Environmental Engineering Reference
In-Depth Information
Considering that P α in the nucleation experiments is normally not far from 1 atm and Δ P for the
critical drop is higher essentially we can put P β ≅ Δ P . To know the Debye frequency as a function of
pressure it is enough to know the dependence of sound velocity on pressure (see Equation 19.62) (the
density ρ β is a very weak function of pressure). In Ref. [48] the sound velocity of liquid Cs was mea-
sured in the range of temperatures 300-1500 K and pressure 2 × 10 6 − 6 × 10 7 Pa. The experimental
measurements can be approximated by the following empirical function:
2
)) .
0 1
u
(
m s
/ ≈
)
1.475 10 ( Pa)
×
P
(
+ P T
0
(
(19.66)
where P 0 = (7.35, 6.78, and 6.10) × 10 7 Pa for temperatures 508, 530, and 554 K, respectively. For
the irst iteration we set the pressure to be 1 atm (1.013 × 10 5 Pa), then, using the density of liquid
Cs from Table 19.1 and Equations 19.66 and 19.62 we get u = 903, 895, and 886 m/s and ν max =
(1.80, 1.79, and 1.77) × 10 12 s −1 for T = 508, 530, and 554 K, respectively.
The joint solution of Equations 19.61, 19.62, and 19.64 is shown in Figure 19.4 as ln(σ S ) ver-
sus ln R S . The Tolman length δ can be determined solving the GTKB differential equation (19.5)
which contains d ln (σ S ( R S )/σ )/ d ln( R S ) in the LHS and the RHS contains only δ/ R S . One can see
from Figure 19.4 that within the experimental accuracy the dependence ln(σ S ( R S )/σ ) on ln( R S )
can be approximated by a linear function with a constant slope d ln(σ S ( R S )/σ )/ d ln( R S ) = −0.240,
TABLE 19.1
Important Parameters for Liquid Metals Used in Calculations
Metal
T 0  ( K )
ψ  (Dyne/cm/K)
C
D  (K)
ρ  (g/cm 3 )
κ  (cm 2 /Dyne)
Li
3300
0.140
8.00
8120
0.47
1.0 × 10 −11
Na
2350
0.100
7.70
5460
0.87
2.3 × 10 −11
Cs
1790
0.048
7.25
3920
1.75
7.0 × 10 −11
Ag
6980
0.161
8.92
14464
9.35
1.4 × 10 −12
Hg
2540
0.210
8.04
3215
12.8
3.8 × 10 −12
Mg
3128
0.254
8.80
7674
1.59
5.1 × 10 −12
Zn
5430
0.167
8.35
6400
6.75
1.9 × 10 −12
0.37
554 K
Cs
0.36
0.35
530 K
0.34
0.33
T = 508 K
0.32
0.31
0.30
0.29
0.28
0.30
0.32
0.34
0.36
In R s (nm)
FIGURE 19.4  ln(σ S ) versus ln R S as calculated by solution of Equations 19.61 and 19.64 using the experi-
mental measurements of the nucleation rate from the vapor of Cs (Figure 19.3). Open and illed symbols are
results of the irst and second iterations, respectively. Lines are linear ittings.
 
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