Method and device for removing SO2 in smoke gas by pyrolusite slurry and resource utilization
A technology of resource utilization and pyrolusite, applied in chemical instruments and methods, separation methods, manganese sulfate, etc., can solve the problems of large investment and energy consumption, loss of ammonia volatilization, high cost, etc., and achieve low operating costs and good economic benefits Effect
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[0026] Example 1
[0027] Such as Figure one As shown, a manganese ore slurry removes SO in flue gas 2 And its resource utilization equipment, including pressurized blower 1, desulfurization tower 2, demister 3, slurry pump I4, circulating pump 5, slurry tank 6, desulfurization slurry storage tank 7, slurry pump II8, vacuum filter I9 , Receiving tank I10, vacuum pump I11, purification tank 12, screw pump 13, filter press 14, neutralization tank 15, clarification sedimentation tank 16, slurry pump III17, vacuum filter II18, receiving tank II19, vacuum pump II20, vacuum evaporator 21. Centrifuge I22, clear liquid pump 23, carbonization tank 24, centrifuge II25, mother liquor tank 26, ammonia pump 27, ammonia distillation tower 28, separator 29, dryer I30, dryer II31; pressurized blower 1 and The lower part of the desulfurization tower 2 is connected, the bottom of the desulfurization tower 2 is equipped with a material box, and the upper part is equipped with a spray device. The ...
Example Embodiment
[0035] Example 2
[0036] The manganese ore slurry in this example removes SO from flue gas 2 And the method of resource utilization, the device adopted is the same as that of Example 1, except that two rows of spray devices are set, and each row is set with 7 nozzles. The specific steps are as follows:
[0037] (1) Wet grind the pyrolusite with a ball mill, pass a 200-mesh sieve, add water in the slurry tank 6 to make a pyrolusite slurry, the solid content of the pyrolusite slurry is 22%, and the pH of the pyrolusite slurry is adjusted to 4;
[0038] (2) The flue gas is the flue gas of the power plant boiler, and the flue gas volume is 100,000Nm 3 / h, SO in flue gas 2 The content is 2000mg / Nm 3 , The average temperature is 120℃, and the flue gas SO is required 2 Less than 400mg / Nm 3 The flue gas with higher temperature first enters the waste heat exchanger to produce low-pressure steam for the evaporation process. After cooling, the flue gas enters from the lower part of the desulfur...
Example Embodiment
[0043] Example 3
[0044] The manganese ore slurry in this example removes SO from flue gas 2 Its resource utilization method uses the same device as that of Embodiment 1. The specific steps are as follows:
[0045] (1) Wet grind the pyrolusite with a ball mill, pass a 200-mesh sieve, and add water in the slurry tank 6 to make a pyrolusite slurry. The solid content of the pyrolusite slurry is 18%, and the pH of the pyrolusite slurry is adjusted to 4.5;
[0046] (2) The flue gas is the flue gas of the sulfuric acid preparation plant, and the sulfuric acid tail gas treatment capacity is 200,000Nm 3 / h, SO in the tail gas of two-rotation and two-absorption sulfuric acid plant 2 Content 650mg / Nm 3 , Tail gas outlet requirements SO 2 Content 100mg / Nm 3 Below, the desulfurization efficiency is more than 85%, and the flue gas with higher temperature first enters the waste heat exchanger to produce low-pressure steam for use in the evaporation process. After cooling, the flue gas enters from ...
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