Method for manufacturing lightweight concrete product through flue gas desulfurization and denitrification based on red mud
A lightweight concrete, desulfurization and denitrification technology, applied in separation methods, air quality improvement, chemical instruments and methods, etc., can solve problems such as environmental pollution, complex components, ecological damage, etc., and achieve the effect of ensuring high-efficiency operation
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Embodiment 1
[0060] According to the formula in Table 1, mix the components uniformly to obtain the desulfurization and denitrification agent, then add alkaline waste water to make the 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 ozone oxidation (ozone comes from an ozone generator, and the ozone concentration of the ozone generator is 10wt%) and desulfurization and denitration agent slurry three-layer absorption spray After leaching, sulfur dioxide and nitrogen oxides are fully absorbed by the desulfurization and denitrification agent slurry. After the 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 by gravity. The slurry in the upper part of the slurry circulation...
Embodiment 2
[0073] Using the desulfurization and denitrification 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.
[0074] Table 6 Formula of desulfurization and denitrification agent
[0075]
[0076] Table 7 Desulfurization and denitrification working condition parameters
[0077] serial number
project
quantity
unit
1
Flue gas volume at the inlet of desulfurization tower (working condition)
1035070
m 3 / h
2
Standard smoke volume
701064
N m 3 / h
3
Desulfurization tower inlet temperature
140
℃
4
SO2 inlet concentration
985
mg / Nm 3
5
NOx inlet concentration
415
mg / Nm 3
6
Inlet soot
100
mg / Nm 3
7
5.3
wt...
Embodiment 3
[0085] Table 12 and Table 13 show the formula of desulfurization and denitrification agent used in Table 11, and the working conditions of flue gas desulfurization and denitrification. All the other conditions are the same as in Example 1. See Table 14 for the recipe. See Table 15 for performance test results.
[0086] Table 11 Formula of desulfurization and denitrification agent
[0087]
[0088] Table 12 Desulfurization and denitrification working condition parameters
[0089] serial number
project
quantity
unit
1
Flue gas volume at the inlet of desulfurization tower (working condition)
1094076
m 3 / h
2
Standard smoke volume
741561
N m 3 / h
3
Desulfurization tower inlet temperature
149
℃
4
SO2 inlet concentration
968
mg / Nm 3
5
NOx inlet concentration
401
mg / Nm 3
6
Inlet soot
110
mg / Nm 3
7
5.8
wt% ...
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