Ikelic - Alliance Digital Repository
Ikelic - Alliance Digital Repository
Ikelic - Alliance Digital Repository
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COAL<br />
Process Description<br />
In the HYCOL process, powdered coal is<br />
pneumatically conveyed using nitrogen, and intro<br />
duced with oxygen into the gasifier through two<br />
stages of tangential multi-burners; four burners<br />
arranged in each stage. The gasifier, operating<br />
at 3 MPa and up to 1,800C, converts the coal to<br />
a synthesis gas. Most of the ash in the coal<br />
melts and circulates down along the wall of the<br />
gasifier as molten slag, and eventually exits the<br />
gasifier mainly through the outer slag tap holes in<br />
the bottom. The slag is quenched, solidified in a<br />
water bath, and crushed by the slag crusher,<br />
then removed via lockhoppers. When the hot<br />
gas exits the gasifier, recycle cooled gas and<br />
steam are mixed to quench the gas so that the<br />
solids in the hot gas are no longer sticky<br />
(Figure 2).<br />
The solids in the synthesis gas, termed recycle<br />
char, are removed from the gas in double hot<br />
Heat Recovery<br />
Zone<br />
FIGURE 2<br />
cyclones. The recovered char, at about 300C, is<br />
circulated to the gasifier via lockhoppers and a<br />
pneumatic conveying system. This achieves<br />
higher carbon conversion and allows a greater<br />
recovery<br />
of the coal ash as slag.<br />
Technological Features<br />
To achieve high gasification efficiency and ap<br />
plicability to a wide range of coals, the HYCOL<br />
gasifier has the following features:<br />
- The<br />
oxygen-blown one-chamber with<br />
two-step<br />
HYCOL PLANT CONFIGURATION<br />
.Water.<br />
(Quench)<br />
Radiant"<br />
Boiler<br />
f CoaVOxygen<br />
Gasification (Upper Burners)<br />
Zone<br />
CoaVOxygen<br />
4 (Lower Burners)<br />
Slag Quenching<br />
Zone<br />
HYCOL Reactor<br />
SOURCE: MATSUOKA ET AL.<br />
<<br />
O<br />
Oil Burner V Crusher<br />
spiral flow concept lengthens<br />
the residence time of coal particles in the<br />
gasification zone, and thus enables a<br />
higher gasification efficiency with com<br />
pact reactor size. In addition, a wide<br />
range of split ratios of coal and oxygen<br />
fed to upper and lower burners can be<br />
chosen independently to obtain optimum<br />
gasification efficiency with a wide<br />
Recycte (Quench)<br />
Hot CyctoneJ nel i Convectj<br />
1 r> Boiler<br />
g &<br />
Y<br />
on Shifter<br />
Steam<br />
(Quench)<br />
' Char/Oxygen/Steam<br />
(Char Burner)<br />
Slag<br />
4-36<br />
r\<br />
E<br />
Cooled Gas<br />
Scrubber<br />
| Wash Water<br />
THE SYNTHETIC FUELS REPORT, JANUARY 1995