Human Health Risk Assessment - Raytheon
Human Health Risk Assessment - Raytheon
Human Health Risk Assessment - Raytheon
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u = Wind speed (m/s)<br />
23<br />
<strong>Human</strong> <strong>Health</strong> <strong>Risk</strong> <strong>Assessment</strong><br />
DRAFT<br />
The air/water partition coefficient used in this model is the dimensionless Henry’s Law constant,<br />
which varies with temperature, and is calculated according to equation (4-9).<br />
where:<br />
K eq<br />
H = Henry’s Law constant (atm-m 3 /mole)<br />
H<br />
= (4-9)<br />
R ⋅ T<br />
R = Ideal gas constant (8.206 x 10 -5 atm-m 3 /mole-K)<br />
T = Temperature in degrees Kelvin (K)<br />
The gas phase mass transfer coefficient in units of meters per second can be estimated from<br />
equation (4-10) based on the work of Mackay and Matsugu (1973) 7 .<br />
where:<br />
Scg = Schmidt number<br />
g<br />
−3<br />
0.<br />
78 −0.<br />
67 −0.<br />
11<br />
= 4.<br />
82x10<br />
⋅ u ⋅ ScG<br />
⋅ d e<br />
k (4-10)<br />
de = Effective diameter of the area emitting<br />
The Schmidt number is a dimensionless number that relates to the relative thickness of the<br />
surface boundary layer and is calculated according to equation (4-11).<br />
where:<br />
Sc<br />
g<br />
µ g<br />
=<br />
ρ ⋅ D<br />
µg = Viscosity of air (1.81 x 10 -4 g/cm-s)<br />
ρg = Density of air (1.2 x 10 -3 g/cm 3 )<br />
Da = Diffusivity of COPC in air (cm 2 /s)<br />
The emission rate calculated from equation (4-6) is combined with the box model described by<br />
equation (4-3) to arrive at an upper bound estimate of outdoor air concentrations in the vicinity<br />
g<br />
a<br />
(4-11)<br />
7 D. Mackay and R.S. Matsugu. 1973. Evaporation rates of liquid hydrocarbon spills on land and water. Canadian J.<br />
Chem Eng. 51:434.