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Drugs and the pharmaceutical sciences

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Pore Sizes <strong>and</strong> Distributions 71<br />

pressure differential of 1.66 bar. The simultaneous solution of Eqs. (3) <strong>and</strong> (5), which is<br />

graphically solved in Figure 5, is about 8.5 mm. The calculated hydrodynamic pore size of<br />

this filter is smaller than <strong>the</strong> maximum pore size, as determined by bubble point<br />

measurement. If this was reversed, it would indicate that <strong>the</strong> block had a nonuniform<br />

structure such as that produced by a dense surface skin. This means that <strong>the</strong> assumption<br />

that <strong>the</strong> capillary length is equal to <strong>the</strong> thickness of <strong>the</strong> medium is incorrect. In this block<br />

<strong>the</strong> flow radially through <strong>the</strong> filter resulted in <strong>the</strong> same pore size being calculated. There<br />

was obviously no skin or surface densification. When <strong>the</strong>re is surface densification, <strong>the</strong>re<br />

can be a discrepancy between <strong>the</strong> maximum pore size <strong>and</strong> <strong>the</strong> calculated hydrodynamic<br />

pore size. The value of L must be adjusted to take <strong>the</strong> densification into account.<br />

Sometimes it is difficult to make a conclusion that can be supported by data in <strong>the</strong><br />

determination of L for a dense surface.<br />

In membrane filters this can be very important in <strong>the</strong> determination of pore size <strong>and</strong><br />

retention characteristics. It is possible to measure <strong>the</strong> pore size distribution independently<br />

of surface densification. A rigorous analysis of this process requires <strong>the</strong> solution of <strong>the</strong><br />

flow equation for a wetted filter medium. For membrane filters in <strong>the</strong> pore size range of<br />

about 0.1–3 mm, <strong>the</strong> following equation has been developed:<br />

PV ¼ pD4 PP<br />

128 L<br />

¼ nRT ð8Þ<br />

This represents <strong>the</strong> viscous portion of <strong>the</strong> gas flow. An additional term must be<br />

added to this equation when <strong>the</strong> Knudsen number, Kn, is greater than zero. The flow<br />

equation for small capillaries is (Carman, 1956):<br />

PV ¼ pD4 DPP<br />

128hL<br />

1 þ 4Kn 2<br />

f<br />

FIGURE 6 Carbon block filter dimensions.<br />

1 ð9Þ<br />

Kn is <strong>the</strong> Knudsen number, <strong>the</strong> ratio of <strong>the</strong> mean free path of <strong>the</strong> gas molecules to<br />

<strong>the</strong> diameter of <strong>the</strong> capillary. In membrane filters <strong>the</strong> value of Kn cannot be ignored. In<br />

this equation f is a reflection factor. This factor is absent from <strong>the</strong> viscous flow equation<br />

because <strong>the</strong> molecules never reach <strong>the</strong> surface of <strong>the</strong> capillary, because a layer of

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