Desulfurization absorption liquid capable of simultaneously stabilizing bivalent mercury
A technology for absorbing liquid and divalent mercury, which is applied in the separation of dispersed particles, chemical instruments and methods, separation methods, etc., can solve the problems of deterioration of slurry, equipment wear, poor effect, etc., and achieves suppression of reduction, recycling of resources, and efficient desulfurization. effect of effect
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Embodiment 1
[0028] The mass ratio of calcium carbide slag (industrial waste discharged during the production of acetylene from calcium carbide) to MgO in the absorption liquid is 20:100, the solid concentration of the slurry is 10%, the volume is 5L, the pH is controlled at 4-10, and the temperature is controlled At around 45°C, bubble SO with a concentration of 200ppm into the slurry 2 And the concentration is 80ug / m 3 The mixed gas of divalent mercury, the gas flow rate is 10L / min. After passing through the absorption liquid for 2 hours, SO in the tail gas 2 The concentration is 15ppm, the total mercury concentration is 5ug / m 3 , The desulfurization efficiency is 92.5%; , The total mercury removal efficiency is 94%.
Embodiment 2
[0030] The mass ratio of calcium carbide slag (industrial waste discharged during the production of acetylene from calcium carbide) to MgO in the absorption liquid is 5:100, the solid concentration of the slurry is 10%, the volume is 5L, the pH is controlled at 4-10, and the temperature is controlled At around 45°C. Bubble SO at a concentration of 200ppm into the slurry 2 And the concentration is 80ug / m 3 The mixed gas flow rate of divalent mercury is 10L / min. After passing through the absorption liquid for 2 hours, SO in the tail gas 2 The concentration is 8ppm, the total mercury concentration is less than 24ug / m 3 , the desulfurization efficiency is 95%; the mercury removal efficiency is 70%.
Embodiment 3
[0032] The mass ratio of calcium carbide slag (industrial waste discharged during the production of acetylene from calcium carbide) to MgO in the absorption liquid is 30:100, the solid concentration of the slurry is 10%, the volume is 5L, the pH is controlled at 4-10, and the temperature is controlled At around 45°C. Bubble SO at a concentration of 200ppm into the slurry 2 And the concentration is 80ug / m 3 The mixed gas of divalent mercury, the gas flow rate is 10L / min. After passing through the absorption liquid, the tail gas concentration SO 2 48ppm, the total mercury concentration is less than 7ug / m 3 , the desulfurization efficiency is 76%; the mercury removal efficiency is 91.25%.
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