Zinc-iron layered double metal hydroxide adsorbent, and application thereof in removal of phosphorus and chromium
A layered bimetallic and hydroxide technology, applied in the direction of alkali metal oxides/hydroxides, alkali metal compounds, adsorption water/sewage treatment, etc., can solve the pollution of fresh water resources, affect people's daily life, and ignore the removal of cations Effect and other issues, to achieve the effect of solving pollution problems, significant social value and research value, and good adsorption effect
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Embodiment 1
[0020] Accurately weigh 4.3134g ZnSO 4 and 1.3901 g FeSO 4 ·7H 2 O(molar ratio Zn 2+ / Fe 2+ =3:1) was dissolved in 30ml distilled water and kept stirring, and at the same time slowly added 1.0mol / L NaOH solution dropwise to the mixed solution until the pH of the mixed solution reached about 7.5 and remained basically unchanged, stirred at a constant speed for 2 hours, and then added to the mixed solution In the solution, the mass fraction of 6% hydrogen peroxide was added dropwise, and the Fe 2+ Oxidized to Fe 3+ , aged at 40°C for 4h, filtered and washed the solid precipitate until neutral, dried at 60°C, and ground through a 100-mesh sieve to obtain ZnFe-LDH.
[0021] Take 50ml of phosphorus-containing simulated wastewater with a concentration of 25mg / L and put it into a stoppered Erlenmeyer flask, adjust the pH to 6, add 0.08g of ZnFe-LDH, stir in a magnetic stirrer at 25°C and 180r / min for 4h, and put it on after adsorption. The supernatant was filtered with a 0.22 μ...
Embodiment 2
[0023] Operation method is the same as embodiment 1.
[0024] Get 50ml of phosphorus-containing simulated waste water of 50mg / L and put it into a stoppered Erlenmeyer flask, Cl — , NO 3 — , SO 4 2— , CO 3 2— The ion concentration was 5, 50mmol / L, the pH of the solution was adjusted to 6, and 0.05g (1g / L) of ZnFe-LDH was added respectively, and stirred in a magnetic stirrer at 25°C and 180r / min for 4h, and the supernatant was absorbed with 0.22 μm syringe filter, the calculated removal rates under the condition of coexistence of different concentrations of anions are respectively Cl — : 70%, 78.5%; NO 3 — : 70.5%, 81.5%; SO 4 2— : 58%, 69.8%; CO 3 2— : 52.2%, 42.3%. The order of the effect of coexisting anions on the adsorption of phosphorus is CO 3 2— >SO 4 2— >Cl — >NO 3 — .
Embodiment 3
[0026] Operation method is the same as embodiment 1.
[0027] Take 50ml of 10mg / L simulated wastewater containing Cr(VI) in a stoppered Erlenmeyer flask, adjust the pH to 7.5, add 0.11g of ZnFe-LDH, stir in a magnetic stirrer at 25°C and 180r / min for 4h, and put on The supernatant was filtered with a 0.22 μm needle filter, and the calculated removal rate was 86.7%.
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