Optimizing control system for large-scale pulverized coal furnace
An optimization control, pulverized coal furnace technology, applied in the direction of combustion control, coke oven, special form of dry distillation, etc., can solve the problems of not completely solving the conditions for the composition and solution of boiler combustion balance equations, not being able to guarantee validity, and insufficient measured data.
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Embodiment 1
[0064] According to the scheme of the present invention, the ten conditions adopted in this embodiment are:
[0065] ① The total calorific value of the elements should be equal to the sum of the heat absorption of the boiler and the losses of various items. See formula (12).
[0066] ②The heat balance of the milling system. Calculate M ar .
[0067] ③ The total input of coal is equal to the sum of elements, water and ash. See formula (2).
[0068] ④ Actual measurement of SO in boiler flue gas 2 , the obtained S components in coal and SO in flue gas 2 Components correspond to expressions. See formula (5).
[0069] ⑤ Regression equation or empirical formula of composition among elements (such as H, N). See formula (4).
[0070] ⑥ Regression equation or empirical formula of composition among elements (such as C, O). See (3) type.
[0071] ⑦ Measured O of boiler flue gas 2 Corresponding expressions for the composition of coal are obtained. See formulas (6), (7), (8),...
Embodiment 2
[0148] According to the scheme of the present invention, the ten conditions adopted in this embodiment are:
[0149] ① The total calorific value of the elements should be equal to the sum of the heat absorption of the boiler and the losses of various items. See formula (12).
[0150] ②The heat balance of the milling system. Calculate M ar .
[0151] ③ The total input of coal is equal to the sum of elements, water and ash. See formula (2).
[0152] ④ Actual measurement of SO in boiler flue gas 2 , the obtained S components in coal and SO in flue gas 2 Components correspond to expressions. See formula (5).
[0153] ⑤ Regression equation or empirical formula of composition among elements (such as H, N). See formula (4).
[0154] ⑥ Regression equation or empirical formula of composition among elements (such as C, H). See the formula below.
[0155] h ar =A 3 C ar +B 3 , for anthracite A 3 =-0.448, B 3 = 44.73.
[0156] ⑦ Measured O of boiler flue gas 2 Correspo...
Embodiment 3
[0166] According to the scheme of the present invention, the ten conditions adopted in this embodiment are:
[0167] ① The total calorific value of the elements should be equal to the sum of the heat absorption of the boiler and the losses of various items. See formula (12).
[0168] ②The heat balance of the milling system. Calculate M ar .
[0169] ③ The total input of coal is equal to the sum of elements, water and ash. See formula (2).
[0170] ④ Actual measurement of SO in boiler flue gas 2 , the obtained S components in coal and SO in flue gas 2 Components correspond to expressions. See formula (5).
[0171] ⑤ Regression equation or empirical formula of composition among elements (such as H, N). See formula (4).
[0172] ⑥ Regression equation or empirical formula of composition among elements (such as C, O). See (3) type.
[0173] ⑦ Measured O of boiler flue gas 2 Corresponding expressions for the composition of coal are obtained. See formulas (6), (7), (8),...
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