A method of using low-grade alkali-containing brine for flue gas desulfurization-oxidation nitrate production
A low-grade, alkaline brine technology, applied in the field of nitrate-making process, can solve the problems of low-grade nitrate-making raw materials and the inability to fully utilize low-grade alkali-containing brine, so as to achieve reduced energy consumption, high application value and environmental benefits, and reduced production cost effect
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Embodiment 1
[0031] a. The alkali-containing brine is pumped from the bottom of the desulfurization tower by the slurry transfer pump into the upper part of the desulfurization tower, and is distributed by spraying. When it falls to the bottom of the desulfurization tower, the slurry transfer pump is pumped from the bottom of the desulfurization tower into the spray system at the top of the desulfurization tower. Circulation, the flow of alkali-containing brine is 100m 3 / h, pH value is controlled to 7.5;
[0032] b. The boiler flue gas is blown in from the bottom of the desulfurization tower by a fan, flows countercurrently with the alkaline water containing halogen, and contacts desulfurization. The flue gas flow rate is 180,000m 3 / h, the liquid-gas ratio of the alkali-containing brine entering the desulfurization tower and boiler flue gas is 1:1.8 L / m 3 , The flue gas after desulfurization is discharged from the top outlet of the desulfurization tower, and through online detection, SO in th...
Embodiment 2
[0039] a. The alkali-containing brine is pumped from the bottom of the desulfurization tower by the slurry transfer pump into the upper part of the desulfurization tower, and is distributed by spraying. The flow rate of the alkali-containing brine is 200m 3 / h, pH value is controlled to 6.5;
[0040] b. The boiler flue gas is blown in from the bottom of the desulfurization tower by a fan, flows countercurrently with the alkali water containing halogen, and contacts desulfurization. The flue gas flow rate is 220,000m 3 / h, the liquid-gas ratio of the alkali-containing brine entering the desulfurization tower and boiler flue gas is 1:1.1 L / m 3 , The flue gas after desulfurization is discharged from the top outlet of the desulfurization tower, and through online detection, SO in the flue gas after desulfurization 2 The concentration is 200mg / Nm 3 , Comply with emission standards
[0041] c. It is used in the deoxidation reactor of alkali-containing brine after flue gas desulfurization, ...
Embodiment 3
[0047] a. The alkali-containing brine is pumped from the bottom of the desulfurization tower by the slurry transfer pump into the upper part of the desulfurization tower, and is distributed by spraying. When it falls to the bottom of the desulfurization tower, the slurry transfer pump is pumped from the bottom of the desulfurization tower into the spray system at the top of the desulfurization tower. Circulation, the flow rate of alkaline brine is 150m 3 / h, pH value is controlled to 7;
[0048] b. The boiler flue gas is blown in from the bottom of the desulfurization tower by a fan, flows countercurrently with the alkali water containing halogen, and contacts desulfurization. The flue gas flow rate is 135000m 3 / h, the liquid-gas ratio of the alkali-containing brine entering the desulfurization tower and boiler flue gas is 1:0.9 L / m 3 , The flue gas after desulfurization is discharged from the top outlet of the desulfurization tower, and through online detection, SO in the flue ga...
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