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NOx Emissions from Cement Mfg - US Environmental Protection ...

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to 50 percent of the fuel is burned at a lower (calcination)<br />

temperature which is expected to reduce the thermal <strong>NOx</strong> formation<br />

considerably. The preheater kilns may also use the secondary<br />

firing to a lesser extent. Up to 15 to 20 percent of the fuel<br />

may be fired in the riser duct in preheater designs1 although the<br />

primary emphasis in these designs is on efficient heat recovery<br />

<strong>from</strong> kiln exhaust gases.<br />

The concept of staged combustion may also be used in the<br />

precalciner designs by injecting part of the calciner fuel in the<br />

kiln exhaust gas entering the calciner (secondary combustor).<br />

The tertiary air is added at a later point to complete the<br />

combustion of the calciner fuel. The injection of fuel in the<br />

kiln exhaust gas creates a reducing zone which reduces the <strong>NOx</strong><br />

formed in the kiln combustor by following simplified reactions:<br />

and<br />

NO % C 6 N % CO<br />

NO % CO 6 N % CO 2 .<br />

5-11<br />

(5-1)<br />

(5-2)<br />

As discussed in Section 4.2.2, nitrogen present in the fuel may<br />

also participate in the reduction of <strong>NOx</strong>. The primary <strong>NOx</strong><br />

formation mechanism in the secondary firing is the fuel <strong>NOx</strong><br />

formation which depends upon the nitrogen content of the fuel<br />

used. In order for the above reactions (5-1) and (5-2) to<br />

proceed at reasonable rates the temperature in the reduction zone<br />

should be maintained between 1000 and 1200 EC (1830 to 2190 EF).<br />

These temperatures may lead to coating difficulties, particularly<br />

if the fuel used is coal with high ash content.15 Very promising<br />

results appear to have been obtained recently with the staged

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