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Code Manual for CONTAIN 2.0 - Federation of American Scientists

Code Manual for CONTAIN 2.0 - Federation of American Scientists

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diffusivity being replaced by the particle diffusivity. Details <strong>of</strong> the treatment <strong>for</strong> the vapor are given<br />

in Section 12.3.<br />

Thermo~horesiS<br />

E therm=<br />

4Cti(2 + 0.6N~~li2N#3)(T~ - T~)<br />

v~D<br />

(7-45)<br />

Here, N% is the Prandtl number, C is the Cunningham slip correction given in Equation (7-17),<br />

Nti – 21/~ is the Knudsen number, where k is the molecular mean free path, ~ is the dynamic shape<br />

factor, and k~ is the user-specifiable ratio <strong>of</strong> the gas thermal conductivity to the particle<br />

conductivity. The constants Cmand C~are related to slip and thermal accommodation, respectively<br />

(see Equation (7-19)).<br />

DiffusioDhoresi$<br />

[1<br />

Pg - P,d<br />

‘@h = 4DV2 ( +0.6 N~el’2NScl’3)<br />

(w X<br />

MW1’21n ‘<br />

Pg - P,<br />

~1’2+ X~CM~j’2vdD<br />

)<br />

(7-46)<br />

In Equation (7-46), B, is the boundary layer vapor diffusivity, N%= p~p@, is the Schmidt number;<br />

P~ is the atmosphere pressure; Pv,~is the vapor pressure at the drop surface, P, is the bulk vapor<br />

pressure; ~ is the boundary layer vapor mole fraction; ~ is the molecular weight <strong>of</strong> waten ~C is<br />

the boundary layer noncondensable gas mole fraction; and WC is the molecular weight <strong>of</strong> the<br />

noncondensable gas.<br />

The expression given in Equation (7-45) <strong>for</strong> the thermophoretic collection efficiency is based upon<br />

the expression given in Equation (7-19) <strong>for</strong> therrnophoretic deposition upon structures together with<br />

the temperature gradients at the drop surface implied by the heat transfer and Nusselt number<br />

relations given <strong>for</strong> the drop in Section 12.3. Likewise, the diffksiophoresis expression is given by<br />

combining the treatment <strong>of</strong> diffbsiophoretic deposition on structures given in Equation (7-20) with<br />

the condensation/evaporation rate calculated <strong>for</strong> the drop as described in Section 12.3. The phoretic<br />

effects can be negative under certain conditions; <strong>for</strong> example, the diffusiophoretic effect is negative<br />

when the drop is evaporating. Jn such cases, the phoretic effects are still evaluated from Equations<br />

(7-45) and (7-46) and added algebraically to the other collection efficiencies. The total collection<br />

efficiency is constrained to be non-negative, however.<br />

Rev. O 7-35 6/30/97

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