A method for preparing high-efficiency adsorbent by using fluidized bed gasification fly ash and industrial waste sulfuric acid
A fluidized bed gasification, waste sulfuric acid technology, applied in chemical instruments and methods, separation methods, gas treatment and other directions, can solve the problems of resource waste, fly ash on-site pollution, etc., to reduce pollution, solve dust pollution problems, process Simple process effect
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Embodiment 1
[0039] A method for preparing a high-efficiency adsorbent by gasifying fly ash and high-concentration industrial waste sulfuric acid in a fluidized bed, characterized in that, first, adding fly ash and raw coal masterbatch to a reactor with a stirring device according to the mass ratio of 1:1 , and stirred under airtight conditions for 0.7 hours. After the stirring is completed, add coking high-temperature coal tar (contains 9% naphthalene oil by mass and 21% anthracene oil by mass) into the reactor. Hour. Then, add industrial waste sulfuric acid with a weight percentage of 85% to the reactor, and the mass ratio of the added industrial waste sulfuric acid to coal tar, raw coal masterbatch and fly ash is 1.5:1. Stir for 10 minutes under closed condition of the reactor. During the reaction, gas A is generated and discharged from the upper part of the reactor. Finally, the mixed gas B is introduced from the bottom of the reactor, the volume concentration of oxygen in B is 2.5%,...
Embodiment 2
[0043] A method for preparing high-efficiency adsorbent by gasifying fly ash and high-concentration industrial waste sulfuric acid in a fluidized bed. It is characterized in that, first, fly ash and raw coal masterbatch are added into a reactor with a stirring device according to a mass ratio of 1.7:1, and stirred for 0.7 hours under airtight conditions. After the stirring is completed, add coking high-temperature coal tar (the mass contains 11% of naphthalene oil and 18% of anthracene oil) into the reactor, the mass ratio of the added coal tar to fly ash is 2.1:1, and stir under closed conditions 0.55 hours. Then, 80% by weight of industrial waste sulfuric acid is added to the reactor, and the mass ratio of the added industrial waste sulfuric acid to coal tar, raw coal masterbatch and fly ash is 3.1:1. Stir for 17 minutes under the closed condition of the reactor. During the reaction, gas A is generated and discharged from the upper part of the reactor. Finally, the mixed g...
Embodiment 3
[0047] A method for preparing high-efficiency adsorbent by gasifying fly ash and high-concentration industrial waste sulfuric acid in a fluidized bed. It is characterized in that, first, fly ash and raw coal masterbatch are added into a reactor with a stirring device according to a mass ratio of 2.0:1, and stirred for 0.8 hours under airtight conditions. After the stirring is completed, add coking high-temperature coal tar (the mass contains 12% of naphthalene oil and 22% of anthracene oil) into the reactor, the mass ratio of the added coal tar to fly ash is 3.5:1, and stir under closed conditions 0.65 hours. Then, add industrial waste sulfuric acid with a weight percentage of 90% to the reactor, and the mass ratio of the added industrial waste sulfuric acid to coal tar, raw coal masterbatch and fly ash is 4.6:1. Stir for 17 minutes under the closed condition of the reactor. During the reaction, gas A is generated and discharged from the upper part of the reactor. Finally, t...
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Abstract
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