Preparation method and application core-shell structure laminated double-metal hydroxide composite particles
A layered bimetallic, hydroxide technology, applied in the directions of alkali metal oxides/hydroxides, alkali metal compounds, chemical instruments and methods, etc., can solve the problems of low affinity and poor dispersion of organic pollutants, and achieve The effect of low processing cost, convenient operation and simple process
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Embodiment 1
[0032]Take 1000mL of wastewater containing 2,4-dichlorophenoxyacetic acid at a concentration of 100mg / L, and the temperature is 293K. Add the prepared treatment agent to the wastewater at a dosage of 1.5g / L, and use a pH regulator to adjust the pH of the system to 3.0, 4.0, 5.0, 6.0, 7.0, 8.0, 9.0, 10.0, and the pH regulator is at a concentration of 0.1 mol / L NaOH solution and 0.1mol / L HNO 3 solution. During the reaction, maintain the oscillation speed at 200 rpm (can be adjusted from 150 rpm to 250 rpm), shake for 120 minutes, and then filter with a 0.45 μm filter membrane, take the treated liquid for water quality analysis, and determine the pH = 4, the removal rate can reach 97.32%, and the water quality is stable, such as image 3 As shown, the FT-IR spectrum of the treatment agent before and after adsorption of 2,4-dichlorophenoxyacetic acid is shown in 4.
Embodiment 2
[0034] Take 1000mL of waste water containing 2,4-dichlorophenoxyacetic acid, the pH is 4.0, the initial concentration of 2,4-dichlorophenoxyacetic acid is 5mg / L, 10mg / L, 30mg / L, 50mg / L, 80mg / L L, 120mg / L. The dosage of treatment agent is 1g / L, and the treatment temperature is controlled at 298K, 308K, 318K. During the reaction, the oscillation speed is 200 rpm (can be adjusted from 150 rpm to 250 rpm), and the oscillation time is 120 minutes. After the oscillation is completed, use a 0.45 μm filter membrane to filter, and take the treated liquid for water quality analysis. After data analysis, the saturated adsorption capacity at different temperatures was calculated, and the reaction was determined to be an endothermic reaction, and increasing the temperature would help to increase the removal rate of 2,4-dichlorophenoxyacetic acid.
[0035] The results of this embodiment are shown in the table below:
[0036]
Embodiment 3
[0038] Take 1000mL of wastewater containing 2,4-dichlorophenoxyacetic acid, the initial concentration of 2,4-dichlorophenoxyacetic acid in wastewater is 100mg / L and 200mg / L, the pH value is 4.0, and the adsorption temperature is 298K. Add the treatment agent to the wastewater at a dosage of 0.5 mg / L, the oscillation speed is 200 rpm (adjustable from 150 rpm to 250 rpm), and the oscillation time is 5 minutes to 120 minutes. After the treatment is completed Use a 0.45μm filter membrane to filter, and take the treated liquid for water quality analysis. It is confirmed that the rate of adsorption of 2,4-dichlorophenoxyacetic acid is relatively fast, and the adsorption equilibrium is basically reached in 60 minutes. The results of this example are as Figure 5 shown.
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