MODELING CHAR OXIDATION AS A FUNCTION OF PRESSURE ...
MODELING CHAR OXIDATION AS A FUNCTION OF PRESSURE ...
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