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User's guide of Proceessing Modflow 5.0

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126 Processing <strong>Modflow</strong><br />

3 -1<br />

where n j,i,k [-] is the porosity <strong>of</strong> the porous medium in the cell [j, i, k]; K d [L M ] is the<br />

distribution coefficient that depends on the solute species, nature <strong>of</strong> the porous medium, and<br />

-3<br />

other conditions <strong>of</strong> the system; and D b [ML ] is the bulk density <strong>of</strong> the porous medium. The<br />

bulk density is the ratio <strong>of</strong> the mass <strong>of</strong> dried soil to total volume <strong>of</strong> the soil.<br />

¯C j,i,k ' K f @ C a<br />

j,i,k<br />

R j,i,k ' 1 % D b<br />

n j,i,k<br />

¯C j,i,k ' K L @ ¯S @ C j,i,k<br />

1 % K L @ C j,i,k<br />

R j,i,k ' 1 % D b<br />

n j,i,k<br />

@ a @ C a&1<br />

j,i,k @ K f<br />

@<br />

K L @ ¯S<br />

(1 % K L @ C j,i,k ) 2<br />

3 -1<br />

where K [L M ] is the Langmuir constant and ¯S<br />

-1<br />

[MM ] is the maximum amount <strong>of</strong> the<br />

)CRCT i,j,k ' & )t<br />

@ 81@C i,j,k % 82@ Ri,j,k Db @ ¯C i,j,k<br />

ni,j,k -1 -1<br />

where 8 1 [T ] is the first-order rate constant for the dissolved phase; 8 2 [T ] is the first-order<br />

rate constant for the sorbed phase; )t is the transport time-step; and ¯C j,i,k is the mass <strong>of</strong> the<br />

solute species adsorbed on the solids per unit bulk dry mass <strong>of</strong> the porous medium at the<br />

3.6.3 MT3D<br />

The Freundlich isotherm is a non-linear isotherm, which can be expressed in eq. 3.43.<br />

The retardation factor at the beginning <strong>of</strong> each transport step is calculated by eq. 3.44.<br />

(3.43)<br />

(3.44)<br />

where C j,i,k is the solute concentration in the cell in the cell [j, i, k] at the beginning <strong>of</strong> each<br />

3 -1<br />

transport step; a [-] is the Freundlich exponent; and K f [L M ] is the Freundlich constant.<br />

The Langmuir non-linear sorption isotherm is described by eq. 3.45. The retardation<br />

factor at the beginning <strong>of</strong> each transport step is calculated by 3.46.<br />

L<br />

solute that can be adsorbed by the soil matrix.<br />

(3.45)<br />

(3.46)<br />

For more information on the mathematical description <strong>of</strong> adsorption and transport <strong>of</strong><br />

reactive solutes in soil, the user can refer to Travis (1978) or Bear and Verruijt (1987).<br />

< Simulate the radioactive decay or biodegradation: Check this box to simulate the effect<br />

<strong>of</strong> the first-order irreversible rate reactions. The concentration change due to the chemical<br />

reaction from one transport step to another transport step at cell [j, i, k] can be expressed as<br />

(3.47)

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