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

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of <strong>NOx</strong> emissions in a cement kiln. The information obtained<br />

during this study indicated that some plants indeed relied on<br />

process monitoring and control as a means to maintain <strong>NOx</strong><br />

emissions within their respective permit limits. These plants<br />

also indicated that no additional costs were involved in these<br />

process control measures.5<br />

Based on existing installations, the cost of a commercially<br />

available kiln process control system is in the neighborhood of<br />

$750,000.6 The resulting savings due to reduced energy and fuel<br />

requirements and increased refractory life were estimated to be<br />

about $1.37 per short ton of clinker. Thus, for a cement kiln<br />

facility producing 300,000 tons/year of clinker the reduced cost<br />

of producing cement is expected to recover process control<br />

installation costs in less than 2 years.<br />

6.2.1.2 Process Modifications. As discussed in Sections<br />

5.1.2 and 5.3, process modifications measures can be highly site<br />

specific and data <strong>from</strong> one site cannot be directly translated to<br />

other sites. Data are not available to determine costs of<br />

individual process modifications. Quite often a number of<br />

process modifications and combustion control measures are<br />

implemented simultaneously. Similar to combustion process<br />

control approaches, process modifications have also shown to<br />

reduce energy requirement and increase productivity, thus<br />

providing an economic incentive to implement them in addition to<br />

<strong>NOx</strong> reduction.<br />

6.2.1.3 Low <strong>NOx</strong> Burners. <strong>Cement</strong> kiln burners, specifically<br />

marketed as low <strong>NOx</strong> burners, require an indirect-fired kiln<br />

system. Therefore, to install a low <strong>NOx</strong> burner in an existing<br />

direct-fired kiln, it is necessary to convert the kiln-firing<br />

system to an indirect-firing one. Two sets of costs are<br />

therefore developed: (1) to install a low <strong>NOx</strong> burner in an<br />

existing indirect-fired kiln, and (2) to install a low <strong>NOx</strong> burner<br />

in an existing direct-fired kiln. In the first case, only the<br />

costs of the low <strong>NOx</strong> burner equipment are considered, whereas in<br />

the second case the costs of conversion of a direct-fired system<br />

to an indirect-fired system are added to the low <strong>NOx</strong> burner cost.<br />

6-15

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