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longitudinal dispersion in nonuniform isotropic porous media

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193<br />

max1mum error). The breakthrough curve for the exit concentration from<br />

a f<strong>in</strong>ite medium has a maximum error of about 4% relative to the other<br />

solutions when X = 80. The solution for a semi-<strong>in</strong>f<strong>in</strong>ite medium with a<br />

flux boundary condition is approximated to with<strong>in</strong> 2% for X = 8.0<br />

(Figure B.3) by the solution for an <strong>in</strong>f<strong>in</strong>ite medium.<br />

For high Peclet flows (Pe > 1.0), we can write for the <strong>dispersion</strong><br />

coefficient 1n a uniform medium<br />

DL > vd/2<br />

Us<strong>in</strong>g this <strong>in</strong> the expression for X we f<strong>in</strong>d,<br />

X < 2x/d<br />

which says that X is less than two times the number of gra<strong>in</strong> diameters<br />

downstream. Thus, for Pe > 1.0, equation (B.6) approximates equation<br />

(B.12) with<strong>in</strong> 2% maximum error for X = 8.0, which is less than 16 gra<strong>in</strong><br />

diameters downstream. This is probably well with<strong>in</strong> the accuracy<br />

requirements for most situations. By 48 gra<strong>in</strong> diameters downstream,<br />

equations (B.6), (B.ll), and (B.12) have less than 1% maximum error.<br />

For low Pee let number flows (Pe < 1.0), DL tends to a constant, which<br />

means X + 0 as v + 0 for a given x. Under these conditions, the<br />

different solutions accord<strong>in</strong>g to the different boundary conditions may<br />

rema<strong>in</strong> dist<strong>in</strong>ct far enough downstream to be significant.

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