Reduction of NOx emissions from a dry process preheater kiln with calciner through the use of the urea based SNCR process

The post combustion reduction of NO_x using urea has proven to be an effective method in controlling NO_x from various combustion sources. Such a reduction process has been successfully demonstrated in a week-long test at Ash Grove´s dry process cement kiln system located in Seattle. This system is equipped with planetary coolers, a 5-stage preheater and an air-through-the-kiln calciner, Testing was done under ten different kiln/calciner operating conditions. Using three to four injectors, NO_x was efficiently reduced from 350-600 pounds per hour lb/ton of clinker to less than 100 pounds per hour. This calculates to a NO_x reduction of greater than 80 percent for most cases. Chemical utilization was greater than 50 percent. A high degree of mixing and a long residence time at an appropriate temperature present in the preheater tower contributed to these excellent results. An average ammonia slip was four ppm above a baseline level at normalized stoichiometric ration of 1. This demonstration confirms expectations that dry process cement kilns with 4+ preheater states are an ideal application for the selective non-catalytic reduction of ν´_x with urea. NO_x was efficiently and effectively reduced with minimal byproduct emissions and virtually no effect on plant operations