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the coking properties of coal at elevated pressures. - Argonne ...

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-6-<br />

abrasion r<strong>at</strong>e <strong>at</strong> <strong>the</strong> bottom <strong>of</strong> <strong>the</strong> tube is three times as high as th<strong>at</strong><br />

<strong>at</strong> <strong>the</strong> top. Several types <strong>of</strong> antiabrasive tre<strong>at</strong>ments for immersed tubes<br />

were tried, and some <strong>of</strong> <strong>the</strong>m have showed effect. However, when<br />

rel<strong>at</strong>ively hard <strong>coal</strong>s are burned <strong>the</strong>se measures can only extend tube<br />

life to a certain degree, <strong>the</strong>refore <strong>the</strong> abrasion problem cannot be<br />

regarded as solved. Lignite-fired, fluidized-bed boilers may be <strong>the</strong><br />

Only exception. The erosion r<strong>at</strong>e <strong>of</strong> <strong>the</strong>ir immersed tubes is not high,<br />

owing to <strong>the</strong> s<strong>of</strong>tness and light weight <strong>of</strong> <strong>the</strong> lignite.<br />

It seems to us th<strong>at</strong> low fluidizing velocity should be accepted as <strong>the</strong><br />

primary measure for extending <strong>the</strong> life <strong>of</strong> immersed tubes, with<br />

additional antiabrasive tre<strong>at</strong>ment when necessary. This may be <strong>the</strong> final<br />

solution to <strong>the</strong> erosion problem. Besides <strong>the</strong> diminished tube abrasion,<br />

low fluidizing velocity may <strong>of</strong>fer o<strong>the</strong>r benefits such as higher<br />

combustion efficiency, better SO2 absorption (when limestone or dolomite<br />

is added to beds where high-sulfur <strong>coal</strong> is burned), and <strong>the</strong> possibility<br />

<strong>of</strong> using shallow beds to reduce <strong>the</strong> amount <strong>of</strong> blower power required. In<br />

order to lessen <strong>the</strong> abrasion r<strong>at</strong>e, <strong>the</strong> immersed tubes should be<br />

reasonably arranged to avoid excessive puls<strong>at</strong>ions and gas flow<br />

imbalances in <strong>the</strong> bed.<br />

E. Start-up <strong>of</strong> Fluidized Bed<br />

The process <strong>of</strong> start-up is, in essence, to he<strong>at</strong> <strong>the</strong> bed m<strong>at</strong>erial to a<br />

temper<strong>at</strong>ure high enough for stable combustion <strong>of</strong> <strong>coal</strong>. It seems very<br />

simple, but when boiler service is initi<strong>at</strong>ed oper<strong>at</strong>ors <strong>of</strong>ten run into<br />

trouble.<br />

"Fixed st<strong>at</strong>e" start-up is a method adopted in <strong>the</strong> initial period <strong>of</strong> FBB<br />

development in China. In this process, <strong>the</strong> bed remains fixed <strong>at</strong> <strong>the</strong><br />

beginning <strong>of</strong> start-up. When <strong>the</strong> bed m<strong>at</strong>erial has been he<strong>at</strong>ed to <strong>the</strong><br />

appropri<strong>at</strong>e degree, <strong>the</strong> bed is tranformed from a fixed to a fluidized<br />

st<strong>at</strong>e and continues to be he<strong>at</strong>ed to <strong>the</strong> required temper<strong>at</strong>ure. During<br />

<strong>the</strong> start-up process, clinkering or flame failure may easily take place<br />

if <strong>the</strong> he<strong>at</strong> balance is not properly controlled. Exploit<strong>at</strong>ion depends to<br />

a gre<strong>at</strong> extent on <strong>the</strong> oper<strong>at</strong>or's experience, so it is not completely<br />

reliable. Fur<strong>the</strong>rmore, <strong>the</strong> time required for starting up is ra<strong>the</strong>r<br />

long.<br />

Through <strong>the</strong> search for a better method, <strong>the</strong> so called "fluidized st<strong>at</strong>e"<br />

start-up technology has been developed. The major fe<strong>at</strong>ure <strong>of</strong> this<br />

process is th<strong>at</strong> <strong>the</strong> bed is brought to fluidiz<strong>at</strong>ion <strong>at</strong> <strong>the</strong> very beginning<br />

<strong>of</strong> start-up. The fluidized bed is he<strong>at</strong>ed up by an oil burner; <strong>the</strong><br />

he<strong>at</strong>ing is uniform and steady. In 10-20 minutes, 8 bed Bith an area <strong>of</strong><br />

4 mz can be he<strong>at</strong>ed from ambient temper<strong>at</strong>ure to 900 -1000 C. It is much<br />

quicker than <strong>the</strong> "fixed st<strong>at</strong>e" method, and oil consumption can thus be<br />

reduced. Figure 5 shows a typical bed start-up curve in which <strong>the</strong><br />

"fluidized st<strong>at</strong>e" method was used.<br />

CONCLUSION<br />

The main reason for developing fluidized-bed boilers in China is to burn<br />

high-ash <strong>coal</strong> <strong>of</strong> low calorific value, and thus broaden <strong>the</strong> scope <strong>of</strong> energy<br />

resources. This appears to be especially important in <strong>the</strong> sou<strong>the</strong>rn pro-<br />

201

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