Hazardous Waste Disposal with Thermal Oxidation - John Zink ...
Hazardous Waste Disposal with Thermal Oxidation - John Zink ...
Hazardous Waste Disposal with Thermal Oxidation - John Zink ...
Create successful ePaper yourself
Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.
Configuration 1.4 is a T.O. fitted <strong>with</strong> a gas-to-gas exchanger and a heat recovery boiler. The heat<br />
exchanger heats incoming combustion air or waste gases, and the boiler further extracts the heat<br />
available in the flue gas discharged from the exchanger. This configuration offers flexibility in the<br />
amount of steam produced versus fuel usage.<br />
WASTE EXAMPLE PRODUCTS OF OXIDATION<br />
Gas<br />
Liquid<br />
Air<br />
Fuel<br />
T. O.<br />
Tail Gas Organic<br />
Acid<br />
<strong>Waste</strong><br />
H. Exchanger<br />
Configuration 1.4 : <strong>Waste</strong> Process<br />
Steam<br />
FG, NO XA ,SO XA<br />
FG, NO XA<br />
Boiler<br />
Stack<br />
Flue Gas<br />
Configuration 1.5 illustrates a Catalytic Oxidizer fitted <strong>with</strong> a gas-to-gas exchanger. The<br />
heat exchanger preheats contaminated air which is routed to chamber containing catalyst<br />
material. The catalyst causes oxidation of the HC to occur at much lower temperatures than<br />
in a thermal oxidizer, thus greatly reducing the fuel usage. The HC content of the air is<br />
generally limited to less the 0.75 % because of temperature limits of the catalyst.<br />
WASTE EXAMPLE PRODUCTS OF OXIDATION<br />
Gas<br />
Liquid<br />
Fuel<br />
Tail Gas Organic<br />
Acid<br />
Contaminated Air<br />
Catalytic Oxidizer<br />
Configuration 1.5 : <strong>Waste</strong> Process<br />
8<br />
H. Exchanger<br />
FG, NO XA ,SO XA<br />
FG, NO XA<br />
Stack<br />
Flue Gas
Change language