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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more than 3 years, since 1977. The performance <strong>of</strong> <strong>the</strong> unit has been s<strong>at</strong>isfactory<br />
to <strong>the</strong> user. Figure 1 shows <strong>the</strong> general arrangement <strong>of</strong> this modified<br />
boiler. Its major parameters are as follows:<br />
Steam capacity 24 t/h 2<br />
Steam pressure<br />
Superhe<strong>at</strong>ed steam<br />
32 kg/cm<br />
temper<strong>at</strong>ure 45OEC<br />
Feed w<strong>at</strong>er temper<strong>at</strong>ure<br />
Gas temper<strong>at</strong>ure <strong>at</strong><br />
150 C<br />
boiler exit 20o0c<br />
Designed fuel Bituminous <strong>coal</strong><br />
N<strong>at</strong>ural circul<strong>at</strong>ion was adopted for <strong>the</strong> immersed evapor<strong>at</strong>ing surface. To<br />
d<strong>at</strong>e no problem in w<strong>at</strong>er circul<strong>at</strong>ion has occurred. An experimental immersed<br />
superhe<strong>at</strong>er was placed in <strong>the</strong> bed and its behavior observed. For distribution<br />
<strong>of</strong> combustion air, a refractory covered bubble cap pl<strong>at</strong>e was installed.<br />
In order to facilit<strong>at</strong>e bed start-up and load changes, <strong>the</strong> windbox was divided<br />
into four separ<strong>at</strong>e compartments. Because bituminous <strong>coal</strong> was to be used, no<br />
carbon recycling was considered; thus <strong>the</strong> uncertainty <strong>of</strong> a recycle system was<br />
avoided. The once-through combustion efficiency (i.e.,<br />
elutri<strong>at</strong>ed fines) was measured as 94.8 to 95.5 percent.<br />
without reburning <strong>of</strong><br />
TEST RESULTS AND DISCUSSION<br />
A- Combustion Efficiency<br />
When compared with pulverized <strong>coal</strong> firing, carbon losses from a fluid-<br />
ized bed are high as a result <strong>of</strong> <strong>the</strong> rel<strong>at</strong>ively coarse <strong>coal</strong> particul<strong>at</strong>es<br />
and low combustion temper<strong>at</strong>ure. Combustion efficiency depends on <strong>the</strong><br />
bed velocity and temper<strong>at</strong>ure, excess air, and on <strong>the</strong> <strong>coal</strong> character-<br />
istics (which have significant influence on carbon losses). Coal with<br />
high ash content and less vol<strong>at</strong>ile m<strong>at</strong>ter would have lower combustion<br />
efficiency. The following experimental d<strong>at</strong>a from <strong>the</strong> test rig demon-<br />
str<strong>at</strong>e th<strong>at</strong> c.e. values in burning different <strong>coal</strong>s may differ gre<strong>at</strong>ly,<br />
even when <strong>the</strong> superficial ve$ocity, bed temper<strong>at</strong>ure, and excess air r<strong>at</strong>e<br />
are approxim<strong>at</strong>ely <strong>the</strong> same.<br />
Vol<strong>at</strong>ile m<strong>at</strong>ters Ash<br />
on combustible on analytical Total<br />
basis basis carbon losses<br />
Bituminous <strong>coal</strong> 35.48 31.40 3.77<br />
Lean <strong>coal</strong> 17.50 39.04 10.67<br />
Colliery wastage 48.09 76.50 7.95<br />
If anthracite is burned, carbon losses will be higher than <strong>the</strong> above<br />
values. It is evident th<strong>at</strong> applic<strong>at</strong>ion <strong>of</strong> FBC in utility boilers will<br />
require significantly increased combustion efficiencies.<br />
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