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Mathematical Modelling of Dynamics of Boiler (锅炉动态数学模型)
11
Mathematical Modelling of Dynamics of
Boiler Surfaces Heated Convectively
Wiesław Zima
Cracow University of Technology
Poland
1. Introduction
In order to increase the efficiency of electrical power production, steam parameters, namely
pressure and temperature, are increased. Changes in the superheated steam and feed water
temperatures in boiler operation are also caused by changes in the heat transfer conditions
on the combustion gases side. When the waterwalls of the furnace chamber undergo
slagging up, the combustion gases temperature at the furnace chamber outlet increases, and
the superheaters and economizers take more heat. In order to maintain the same
temperature of the superheated steam at the outlet, the flow of injected water must be
increased. Upon cleaning the superheater using ash blowers, the heat flux taken by the
superheater also increases, which in turn changes the coolant mass flow. Changes of the
superheated steam and feed water temperatures caused by switching off some burners or
coal pulverizers or by varying the net calorific value of the supplied coal may also be
significant. Precise modelling of superheater dynamics to improve the quality of control of
the superheated steam temperature is therefore essential. Designing the mathematical
model describing superheater dynamics is also very important from
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