A kind of flue gas desulfurization and denitrification process method
A desulfurization and denitration technology, which is applied in the field of boiler flue gas and refinery FCC flue gas desulfurization and denitrification technology, can solve the problems of unutilized NOx, substandard exhaust particulate matter, excessive ammonia, etc. The effect of improving quality and quantity, and large denitration load
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Embodiment 1
[0030] The flue gas of a coal-fired boiler has a SOx content of 2050mg / m 3 , NOx content is 1650mg / m 3 .
[0031] By adopting the method of the present invention, the flue gas is washed with water at first, and a packed tower is adopted, and the liquid-gas volume ratio of spraying is 5L / M 3 .
[0032] The washed flue gas enters the desulfurization tower from the bottom. The desulfurization tower adopts a packed tower. The desulfurization tower is divided into two parts, the upper part and the lower part. The liquid phase material and the introduced spray liquid, the introduced spray liquid is a mixture of circulating desulfurization liquid and ammonia water with a mass concentration of 4%, and the pH value of the mixture is 6.4. The volume ratio of the upper and lower fillers is generally 1:4. The upper liquid-gas volume ratio is 5L / M 3 , the lower liquid-gas volume ratio is 8L / M 3 . The total volumetric space velocity of the flue gas passing through the desulfurization...
Embodiment 2
[0036] The flue gas of a coal-fired boiler has a SOx content of 1800mg / m 3 , NOx content is 840mg / m 3 .
[0037] Adopt the method of the present invention, flue gas is washed with water at first, adopt packed tower, the liquid-gas volume ratio of spraying is 4L / M 3 .
[0038] The washed flue gas enters the desulfurization tower from the bottom. The desulfurization tower adopts a packed tower. The desulfurization tower is divided into two parts, the upper part and the lower part. The liquid phase material and the introduced spray liquid, the introduced spray liquid is a mixed material of circulating desulfurization liquid and ammonia water with a mass concentration of 5%, and the pH value of the mixed material is 6.8. The volume ratio of the upper and lower fillers is generally 1:5. The upper liquid-gas volume ratio is 4L / M 3 , the liquid-gas volume ratio of the lower part is 6L / M 3 . The total volume space velocity of the flue gas passing through the desulfurization tow...
Embodiment 3
[0042] A catalytic cracking regeneration flue gas, SOx content is 1250mg / m 3 , NOx content is 1050mg / m 3 .
[0043] Adopt the method of the present invention, flue gas is washed with water at first, adopt packed tower, the liquid-gas volume ratio of spraying is 10L / M 3 .
[0044] The washed flue gas enters the desulfurization tower from the bottom. The desulfurization tower adopts a packed tower. The desulfurization tower is divided into two parts, the upper part and the lower part. The liquid phase material and the introduced spray liquid, the introduced spray liquid is a mixture of circulating desulfurization liquid and ammonia water with a mass concentration of 6%, and the pH value of the mixture is 6.8. The volume ratio of the upper and lower fillers is generally 1:6. The liquid-gas volume ratio of the upper part is 8L / M 3 , the lower liquid-gas volume ratio is generally 15L / M 3 . The total volume space velocity of the flue gas passing through the desulfurization to...
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