Flue gas mercury absorption liquid with functions of oxidizing and fixing synchronously
A technology for mercury absorption and coal-fired flue gas, which is applied in chemical instruments and methods, dispersed particle separation, separation methods, etc., can solve the problems of large consumption of oxidant, unsatisfactory reduction inhibition effect, increased absorption liquid corrosion, etc., to achieve mercury The effect of high removal rate
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Embodiment 1
[0040] Example 1: Fenton's reagent oxidation combined with lime slurry + sodium thiosulfate to absorb and remove mercury
[0041] The mercury removal absorption liquid used in this embodiment includes lime slurry with a mass concentration of 4%, and Fenton's reagent and sodium thiosulfate, Fe 3+ From Ferric Chloride, Fe 3+ :H 2 o 2 =0.5, the pH value of the absorption solution is 3.5, and the addition amount of Fenton’s reagent is expressed as H 2 o 2 Calculated as 0.09mol / L, the amount of sodium thiosulfate added is 0.8mol / L; under simulated conditions, the imported mercury concentration is 60μg / L, the sulfur dioxide concentration is 500ppm, and the gas volume is 2L / min, the height of the absorption liquid is 14cm, and the volume of the absorption liquid is 300ml. The removal rate of sulfur dioxide is greater than 25%, and the removal efficiency of mercury reaches 50%.
Embodiment 2
[0042] Example 2: Fenton reagent oxidation combined with limestone slurry + calcium thiosulfate to absorb and remove mercury
[0043] The mercury removal absorbing solution used in this embodiment includes limestone slurry with a mass concentration of 4%, and Fenton's reagent and sodium thiosulfate, Fe 3+ From Ferric Chloride, Fe 3+ :H 2 o 2 =0.6, the pH value of the absorption solution is 1.5, and the addition amount of Fenton's reagent is expressed as H 2 o 2 Calculated as 0.07mol / L, the amount of sodium thiosulfate added is 0.6mol / L; under simulated conditions, the imported mercury concentration is 60μg / L, absorbed by the bubble bottle, the gas volume is 2L / min, and the absorption liquid height is 14cm , the volume of the absorption liquid is 300ml, the temperature of the absorption liquid is 30°C; the removal rate of sulfur dioxide is greater than 20%, and the removal efficiency of mercury reaches 60%.
Embodiment 3
[0044] Example 3: Fenton reagent oxidation combined with calcium oxide + potassium thiosulfate to absorb and remove mercury
[0045] The mercury removal absorbing solution used in this embodiment includes a calcium oxide (calcium hydroxide after entering the solution) slurry with a mass concentration of 3%, and in the slurry, Fenton's reagent and potassium thiosulfate, Fe 3+ From ferric nitrate, Fe 3+ :H 2 o 2 =0.7, the pH value of the absorption solution is 1.5, and the addition amount of Fenton’s reagent is expressed as H 2 o 2 Calculated as 0.15mol / L, the amount of potassium thiosulfate added is 0.9mol / L; under simulated conditions, the imported mercury concentration is 60μg / L, the sulfur dioxide concentration is 500ppm, and the gas volume is 2L / min, the height of the absorption liquid is 14cm, the volume of the absorption liquid is 300ml, and the temperature of the absorption liquid is 45°C; the removal rate of sulfur dioxide is greater than 35%, and the removal effic...
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