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 />
Blockage of fuel feeding lines has been noted in Wakamatsu. This could be resolved by<br />
improving the <strong>coal</strong>’s particle size distribution and equipment modifications (Sakanishi<br />
1995). Such a problem was also reported in Osaki, where their fuel nozzle was clogged<br />
several times by <strong>for</strong>eign material in the raw <strong>coal</strong> and <strong>coal</strong> lumps. As a countermeasure, a<br />
reducer in front of the nozzle cut-off valve was installed (Matsumoto and Kawahara ).<br />
Swelling <strong>coal</strong>s are sticky and they could stick the surrounding bed particles together<br />
<strong>for</strong>ming agglomerates (Palit and Mandal 1995). There<strong>for</strong>e, it was advised to use <strong>coal</strong>s<br />
with low crucible swelling number (CSN) or non-caking <strong>coal</strong>s.<br />
Bed agglomeration was also encountered in plants that used dry <strong>coal</strong> feed, such as<br />
Tomatoh-Atsuma, instead of slurry feeding system. The temperature of the combustion<br />
domain near the fuel nozzle outlet induced the agglomeration. A low ash fusion<br />
temperature generated agglomeration. The Tomatoh-Atsuma plant selects <strong>coal</strong>s based on<br />
the iron content, <strong>coal</strong>s with an iron content of 7% or more will have low ash melting<br />
point (Kazuhiro 2002). Karita requires their <strong>coal</strong>s to contain less than 7% Fe2O3 and to<br />
have an ash fusion temperature higher than 1200 o C. If <strong>coal</strong>s with low ash fusion<br />
temperature are used, the bed temperature has to be kept below the ash fusion<br />
temperature to prevent agglomeration (Palit and Mandal 1995).<br />
Bed agglomeration is caused by amorphous clay mineral fragments and alkali species<br />
adhering to sorbent and chars surfaces (Steenari, Lindqvist et al. 1998). Inside the<br />
agglomerates, the chars are still burning, causing high temperature and reducing<br />
conditions. Steenari et al. found that reducing conditions in the bed caused sintering<br />
through reaction in the CaS-CaSO4 system and through eutectic melting of silicate-iron<br />
mixtures (Steenari, Lindqvist et al. 1998). An increase in the <strong>coal</strong>’s clay content increased<br />
the viscosity of the paste (Wright, Clark et al. 1991). Less agglomeration was found when<br />
using dolomite instead of limestone as the sorbent. The reason was that dolomite contains<br />
a higher quantity of MgO which raised the ash fusion temperature of the CaO-MgO-<br />
Al2O3 (Marocco and Bauer 1993). Improved bed mixing and fluidization was observed<br />
by using finer dolomite (