Aiming to reduce consumption amount of ammonia (NH
3), which is blown into the catalytic denitrification process of the refuse incinerator plant, application of the periodic control method has been studied.
Through a step response examination in an actual plant, remarkable process dynamic characteristics have been observed: namely, that time-constant (T
u) of blowing in NH
3 is smaller than (T
d) of blowing off.
Applying the optimal periodic control theory to the process, the following analytical results are obtained: (i) Optimal bang-bang type periodic control of NH
3 blowing is more effective in reducing NH
3 consumption than optimal continuous steady state control, and (ii) The NH
3 consumption reduction rate depends on the
Td/Tu ratio and the ζ parameter (ζ=aimed denitrification rate/process capable denitrification rate)
Because the theoretical solution of the optimal control period is approximately zero, a practical finite periodic control has been examined on an actual catalytic denitrification process. Results of the examination have shown that the NH
3 reduction level is acceptable but lower than the theoretical value.
In actual plants, because of wide fluctuation of nitrogenoxide (NO
x) generation, simple periodic control cannot maintain exhaust NO
x concentration under the required NO
x concentration for a long time. The periodic control with feedback correction of control timing has been proposed and demonstrated to be effective by simulation.
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