the coking properties of coal at elevated pressures. - Argonne ...
the coking properties of coal at elevated pressures. - Argonne ...
the coking properties of coal at elevated pressures. - Argonne ...
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3. Bed m<strong>at</strong>erial composition (high calcium content tends to delay, and decrease<br />
<strong>the</strong> severity <strong>of</strong> agglomer<strong>at</strong>es formed)<br />
4. Ash recycle (increased<br />
tendency)<br />
recycle <strong>of</strong> ash tends to increase agglomer<strong>at</strong>ion<br />
5. There appears to be a bed design parameter such as position <strong>of</strong> <strong>coal</strong> feed<br />
points, and distributor pl<strong>at</strong>e performance which affect bed m<strong>at</strong>erial agglomer<strong>at</strong>ion.<br />
The bed m<strong>at</strong>erial used in baseline run 2181 was 10 mesh quartz sand. Upon<br />
startup <strong>the</strong> bed was sampled every eight hours for <strong>the</strong> dur<strong>at</strong>ion <strong>of</strong> <strong>the</strong> 69 hour run.<br />
At <strong>the</strong> end <strong>of</strong> <strong>the</strong> run <strong>the</strong> system was cooled and opened to expose <strong>the</strong> inside <strong>of</strong> <strong>the</strong><br />
combustor. The bed m<strong>at</strong>erial was removed and several agglomer<strong>at</strong>es were found,<br />
which varied in size and shape, with <strong>the</strong> largest having a diameter <strong>of</strong> 6 cm. These<br />
agglomer<strong>at</strong>es were found both free flo<strong>at</strong>ing in <strong>the</strong> bed and <strong>at</strong>tached to <strong>the</strong> inside<br />
wall <strong>of</strong> <strong>the</strong> combustor.<br />
The limestone bed m<strong>at</strong>erial was tested in run 2281 using 100% ash reinjection<br />
for a dur<strong>at</strong>ion <strong>of</strong> 73 hours. The bed was sampled in <strong>the</strong> same manner as 2181.<br />
The form<strong>at</strong>ion <strong>of</strong> agglomer<strong>at</strong>es in <strong>the</strong> run was very minimal with no major agglomer-<br />
<strong>at</strong>es found. On <strong>the</strong> o<strong>the</strong>r hand, run 2481 which used a limestone bed ran for 160<br />
hours with 100% ash reinjection and had severe problems with agglomer<strong>at</strong>ion. After<br />
<strong>the</strong> run numerous agglomer<strong>at</strong>es were found loose in <strong>the</strong> bed. In addition, a large<br />
agglomer<strong>at</strong>e was found on top <strong>of</strong> <strong>the</strong> distributor pl<strong>at</strong>e <strong>at</strong> <strong>the</strong> bottom <strong>of</strong> <strong>the</strong> combus-<br />
tor. The agglomer<strong>at</strong>e had dimensions <strong>of</strong> 30.5 cm X 30.5 cm X 12.5 cm; it weighed<br />
10 kg and covered 30% <strong>of</strong> <strong>the</strong> distributor pl<strong>at</strong>e.<br />
The bed m<strong>at</strong>erial and agglomer<strong>at</strong>es were characterized by polished thin section<br />
study, polarized light microscopy, and scanning electron microscopy/microprobe<br />
(SEM) - both secondary electron (SEI) and backsc<strong>at</strong>ter electron (BEl) images were<br />
used. Bulk samples were analyzed by x-ray diffraction and x-ray fluorescence.<br />
The goals in characterizing <strong>the</strong> bed m<strong>at</strong>erial and agglomer<strong>at</strong>es are to identify <strong>the</strong><br />
stages which lead to agglomer<strong>at</strong>ion and possibly postul<strong>at</strong>e a mechanism <strong>of</strong> <strong>the</strong>ir forma-<br />
tion to <strong>the</strong>reby determine methods and procedures to control <strong>the</strong>ir growth.<br />
Quartz Bed Agglomer<strong>at</strong>es<br />
RESULTS AND DISCUSSION<br />
Agglomer<strong>at</strong>ion <strong>of</strong> quartz bed m<strong>at</strong>erial is typified by run 2181 utilizing high-Na<br />
Beulah lignite and ash injection. Samples <strong>of</strong> bed m<strong>at</strong>erial taken <strong>at</strong> various intervals<br />
during <strong>the</strong> run are illustr<strong>at</strong>ed in Figures 1 to 11 with chemical analyses d<strong>at</strong>a given<br />
in Table 3. The following four stages can be used to summarize <strong>the</strong> agglomer<strong>at</strong>ion<br />
process :<br />
Stage 1. Initial ash co<strong>at</strong>ing.<br />
Initial samples <strong>of</strong> bed m<strong>at</strong>erial have a fine co<strong>at</strong>ing, about 50 microns thick,<br />
consisting <strong>of</strong> sulf<strong>at</strong>ed aluminosilic<strong>at</strong>e particles (Figure 1). The co<strong>at</strong>ings contain some<br />
coarser ash m<strong>at</strong>erials in <strong>the</strong> outer parts and <strong>the</strong> inner parts have penetr<strong>at</strong>ed <strong>the</strong><br />
quartz grains slightly along gently curved or cusp<strong>at</strong>e embayments. The quartz<br />
grains are extensively fractured, apparently as a result <strong>of</strong> <strong>the</strong>rmal stresses.<br />
Stage 2. Thickened nodular co<strong>at</strong>ings.<br />
Longer bed usage results in <strong>the</strong> development <strong>of</strong> thicker ash co<strong>at</strong>ings about<br />
100 - 300 microns thick with nodular outer surfaces resulting from incorpor<strong>at</strong>ion <strong>of</strong><br />
larger ash particles (Figure 2). Sulf<strong>at</strong>ing, shown by lighter colored areas in <strong>the</strong><br />
SEM photographs, is common within both <strong>the</strong> finer and coarser ash particles <strong>of</strong> <strong>the</strong><br />
co<strong>at</strong>ing.<br />
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