Agent for absorbing fire coal flue gas mercury pollutant and preparation and use thereof
A technology for coal-fired flue gas and pollutants, applied in separation methods, chemical instruments and methods, and other chemical processes, to achieve low production costs, high adsorption efficiency, and wide application range
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Embodiment 1
[0037] The preparation method of coal-fired flue gas mercury pollutant adsorbent comprises the following steps:
[0038] 1) Take a certain amount of dewatered sludge from urban sewage plants, add sawdust additive with a mass fraction of 1.5%, stir evenly, then add solid zinc chloride powder 1 times the weight of dry sludge, stir evenly, and let stand for 24 hours.
[0039] 2) Put the static dewatered sludge into the muffle furnace, heat it under the condition of isolating the air, control the heating rate at 15°C / min, raise the temperature to 175°C and dry for 1.5h, and then heat up to the activation temperature of 550°C ℃, the pyrolysis and carbonization time is 2 hours; after cooling in the system state, the dewatered sludge pyrolysis and carbonization products are obtained.
[0040] 3) Rinse the pyrolysis and carbonization product once with 3mol / L hydrochloric acid to remove impurities and metal oxides, then rinse it with 80°C distilled water until the pH is 7.0, and then b...
Embodiment 2
[0045] The preparation process of the coal-fired flue gas mercury pollutant adsorbent is the same as in Example 1, and some process parameters in the process are changed, and the steps and parameters of the change are as follows:
[0046] Step 1): the dosage of sawdust additive is changed to 2%, the dosage of solid zinc chloride powder is 1.5 times the weight of dry sludge, and the standing time is changed to 36h.
[0047] Step 2): heat up to 200°C at a heating rate of 30°C / min and dry for 1.0 h, then heat up to an activation temperature of 700°C, and pyrolysis and carbonization for a certain time of 0.5 h;
[0048] Step 3): The pyrolysis carbonized product was first rinsed twice with 2mol / L hydrochloric acid, then rinsed with 90°C distilled water until the pH was 6.5, and then baked at 120°C for 18 hours.
[0049] Step 4): immerse the adsorbent A in a potassium bromide solution with a concentration of 2mol / L, the solution volume is determined according to 0.55ml per gram of a...
Embodiment 3
[0052] The preparation technological process of adsorbent is identical with embodiment 1, changes some technological parameters in the process, and the steps of change and parameter are as follows:
[0053] Step 1): the dosage of sawdust additive is changed to 1%, the dosage of solid zinc chloride powder is 0.5 times the weight of dry sludge, and the standing time is changed to 12h.
[0054] Step 2): heat up to 150°C at a heating rate of 10°C / min and dry for 2.0 hours, then heat up to an activation temperature of 400°C, and pyrolysis and carbonization for a certain time of 3.0 hours;
[0055] Step 3): The pyrolysis carbonized product was rinsed three times with 1 mol / L hydrochloric acid, then rinsed with 70°C distilled water until the pH was 6.0, and then baked at 100°C for 30 hours.
[0056] Step 4): Put the adsorbent A in a tube furnace, raise the temperature to 175°C at 15°C / min, feed in hydrogen bromide and helium as a carrier gas, and react at constant temperature for 3 h...
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