Method and apparatus for injecting air into long cement kilns
AssigneesCadence Environmental Energy, Inc., Ash Grove Cement Company
InventorsJames R. Tutt, Eric R. Hansen, Michael P. Heap
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AssigneesCadence Environmental Energy, Inc., Ash Grove Cement Company
InventorsJames R. Tutt, Eric R. Hansen, Michael P. Heap
Estimating the term…
A method and improved apparatus is disclosed for improving combustion efficiency and reducing emission of gaseous pollutants during the manufacture of cement in conventional long rotary kilns. Air is injected through a port in the wall of a rotary cement kiln having a secondary burning zone established by burning solid fuel in contact with the in process mineral at a point downstream, relative to kiln gas flow of the clinkering zone in the kiln. The air injection apparatus is designed to enhance mixing of the injected air with the kiln gas stream and is characterized by high linear flow rates and/or multi-directional air injection ports. The air injection ports can be located downstream of a secondary burning zone to provide staged combustion with concomitant reduction in concentration of NO.sub.x, CO and hydrocarbons in the kiln gas stream.
A method for reducing the concentration of nitrogen oxides in the effluent gas emissions during operation of a conventional long rotary cement kiln comprising a rotary vessel having an upper kiln gas exit end with an adjacent mineral drying zone, and opposite fired clinker exit end with an adjacent clinkering zone and an intermediate mineral calcining zone wherein during operation a kiln gas stream flows from said clinkering zone through the calcining zone and out the kiln gas exit end of the rotary vessel and wherein in-process mineral flows from the drying zone through the clinkering zone, said method comprising the steps of:
A method for reducing the concentration of nitrogen oxides in effluent gas emissions during operation of a conventional long rotary cement kiln comprising a rotary vessel having an upper kiln gas exit end with an adjacent mineral drying zone, and opposite fired clinker exit end with an adjacent clinkering zone and an intermediate mineral calcining zone wherein during operation a kiln gas stream flows from said clinkering zone through the calcining zone and out the kiln gas exit end of the rotary vessel and wherein in-process mineral flows from the drying zone through the clinkering zone, said method comprising the steps of:
Dependencies are inferred from the claim text.