A process for treating heavy metal wastewater by using fly ash
A heavy metal, fly ash technology, applied in water/sewage treatment, adsorbed water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problem of increased production cost, large amount of adsorbent, and utilization of adsorbent adsorption capacity. Low rate and other problems, to achieve the effect of convenient operation, simple process, easy promotion and implementation
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Embodiment 1
[0022] The fly ash used in embodiment 1, embodiment 2 and comparative example is made up of the component of following percentage by weight: SiO 2 : 52.87%; Al 2 o 3 : 24.19%; Fe 2 o 3 : 8.33%; CaO: 3.67%; K 2 O: 1.45%; MgO: 1.03%; SO 3 : 0.77%; TiO 2 : 0.74%; Impurities: 6.95%.
[0023] Example 1
[0024] A process for efficiently treating heavy metal wastewater using fly ash, comprising the following steps:
[0025] (1) start: first add in the reactor that the pH value is 6.2, the volume is 1L, the concentration of nickel is 10.07mg / L heavy metal waste water and the quality is 4g of fly ash, stirring makes its adsorption reach balance;
[0026] (2) Dosing: After adding 1.6g of fly ash to the reactor, stir to make it reach adsorption equilibrium, and obtain effluent with a nickel concentration of 0.47mg / L, and then remove it from the reactor by precipitation separation. Discharge water with a volume of 0.4L;
[0027] (3) Influent: in the reactor, supplement volume i...
Embodiment 2
[0031] A process for efficiently treating heavy metal wastewater using fly ash, comprising the following steps:
[0032] (1) Start-up: first add to the reactor a pH value of 6.2, a volume of 1L, a nickel concentration of 10.07mg / L of heavy metal waste water and a quality of 3.6g of fly ash, stirring to make its adsorption reach equilibrium;
[0033] (2) Dosing: After adding 2.52g of fly ash to the reactor, stir to make it reach adsorption equilibrium, and obtain effluent with a nickel concentration of 0.48mg / L, and then remove it from the reactor by precipitation separation. Discharge water with a volume of 0.7L;
[0034] (3) Influent: in the reactor, replenishing volume is 0.7L, the concentration of nickel is the heavy metal waste water of 10.07mg / L, and the concentration of nickel in the reactor is 7.19mg / L this moment, continue to throw in the step (2) The added fly ash undergoes an adsorption reaction, and after reaching the adsorption equilibrium, the pretreated water wi...
Embodiment 3
[0038] A process for efficiently treating heavy metal wastewater using fly ash, comprising the following steps:
[0039] (1) Start-up: first add to the reactor a pH value of 6.0, a volume of 1L, a copper concentration of 10.01mg / L of heavy metal waste water and a quality of 3.9g of fly ash, stirring to make its adsorption reach equilibrium;
[0040] (2) Dosing: After adding 1.95g of fly ash to the reactor, stir to make it reach adsorption equilibrium, and obtain effluent with a copper concentration of 0.45 mg / L, and then remove it from the reactor by precipitation separation. Discharge water with a volume of 0.5L;
[0041] (3) Influent water: add to the reactor volume 0.5L, the concentration of copper is 10.01mg / L waste water, at this moment the concentration of copper in the reactor is 5.23mg / L, continue to add in step (2) The fly ash carried out the adsorption reaction, and the concentration of copper obtained after reaching the adsorption equilibrium is 1.5mg / L pretreated ...
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