Disposal method of using As-containing wastewater in LED industry for preparing electronic-grade ultrapure water
A treatment method, electronic-level technology, applied in the direction of water/sewage multi-stage treatment, water/sludge/sewage treatment, non-polluted water treatment, etc., can solve the problem of increasing the cost of subsequent hazardous waste/solid waste treatment and large sludge output , waste of water resources and other issues, to achieve the effect of reducing sludge production, realizing zero discharge of wastewater, and reducing waste
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Embodiment 1
[0041] An LED industry contains As-containing wastewater, in which the As content is 35mg / L, the conductivity=200μs / cm, and the pH=6.7.
[0042] Step (1): Take 20 L of the above wastewater, add 0.5g / L pretreatment agent, stir and react for 20 minutes, add sodium hydroxide to adjust pH=8, let stand and filter, the filtrate pH=7.2;
[0043]Step (2): After step (1), the effluent water enters the adsorption system, the adsorption water flow rate is 5BV / h, the amount of activator added is 0.05%, and the aeration rate is 1mL / min;
[0044] Step (3): The effluent from step (2) enters the ultrafiltration system, in which the security filter selects a PP cotton filter element with a pore size of 5 μm, and the ultrafiltration membrane selects a hollow fiber membrane made of polyvinylidene fluoride with a pore size of 0.005 μm. Choose 0.1MPa, the operating temperature is 25 degrees Celsius;
[0045] Step (4): The effluent from step (3) enters the reverse osmosis system. The reverse osmos...
Embodiment 2
[0050] An LED industry contains As-containing wastewater, in which the As content is 10 mg / L, the conductivity is 100 μs / cm, and the pH is 7.2.
[0051] Step (1): After the As-containing wastewater is directly filtered, it enters the adsorption system, the adsorption water flow rate is 5 BV / h, the amount of activator is 0.1%, and the aeration rate is 1mL / min;
[0052] Step (2): The effluent from step (1) enters the ultrafiltration system, in which the security filter selects a PP cotton filter element with a pore size of 5 μm, and the ultrafiltration membrane selects a hollow fiber membrane made of polyvinylidene fluoride with a pore size of 0.005 μm. Choose 0.15MPa, the operating temperature is 25 degrees Celsius;
[0053] Step (3): The effluent from step (2) enters the reverse osmosis system, using only one-stage reverse osmosis with a membrane pressure of 2MPa and an operating temperature of 25 degrees Celsius.
[0054] Step (5): The effluent from step (4) enters the EDI s...
Embodiment 3
[0058] An LED industry contains As-containing wastewater, in which the As content is 100 mg / L, the conductivity=500μs / cm, and the pH=5.9.
[0059] Step (1): Take 20 L of the above wastewater, add 1g / L pretreatment agent, stir and react for 20 minutes, add sodium hydroxide to adjust pH = 8, let stand and filter, the filtrate pH = 7.2;
[0060] Step (2): After step (1), the filtered effluent enters the adsorption system, the adsorption water flow rate is 4BV / h, the amount of activator added is 0.1%, and the aeration rate is 2mL / min;
[0061] Step (3): The effluent from step (2) enters the ultrafiltration system, in which the security filter selects a PP cotton filter element with a pore size of 5 μm, and the ultrafiltration membrane selects a hollow fiber membrane made of polyvinylidene fluoride with a pore size of 0.005 μm. Choose 0.1MPa, the operating temperature is 25 degrees Celsius;
[0062] Step (4): The effluent from step (3) enters the reverse osmosis system. The revers...
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