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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where<br />
and<br />
An energy balance is used to relate the particle temperature to the reaction rate:<br />
− mC p, p<br />
S g<br />
dTp dt + qheatΔH = − Nu<br />
d (1− e ) p (T 4 4<br />
p − Tg) + (Tp − Tw ) (6.10)<br />
= C p, g d p o q heat<br />
M C Nu<br />
ΔH = 1<br />
M C<br />
72<br />
(6.11)<br />
[ (1 − )ΔH CO + ΔH CO2]<br />
(6.12)<br />
where ΔH CO and ΔH CO2 are the heats of reaction per mole carbon for the reactions C + 0.5<br />
O 2 = CO and C + O 2 = CO 2, respectively. In some cases T p is measured or controlled<br />
(e.g., fixed bed combustion) and the energy balance step can be skipped. The procedure<br />
for solving the energy balance equation is:<br />
1. guess a value for T p;<br />
2. go through the P s loop and compute the converged value of reaction rate<br />
(denoted as q ps here): q ps = q rxn = q diff;<br />
3. compute the value of q heat from the energy equation (6.10);<br />
4. calculate the difference between the value of q ps from the P s loop and q heat from<br />
the energy equation;<br />
5. Guess a new value for T p using Newton-Raphson method so that the difference<br />
q = (q – q heat) is zero. Notice that this new T p changes the value of q from the<br />
P s loop.