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1 KOZENY-CARMAN EQUATION REVISITED Jack Dvorkin -- 2009 ...

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€<br />

€<br />

€<br />

€<br />

Also, if<br />

a → b, the infinity in the denominator of the third term in the square<br />

brackets in Equation (5.2) has the same order as that in the numerator, and<br />

In Figure 5.2 we display the ratio ξ of the flux computed according to Equation<br />

€<br />

(5.2) to that according to Equation (5.3):<br />

€<br />

ξ = (1− €<br />

a2 a2 a2 1<br />

)[1+ + (1− ) ], 2 2 2<br />

b b b ln(a /b)<br />

(5.4)<br />

which behaves predictably.<br />

8<br />

q → 0.<br />

Figure 5.2. Ratio of annular flux to that through a round pipe versus the normalized radius of a<br />

kernel.<br />

The total flux through<br />

Q = Nq = −N<br />

€<br />

π ΔP<br />

8µ<br />

N pipes with a kernel is<br />

Lτ b4 (1− a2 a2<br />

)[1+ 2<br />

b b<br />

Hence the absolute permeability is<br />

kabsolute = N πb<br />

Aτ<br />

4<br />

8<br />

(1− a2<br />

b<br />

2 )[1+ a2<br />

The porosity of this block is now<br />

φ = Nπ(b2 − a 2 )l<br />

AL<br />

The specific surface area is<br />

a2<br />

+ (1− 2<br />

b b<br />

a2<br />

+ (1− 2<br />

b<br />

2 )<br />

2 )<br />

1<br />

]. (5.5)<br />

ln(a/b)<br />

1<br />

]. (5.6)<br />

ln(a/b)<br />

= Nπ(b2 − a 2 )τ<br />

. (5.7)<br />

A

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