A kind of modified fly ash adsorbent and its preparation method and application
A fly ash and adsorbent technology, applied in chemical instruments and methods, adsorption water/sewage treatment, other chemical processes, etc., can solve the problems of high material cost, poor adsorption effect of heavy metals, etc., to reduce reaction energy consumption, Achieve resource utilization and reduce production costs
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Embodiment 1
[0038] 1. Preparation of modified fly ash adsorbent
[0039] Take the fly ash from a power plant, grind it, and sieve it to get the pretreated fly ash with a particle size of about 100 microns.
[0040]Add an appropriate amount of water, ferrous sulfate solution and ferric chloride salt solution to the above-mentioned pretreated fly ash, and adjust the pH value to 8.5 to control the ratio between the quality of fly ash and the total mass of ferrous sulfate and ferric chloride. The ratio is 100:1, and the molar ratio of ferrous sulfate to ferric chloride is 1:2. Under the conditions of room temperature and 160r / min, the primary modification is performed for 60 minutes to obtain primary modified fly ash.
[0041] Add calcium hydroxide to the above-mentioned primary modified fly ash, control the mass ratio of primary modified fly ash to calcium hydroxide to 10:1, slowly stir at 60r / min for 30 minutes, and then age for 2 hours to obtain Secondary modified fly ash.
[0042] The s...
Embodiment 2
[0049] 1. Preparation of modified fly ash adsorbent
[0050] Take the fly ash from a power plant, grind it, and sieve it to get the pretreated fly ash with a particle size of about 200 microns.
[0051] Add an appropriate amount of water, ferrous sulfate solution and ferric chloride salt solution to the above-mentioned pretreated fly ash, and adjust the pH value to 8.5 to control the ratio between the quality of fly ash and the total mass of ferrous sulfate and ferric chloride. The ratio is 80:1, and the molar ratio of ferrous sulfate to ferric chloride is 1:2. Under the conditions of room temperature and 140r / min, the primary modification is performed for 80 minutes to obtain primary modified fly ash.
[0052] Add calcium hydroxide to the above-mentioned primary modified fly ash, control the mass ratio of primary modified fly ash and calcium hydroxide to 20:1, stir slowly at 40r / min for 40 minutes, and then age for 5 hours to obtain Secondary modified fly ash.
[0053] The ...
Embodiment 3
[0058] Except that the reactor structure adopted is different, all the other are basically the same as Example 1.
[0059] combine figure 1 , the reactor structure of the present embodiment is as follows:
[0060] The reactor of this embodiment has a shell 1, and inside the shell 1 is provided with at least two packing layers 2 arranged at intervals up and down, and a sedimentation zone is set below the packing layer 2, and the modified fly ash of Example 1 is adsorbed The heavy metal wastewater flows through the packing layer 2 from top to bottom and contacts with the modified fly ash adsorbent in the packing layer 2. The filling amount of the modified fly ash adsorbent is equal to that of the wastewater in the reactor. 2%.
[0061] The housing 1 is set to a cylindrical shape, and the packing layer 2 adopts porous sponge, and the total height of the packing layer 2 is the same as that of the packing layer in embodiment 1; an arc top 3 is arranged between adjacent packing la...
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Abstract
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