Environmental Engineering Reference
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gas
liquid film
bulk liquid
c
co
2
c
co
2
z=0
z=L
z
Figure 5.4.2
Concentration profi le at the gas liquid interface
C
CO
2
,i
is the equilibrium concentration in the fl uid phase and C*
CO
2
is the actual (non-
equilibrium) concentration.
L
is the typical thickness of the interfacial layer.
approximate concentration profi le at the liquid-vapor interface. In this
scenario, we see that the gas phase is well mixed, so the gas concentra-
tion is constant in the gas phase. The liquid phase however is not well
mixed and we see that next to the gas interface the CO
2
concentration is
higher compared to the concentration in the bulk liquid. Because of this
concentration gradient, CO
2
will diffuse from the interface to the bulk.
This diffusion process follows
Fick's law
, which states that the fl ux (in
molecules per unit area per unit time) is proportional to the gradient in the
concentration:
dc
CO
2
j
=−
D
,
CO
CO
dz
2
2
where
D
CO
2
is the diffusion coeffi cient of CO
2
in the liquid phase. If this
diffusion coeffi cient is suffi ciently high then the fl ux of CO
2
can keep up
with the fl ux of CO
2
from the fl ue gas. If, however, the diffusion coeffi cient
is small it can be a limiting factor in the process.
To quantify this effect let us consider a mass balance (
Figure 5.4.3
)
on a small volume across the interfacial region:
accumulation
=
fl ow in - fl ow out
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