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COAL<br />

a final feasibility study into a coal-based chemi<br />

cals complex at Baotou. The project, which<br />

would use coal reserves from Shenmu, Shanxi<br />

Province and Dongsheng, Inner Mongolia, would<br />

have annual capacities for 330,000 metric tonnes<br />

of ammonia, 570,000 metric tonnes of urea,<br />

330,000 metric tonnes of methanol, and<br />

220,000 metric tons of acetic acid and acetic acid<br />

derivatives. It would cost about $1 billion and<br />

come onstream in year 2000.<br />

####<br />

THREE-TON/DAY GASIFIER TEST UNIT<br />

UNDER CONSTRUCTION IN SOUTH KOREA<br />

A 3-ton per day Bench-Scale Unit (BSU) In<br />

tegrated Gasification Combined Cycle (IGCC)<br />

gasifier is under construction in South Korea as<br />

part of a strategy to develop a complete engineer<br />

ing package for IGCC key components. The test<br />

SOURCE: MMETAL.<br />

FIGURE 1<br />

unit was described by H. Kim et al. of Ajou Univer<br />

sity, Suwon, Korea and the Institute for Advanced<br />

Engineering (IAE), Seoul, at the 1 1th Annual Pitts<br />

burgh Coal Conference last fall.<br />

The project is sponsored by the Korea Govern<br />

ment through a grant to the Energy System<br />

Research Center of Ajou University, with the par<br />

ticipation of IAE, Daewoo Corporation, DSHM<br />

(Daewoo Shipbuilding and Heavy Machinaries)<br />

and United Pacific Technologies.<br />

An oxygen-blown, entrained gasification process<br />

was chosen because of its higher thermal ef<br />

ficiency<br />

and mature demonstration of technol<br />

ogy. A schematic diagram of the IGCC BSU is<br />

shown in Figure 1. Pulverized coal is dried to<br />

less than 5 percent surface moisture for<br />

flowability through the feeding system. Fluxing<br />

agents are required with certain coals to allow<br />

slagging<br />

temperatures and to reduce slag<br />

DIAGRAM OF THE IGCC BENCH SCALE UNIT<br />

PULVERIZED<br />

COAL*<br />

|<br />

?<br />

RAWfcOAL<br />

COAL<br />

FEEDING<br />

SYSTEM<br />

STEAM<br />

J<br />

COIL<br />

PREPARATION<br />

J SYSTEM<br />

0XYCEN<br />

IAE's GASIFIER<br />

GAS COOLER<br />

4-34<br />

SLAG<br />

of the coal ash at reasonable gasifier<br />

CAS TREATMENT<br />

SULFUR<br />

CIZA.N CAS<br />

viscosity. The<br />

THE SYNTHETIC FUELS REPORT, JANUARY 1995

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