coal selection criteria for industrial pfbc firing project 3.2 - CCSD
coal selection criteria for industrial pfbc firing project 3.2 - CCSD
coal selection criteria for industrial pfbc firing project 3.2 - CCSD
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“Coal Selection Criteria <strong>for</strong> Industrial PFBC Firing”<br />
Tomatoh-Atsuma has to limit its SOx emission below 94 ppm, NOx emission below 98<br />
ppm and dust emission below 28 mg/Nm 3 . It successfully operates under normal<br />
conditions while producing 10 ppm SOx, 40 ppm NOx and less than 10 mg/Nm 3 dust. In<br />
accomplishing this excellent result, <strong>coal</strong> with 0.9% sulfur and 1.6% nitrogen was fired<br />
and a Ca:S ratio of 3-6 was used (Koshimizu 1998).<br />
In Fukuoka, Japan, the emissions of SOx should be 76 ppm or less, NOx should be a<br />
maximum of 60 ppm and the concentration of soot and dust at the stack outlet should not<br />
exceed 30 mg/Nm 3 . To meet these requirements, Karita is <strong>firing</strong> <strong>coal</strong>s which contain<br />
1.0% or less sulfur and a maximum of 55% volatile matter.<br />
The Osaki plant faces more stringent NOx and particulates emission regulations. The<br />
maximum permissible emission limit <strong>for</strong> SOx is the same as Karita (76ppm), 19ppm <strong>for</strong><br />
NOx and 9 mg/Nm 3 <strong>for</strong> particulates. The harsh regulations were not a problem <strong>for</strong> Osaki<br />
as its technology enabled operation at full load while producing only 7.0 ppm SOx, 17.8<br />
ppm NOx and 3.5 mg/Nm 3 particulates.<br />
A correlation was developed to predict the emission of NOx from bench and pilot scale<br />
PFBC and it was found that pressure had no influence on the emission of NOx (Newby,<br />
Keairns et al. 1989):<br />
NOx = 12.25 exp(2827/T) [O2] 0.24 Xn 0.44 Y -0.1 (ppmv)<br />
where T = bed temperature (K)<br />
[O2] = volume percent oxygen in the combustion products<br />
Xn = weight percent nitrogen in the <strong>coal</strong><br />
(Eq. 3)<br />
Y = concentration of SO2 in the combustion products (ppmv)<br />
In contrast, other researchers found that NO emissions decreased with increasing pressure<br />
and increasing Ca:S ratio (Nagel, Spliethoff et al. 1999). At pressures above 4 bar and<br />
with extra sorbent feed, NO emissions reduced with increased temperature. On the other<br />
hand, N2O emissions were independent of pressure and sorbent added, but instead<br />
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