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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.

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