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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

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