A catalytic oxidation additive for wet flue gas mercury removal and preparation method thereof
A catalytic oxidation and additive technology, applied in chemical instruments and methods, separation methods, and dispersed particle separation, etc., can solve the problems of prominent Hg0 control, high mercury, and low chlorine content, so as to solve the problem of mercury pollution control, solve the The effect of secondary pollution and improving utilization rate
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Embodiment 1
[0019] Catalytic oxidation additive: H 2 o 2 The contents of , NaCl and metal salts are calculated based on their respective dosing concentrations in the desulfurization slurry, where H 2 o 2 Dosing concentration is 0.05mol / L, NaCl dosing concentration is 0.05mol / L, MnCl 2 The dosing concentration is 0.1mol / L, and the three are mixed evenly.
[0020] The dynamic experiment was carried out in a small packed desulfurization tower with limestone as the desulfurizer, and the density of the limestone slurry was 1150kg / m 3 -1300kg / m 3 , the slurry pH is about 5.6, and the simulated flue gas condition is imported Hg 0 0.3mg / m 3 , SO 2 1000ppm, O 2 3%, CO 2 12%, the rest is N 2 , control the flue gas flow to 1L / min. Add the prepared catalytic oxidation additive directly into the slurry tank, and send it to the absorption tower for reaction after being mixed evenly. The mercury content at the inlet was measured by solution absorption and cold atomic fluorescence, so as to c...
Embodiment 2
[0023] Catalytic oxidation additive: H 2 o 2 The contents of , NaCl and metal salts are calculated based on their respective dosing concentrations in the desulfurization slurry, where H 2 o 2 Dosing concentration is 0.05mol / L, NaCl dosing concentration is 0.1mol / L, Co(NO 3 ) 2 The dosing concentration is 0.1mol / L, and the three are mixed evenly.
[0024] The dynamic experiment was carried out in a small packed desulfurization tower with limestone as the desulfurizer, and the density of the limestone slurry was 1150kg / m 3 -1300kg / m 3 , the slurry pH is about 5.6, and the simulated flue gas condition is imported Hg 0 0.3mg / m 3 , SO 2 1000ppm, O 2 3%, CO 2 12%, the rest is N 2 , control the flue gas flow to 1L / min. Add the prepared catalytic oxidation additive directly into the slurry tank, and send it to the absorption tower for reaction after being mixed evenly. The mercury content at the inlet was measured by solution absorption and cold atomic fluorescence, so as...
Embodiment 3
[0027] Catalytic oxidation additive: H 2 o 2 The contents of , NaCl and metal salts are calculated based on their respective dosing concentrations in the desulfurization slurry, where H 2 o 2 Dosing concentration is 0.05mol / L, NaCl dosing concentration is 0.1mol / L, MnCl 2 Dosing concentration is 0.2mol / L, the three are mixed evenly
[0028] The dynamic experiment was carried out in a small packed desulfurization tower with limestone as the desulfurizer, and the density of the limestone slurry was 1150kg / m 3 -1300kg / m 3 , the slurry pH is about 5.6, and the simulated flue gas condition is imported Hg 0 0.3mg / m 3 , SO 2 1000ppm, O 2 3%, CO 2 12%, the rest is N 2 , control the flue gas flow to 1L / min. Add the prepared catalytic oxidation additive directly into the slurry tank, and send it to the absorption tower for reaction after being mixed evenly. The mercury content at the inlet was measured by solution absorption and cold atomic fluorescence, so as to calculate t...
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