ ⎝ ⎠
/ ak N=ℜBoltzmann constant:
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Distribution of Molecular Speed
c (m/s)
f(c)
( )3 2 2
24 exp2 2
m mcf c dc c dckT kT
ππ
⎛ ⎞−⎛ ⎞= ⎜ ⎟⎜ ⎟⎝ ⎠ ⎝ ⎠
( )1 2
08 kTc c f c dc
mπ∞ ⎛ ⎞= =∫ ⎜ ⎟
⎝ ⎠
3
5
1 23rms
TcMℜ⎛ ⎞= ⎜ ⎟
⎝ ⎠21 3
2 2aTKE N mc ℜ
= =
Kinetic energy of 1 mole of gas:
M: molecular weight of gasrms: root mean square
Molecular Velocity
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2
12z m
cn n d
λπ
= = nz: average number of collisions a particular molecule undergoes in one second
dm: molecule collision diametern: number density of molecules
1 2
2mkTπλ ν ⎛ ⎞= ⎜ ⎟
⎝ ⎠
Particle Mean Free Path
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2Kndλ
=
The ratio of the mean free path of the gas and the particle radius is the Knudsen number Kn:
Kn >> 1: Free Molecular Regime (Kinetic theory)Kn ~ 1: Transition RegimeKn << 1: Continuum Regime (Navier-Stokes)
In the Free Molecular Regime the exchange of momentum, heat & mass is determined by the kinetic theory of gases.
In the Continuum Regime the Navier-Stokes equations describe the momentum, heat and mass transfer between gas and aerosol.
Particle Knudsen Number
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Properties of Air
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Coagulation
Shrinkingby evaporationor dissolution
Fragmentation
Convection in Growth
by condensation or chemical reaction
Diffusion Settling
Convection out
Particle Dynamics
10S. K. Friedlander (1977) Smoke, Dust and Haze: Fundamentals of aerosol behavior, Wiley, New York.
Deposition of Particles in the Lung during Inhalation
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Theory: Population Balance Equation
coagulation
diffusion growth external force
( ) ( ) ( )∫ −−β+v
v~dv~vnv~nv~v,v~02
1 ( ) ( ) ( )∫∞
β−0
v~dv~nvnv~,v
convection
fragmentation
uDcβSγ
zyx u,u,u0unnuun ∇⋅+∇=⋅∇= gas velocity vector
= particle diffusivity
= velocity of particles of size v (e.g. settling)
= coagulation rate
= fragmentation rate
= fragment size distribution
continuity
( ) ( ) ( ) ( )∫∞
γ+−v
v~dv~nSv~,vvnvS
tn∂∂ un⋅∇+ nD∇⋅∇= ⎟
⎠
⎞⎜⎝
⎛∂∂
+tdvdn
vnc⋅∇−
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A phase transition is encountered in many industrial(e.g. crystallization, carbon black production) and environmental (e.g. smog formation) processes
Nucleation-Condensation
The goal is to determine:
1. the critical diameter for particle formation which isdictated by thermodynamics
2. the growth rate that is determined by thermodynamics and transport
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Key feature: The curved interface
The goal is to derive an expression relating the concentration (vapor pressure) of species A with a particle (droplet) of radius dP at equilibrium (Seinfeld, 1986)
If the interface was flat which is, for example, the tabulated equilibrium concentration or vapor pressure at a given temperature and pressure.
Consider the change in Gibbs free energy accompanying the formation of a single drop (embryo) of pure material A of diameter dP containing g molecules of A:
(1)ΔG G Gembryo system pure vapor= −
Critical Particle Size
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Now let’s say that the number of molecules in the starting condition of pure vapor is nT. After the embryo forms, the number of vapor molecules remaining is . Then the above equation is written as:
(2)
where GV and Gl are the free energies of a molecule in a liquid and vapor phases and σ is the surface energy
(3)
Noting that
Where vl is the volume occupied by a molecule in the liquid phase (equivalent sphere in liquid phase).
n n gT= −
vTPlv GndgGnGG −σπ++=Δ 2
( ) ( )ΔG g G G d dv
G G dl v PP
ll v P= − + = − +π σ
ππ σ2
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gv dl
P=π 3
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Before we go further let’s evaluate the difference in Gibbs free energy:
dG = VdP then dG = (vl - vv) dP
But vl << vv then dG = - vv dP
According to ideal gas law vv = kBT/P
Then
Where S is the saturation ratio.
G G k T dPP
k T PP
k T Sv l BP
P
BA
AB
A
A− = − = − = −∫
0 0ln ln
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Now equation 3 becomes:
Now plot ΔG as a function of dP
S <1 monotonic increase in ΔGS > 1 positive and negative contributions at small dP the surface tension dominates and the behavior of ΔG as a function of dP is close to that for S <1. For larger dP the first term becomes important.
ΔG
dP
S < 1
dP∗
S > 1
droplet at equilibriumwith surrounding vapor
ΔG dv
k T S dP
lB
volume free energy of an embryo
P
surfacefree energy
= − +π
π σ3
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ln
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At
This is the minimum possible particle size.
This equation relates the equilibrium radius of a droplet of a pure substance to the physical properties of the substance and the saturation ratio of its environment. It is called also the Kelvin equation and the critical diameter is called the Kelvin diameter.
∂∂ΔGdP
= 0 ⇒ d vk T SP
l
B
∗ =4σ
ln
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The Kelvin equation states that the vapor pressure over a curvedinterface always exceeds that of the same substance over a flat surface:
See the anchoring of the surface molecules on a flat and a curved surface. Surface molecules are anchored on two molecules on the layer below flat surfaces while on curved interfaces some are anchored on just one!These can easily escape (evaporate) from the condensed (liquid or solid) phase.
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The mechanism for particle growth refers to droplet or particle growth from gas (condensation), to crystal growth from solution etc.. In all cases mass should be transported to the particle surface.
In principle, two steps are required, a diffusional step followed by a surface reaction or rearrangement step.In condensation the former is dominant while in crystallization is the latter. In many processes both can be dominant.
Particle Growth
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Consider a single droplet growing by condensation without convection at rather dilute conditions. The goal is to determine the flux of mass to its surface. For this the vapor concentration profile around the droplet is needed at steady state:
(1)
D = vapor diffusivityC = vapor concentration
(moles/cm3)
dP
droplet
vapor molecules
0rCr
rrD
tC 2
2 =⎟⎟⎠
⎞⎜⎜⎝
⎛∂∂
∂∂
=∂∂
Mass transfer to a particle surface (continuum)
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With boundary conditions:at r = dP/2 C = Cd the equilibrium concentration at the droplet surface
at r = ∞ C = C∞ bulk vapor concentration
Solving the above equation for C as a function of r gives:
(2)
Then the rate of condensation F towards the surface is(negative r direction):
(3)
r2d1
CCCC P
d
d −=−−
∞
( )( )
2P2
P
Pd d
2d2d0CCD π
⎥⎥⎦
⎤
⎢⎢⎣
⎡+−= ∞
( ) Pd dCCD2 π−= ∞
Pdr =2
CF= -Dr
∂⎛ ⎞ Α⎜ ⎟∂⎝ ⎠
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And the rate of particle volume growth is:
where MW and ρP are the molecular weight and density of the condensing material
So the diameter growth rate is (molecules/cm2):
(4)( )
PP
dPd
MWCCD4dtdd
ρ−
= ∞
( ) ( )P
Pd
P
3P dMWCCD2MWF
dt6dd
dtdv
ρπ−
=ρ
=π
= ∞
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The collision rate per unit area is:
(5)
where c and m1 are the molecular velocity and mass and NAV the Avogadro number
so z becomes (6)( ) 21
1
BdAVm
Tk84
CCNz ⎟⎟⎠
⎞⎜⎜⎝
⎛π
−= ∞
4cCNz AV=
Mass transfer to a particle surface (free molecule)
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Then the rate of condensation F to particle surface is:
(7)
And the rate of particle volume growth is:
(8)
So the diameter growth rate is:
(9)
( )d2P
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1
BAV CCd
m2TkN/areazF −π⎟⎟⎠
⎞⎜⎜⎝
⎛π
=⋅= ∞
( )P
d2P
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1
B
P
MWCCdm2TkMWF
dtdv
ρ−π⎟⎟
⎠
⎞⎜⎜⎝
⎛π
=ρ
= ∞
( )d
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1
B
P
P CCm2TkMW2
dtdd
−⎟⎟⎠
⎞⎜⎜⎝
⎛πρ
= ∞
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For particle growth from the free molecule to continuum regime, the expression for the continuum regime is extended by an interpolation factor:
(10)
where the Knudsen number is Kn= 2λ/dP
This is called the Fuchs effect.
( )⎟⎟⎠
⎞⎜⎜⎝
⎛
++
+ρ−
= ∞2
PP
dP
Kn33.1Kn71.11Kn1
dMWCCD4
dtdd
Mass transfer to a particle surface (entire spectrum)
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Summary of the lecture
Motion in Gases
Particle DynamicsNucleation: Kelvin effectParticle Growth: Condensation
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Next lecture
Selected Fundamentals of Particle Formation and Motion
Diffusion
Heat Transfer of Matter