Method for preparing fiber cement products based on flue gas desulfurization and denitrification of red mud
A technology for desulfurization, denitrification, and fiber manufacturing, which is applied in the field of fiber cement products. It can solve the problems of low waste utilization rate, difficult industrial production, and complex components, and achieve the effects of ensuring high-efficiency operation, low price, and overcoming high energy consumption.
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Embodiment 1
[0057] According to the formula in Table 1, mix the components uniformly to obtain a flue gas treatment agent, then add alkaline wastewater to make a flue gas desulfurization and denitrification agent slurry, and send it to the desulfurization tower. The flue gas (oxygen content is 18vol%) enters the desulfurization tower from the flue gas inlet of the desulfurization tower, and undergoes three layers of ozone oxidation (ozone comes from the ozone generator, and the ozone concentration of the ozone generator is 10wt%) and flue gas desulfurization and denitrification agent slurry After absorbing the spray layer, sulfur dioxide and nitrogen oxides are fully absorbed by the flue gas desulfurization and denitrification agent slurry. After the flue gas desulfurization and denitrification agent slurry absorbs sulfur dioxide and nitrogen oxides, it is introduced into the slurry circulation tank in the lower part of the desulfurization tower through the action of gravity. The slurry i...
Embodiment 2
[0071] Using the flue gas treatment agent formula in Table 6, the working conditions of flue gas desulfurization and denitrification are shown in Table 7 and Table 8 below. All the other conditions are the same as in Example 1. See Table 9 for the recipe. See Table 10 for performance test results.
[0072] Table 6 Flue gas treatment agent formula
[0073]
[0074] Table 7 Desulfurization and denitrification working condition parameters
[0075] serial number
project
quantity
unit
1
Flue gas volume at the inlet of desulfurization tower (working condition)
1037075
m 3 / h
2
Standard smoke volume
701364
N m 3 / h
3
Desulfurization tower inlet temperature
140
℃
4
SO2 inlet concentration
980
mg / Nm 3
5
NOx inlet concentration
410
mg / Nm 3
6
Inlet soot
100
mg / Nm 3
7
5.3
wt%
[0076] Table 8 Emissions fro...
Embodiment 3
[0083] The formulation of the flue gas treatment agent in Table 11 and the working conditions of flue gas desulfurization and denitrification are shown in Table 12 and Table 13 below. All the other conditions are the same as in Example 1. See Table 14 for the recipe. See Table 15 for performance test results.
[0084] Table 11 Flue gas treatment agent formula
[0085]
[0086] Table 12 Desulfurization and denitrification working condition parameters
[0087] serial number
project
quantity
unit
1
Flue gas volume at the inlet of desulfurization tower (working condition)
1092076
m 3 / h
2
Standard smoke volume
741361
N m 3 / h
3
Desulfurization tower inlet temperature
143
℃
4
SO2 inlet concentration
960
mg / Nm 3
5
NOx inlet concentration
392
mg / Nm 3
6
Inlet soot
113
mg / Nm 3
7
5.8
wt%
[0088] Table 1...
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