Sorbent for removing mercury from flue gas and preparation method thereof
An adsorbent and mercury removal technology, which is applied in separation methods, chemical instruments and methods, and other chemical processes, can solve the problems of complex manufacturing process and high cost, and achieve the effect of uniform distribution, low cost, and easy operation
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Embodiment 1
[0018] The adsorbent for flue gas demercuration in this embodiment includes activated carbon and sulfur evenly distributed on the surface of the activated carbon, the particle size of the activated carbon is 20-40 mesh, and the mass percentage of sulfur is 7%;
[0019] The preparation method of the adsorbent for flue gas demercuration of the present embodiment comprises the following steps:
[0020] a. Dry the activated carbon at 105°C until the water absorption is less than 1%;
[0021] b. Put the activated carbon in step a into a heat-resistant container and place the heat-resistant container in the lower part of the heat-precipitation furnace, place the elemental sulfur in the middle of the heat-precipitation furnace, seal the heat-precipitation furnace, and feed it into the high-temperature furnace at a rate of 1L / min Pure N 2 30min, replace the air in the thermal precipitation furnace; then adjust the N 2 The flow rate is 0.5L / min, the temperature is raised to 400°C, an...
Embodiment 2
[0025] The adsorbent for flue gas demercuration in this embodiment includes activated carbon and sulfur evenly distributed on the surface of the activated carbon, the particle size of the activated carbon is 20-40 mesh, and the mass percentage of sulfur is 10.34%;
[0026] The preparation method of the adsorbent for flue gas demercuration of the present embodiment comprises the following steps:
[0027] a. Dry the activated carbon at 105°C until the water absorption is less than 1%;
[0028] b. Put the activated carbon in step a into a heat-resistant container and place the heat-resistant container in the lower part of the heat-precipitation furnace, place the elemental sulfur in the middle of the heat-precipitation furnace, seal the heat-precipitation furnace, and feed it into the high-temperature furnace at a rate of 2L / min Pure N 2 40min, replace the air in the thermal precipitation furnace; then adjust the N 2 The flow rate is 0.5L / min, the temperature is raised to 550°C...
Embodiment 3
[0031] The adsorbent for flue gas demercuration in this embodiment includes activated carbon and sulfur evenly distributed on the surface of the activated carbon, the particle size of the activated carbon is 20-40 mesh, and the mass percentage of sulfur is 17%;
[0032] The preparation method of the adsorbent for flue gas demercuration of the present embodiment comprises the following steps:
[0033] a. Dry the activated carbon at 105°C until the water absorption is less than 1%;
[0034] b. Put the activated carbon in step a into a heat-resistant container and place the heat-resistant container in the lower part of the heat-precipitation furnace, place the elemental sulfur in the middle of the heat-precipitation furnace, seal the heat-precipitation furnace, and feed it into the high-temperature furnace at a rate of 2L / min Pure N 2 40min, replace the air in the thermal precipitation furnace; then adjust the N 2 The flow rate is 0.5L / min, the temperature is raised to 600°C, a...
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