Additive for inhibiting re-release of mercury during wet method flue gas desulfurization process and using method thereof
A wet flue gas desulfurization and additive technology, which is applied in separation methods, chemical instruments and methods, and dispersed particle separation, etc., can solve problems such as secondary pollution, suppress re-release, improve mercury removal efficiency, and solve mercury pollution problems. Effect
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Embodiment 1
[0017] The desulfurization slurry used in this example is 1% limestone slurry, and 1mmol / L of additives for inhibiting mercury re-release in the wet flue gas desulfurization process are added to the limestone slurry. The additive composition is: sodium tetrasulfide 35wt%, dimethyl 30wt% sodium dithiocarbamate, 35wt% 2,4,6-trimercapto-s-triazine trisodium salt, adjust the pH value of the slurry to 5.5, the temperature is 55°C, and the simulated flue gas composition is 12% CO 2 , 6%O 2 , SO 2 300ppm, the rest is N 2 , using a peristaltic pump to pump 50 μg / L of Hg into the bubbling reactor at a flow rate of 10 mL / h 2+ solution, the absorption liquid volume in the bubble reactor is 400mL, and the flue gas flow rate at the inlet is 1L / min. The inhibitory rate of the additives on the re-release of mercury in the slurry reaches 91.6%.
Embodiment 2
[0019] The desulfurization slurry used in this example is 1% limestone slurry, and 1mmol / L of additives for inhibiting mercury re-release in the wet flue gas desulfurization process is added to the limestone slurry. The additive composition is: sodium tetrasulfide 30wt%, dimethyl 45wt% dithiocarbamate, 25wt% 2,4,6-trimercapto-s-triazine trisodium salt, adjust the pH value of the slurry to 5.5, the temperature is 55°C, and the simulated flue gas composition is 12% CO 2 , 6%O 2 , SO 2 300ppm, the rest is N 2 , using a peristaltic pump to pump 50 μg / L of Hg into the bubbling reactor at a flow rate of 10 mL / h 2+ solution, the absorption liquid volume in the bubble reactor is 400mL, and the flue gas flow rate at the inlet is 1L / min. The inhibitory rate of the additives on the re-release of mercury in the slurry reaches 89.4%.
Embodiment 3
[0021] The desulfurization slurry used in this example is 1% limestone slurry, and 1mmol / L of additives for inhibiting mercury re-release in the wet flue gas desulfurization process are added to the limestone slurry. The additive composition is: sodium tetrasulfide 40wt%, dimethyl 30wt% dithiocarbamate, 30wt% 2,4,6-trimercapto-s-triazine trisodium salt, adjust the pH value of the slurry to 5.5, the temperature is 55°C, and the simulated flue gas composition is 12% CO 2 , 6%O 2 , SO 2 300ppm, the rest is N 2 , using a peristaltic pump to pump 50 μg / L of Hg into the bubbling reactor at a flow rate of 10 mL / h 2+ solution, the absorption liquid volume in the bubble reactor is 400mL, and the flue gas flow rate at the inlet is 1L / min. The inhibitory rate of the additives on the re-release of mercury in the slurry reaches 90.4%.
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