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Hazardous Waste Disposal with Thermal Oxidation - John Zink ...

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<strong>Waste</strong> Containing Combustible Fine Solids -<br />

Acceptable Levels of NOx and/or SOx<br />

The following two block diagrams show configurations of a process to dispose of a waste-containing<br />

combustible fine solids (less than 500 microns particle size), which produces flue gas containing<br />

acceptable amounts of SOx and/or NOx.<br />

Configuration 6.1 consists of a cyclonic T.O. in which a high radial gas velocity causes the denser<br />

solid particles to be preferentially “slung” to the wall, thus markedly increasing their retention time.<br />

WASTE EXAMPLE PRODUCTS OF OXIDATION<br />

GAS / SOLID CO + H 2/C FG, NO XA<br />

AIR<br />

FUEL<br />

HOPPER<br />

Configuration 6.1 : <strong>Waste</strong> Process<br />

CYCLONIC T.O.<br />

Configuration 6.2 shows a cyclonic T.O. fitted <strong>with</strong> a heat recovery boiler which produces steam<br />

to lower the flue gas temperature to 350° F.<br />

17<br />

STACK<br />

FLUE GAS<br />

WASTE EXAMPLE PRODUCTS OF OXIDATION<br />

GAS / SOLID<br />

CO + H2/C FG, NOXA AIR<br />

FUEL<br />

HOPPER<br />

CYCLONIC T.O.<br />

Configuration 6.2 : <strong>Waste</strong> Process<br />

STEAM<br />

BOILER<br />

STACK<br />

FLUE GAS

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