Method for processing heavy metal ion in water using amidocyanogen modified Fe3O4@SiO2 composite microparticle
A technology of heavy metal ions and composite particles, applied in water/sewage treatment, chemical instruments and methods, water/sludge/sewage treatment, etc., to achieve the effects of convenient operation, remarkable treatment effect and low cost
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Embodiment 1
[0025] Amino-modified Fe 3 o 4 @SiO 2 Synthesis of composite particles: Weigh 2 g of dried Fe 3 o 4 @SiO 2 Add the composite particles into a 250mL three-necked round-bottom flask, then add 50mL of toluene, and ultrasonically disperse for 15min. Press Fe 3 o 4 @SiO 2 The mass volume ratio of the composite particles to the silane reagent is 1:2 (g / mL), add 3-aminopropyl-trimethoxysilane, and reflux at 110°C for 12h. The reacted Fe 3 o 4 @SiO 2 The composite particles were washed several times with absolute ethanol and acetone. The washed Fe 3 o 4 @SiO 2 The composite particles were dried in an oven at 50°C for later use to obtain amine-modified Fe 3 o 4 @SiO 2 Composite particles.
[0026] Amino-modified Fe 3 o 4 @SiO 2 Composite particles are used as adsorbents to treat Cu containing heavy metal ions 2+ slightly polluted water. Adsorption is carried out in a closed container (volume 50mL), the mass ratio of adsorbent to slightly polluted water is 1:2500,...
Embodiment 2
[0028] Amino-modified Fe 3 o 4 @SiO 2 Synthesis of composite particles: weigh 1 g of dried Fe 3 o 4 @SiO 2 Add the composite particles into a 250mL three-necked round-bottomed flask, then add 30mL of toluene, and ultrasonically disperse for 10min. Press Fe 3 o 4 @SiO 2 The mass volume ratio of the composite particles to the silane reagent is 1:3 (g / mL), add 3-aminopropyl-triethoxysilane, and reflux at 110°C for 10h. Other treatment is the same as embodiment 1, obtains the Fe of amino modification 3 o 4 @SiO 2 Composite particles.
[0029] Amino-modified Fe 3 o 4 @SiO 2 Composite particles are used as adsorbents to treat heavy metal ions containing Ni 2+ slightly polluted source water. Adsorption condition is the same as embodiment 1, Ni 2+ 、Cd 2+ The initial concentration of Ni is 36.8mg / L and 30.7mg / L respectively, the adsorption temperature is 298K, the adsorption time is 24h, Ni 2+ 、Cd 2+ The removal rates were 47.3% and 85.7%.
Embodiment 3
[0031] Condition is the same as embodiment 1. The adsorption temperature is 298k, Ni 2+ The initial concentration of Cd is 46.0mg / L, and its out rate is 38.3%; Cd 2+ The initial concentration of is 40.9mg / L, and its elimination rate is 70.2%.
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