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

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6.2.2.2 Selective Catalytic Reduction. Although no<br />

selective catalytic reduction (SCR) systems are currently being<br />

used on cement plants in the United States, this control<br />

technique has been applied successfully in other industries.<br />

Capital costs for this control approach would include cost of the<br />

SCR unit, ammonia storage tank, and an ammonia heating/<br />

vaporization injection system along with equipment needed for<br />

preheating flue gases to an appropriate temperature. Operating<br />

costs would include the cost of ammonia reagent, dilution steam,<br />

catalyst replacement and disposal costs, and energy cost<br />

associated with reheating the kiln exhaust gases as well as the<br />

operating labor and maintenance costs.<br />

Since the SCR technology has not been proven in cement<br />

plants in the United States, approximate capital and operating<br />

costs as applicable to the model plants were not available <strong>from</strong><br />

any of the SCR control system vendors in the United States. An<br />

equipment cost estimate of an SCR system was submitted by a<br />

Japanese supplier to a cement company in the United States in<br />

1991.19 For a dry long kiln with 1,120 tons/day (47 tons/hr)<br />

clinker capacity, the estimated equipment cost was 1 billion/Yen.<br />

With a current exchange rate of 108 Yen/$ and assuming 5 percent<br />

inflation, the estimated cost in 1992 U.S. dollars was about 9.72<br />

6-45

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