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MODELING CHAR OXIDATION AS A FUNCTION OF PRESSURE ...

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Introduction<br />

4. Analytical Solutions of the Effectiveness Factors<br />

Pore diffusion effects can be treated with either a full numerical solution radially<br />

through the porous char matrix (Reade, 1996), or treated using the analytical Thiele<br />

modulus approach (Thiele, 1939). Since the char particle reactivity is often sought for<br />

inclusion into a comprehensive model of a coal combustor, an analytical solution is<br />

preferred here over the full numerical solution.<br />

It was shown in the literature review that the effectiveness factor can be<br />

approximately predicted by the asymptotic solution in spherical coordinates (Thiele,<br />

1939; Bischoff, 1965):<br />

= 1<br />

M T<br />

⎛ 1<br />

⎝ tanh(3MT ) ⎜<br />

where M T is the general Thiele modulus, which is<br />

M T = L<br />

(m + 1)<br />

2<br />

for the m-th order rate equation, and<br />

M T = L<br />

o k 1<br />

2D e<br />

1 ⎞<br />

− ⎟ (4.1)<br />

3MT ⎠<br />

okmC m −1<br />

s<br />

De 27<br />

(4.2)<br />

KCs (1 + KCs ) [KCs − ln(1 + KC 1<br />

2<br />

s )]− (4.3)<br />

for the Langmuir rate equation. It was also shown that the classic asymptotic solution of<br />

the effectiveness factor is inaccurate when the general Thiele modulus is in the<br />

intermediate range, and the error can be up to 24% in Cartesian coordinates, as shown in

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