Harmless treatment system and method for fracturing flowback fluid
A fracturing flowback fluid, harmless treatment technology, applied in chemical instruments and methods, oxidized water/sewage treatment, mining wastewater treatment, etc. To deal with problems such as unstable treatment effect, to achieve the effect of good process treatment effect, simplified operation and avoid long processing time
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Embodiment 1
[0047] Add a gel-breaking flocculant to the 100L oil-gas field fracturing operation and return it to the ground. The gel-breaking flocculant is calcium oxide, aluminum sulfate, and ferrous sulfate. Liquid discharge meter, the addition of calcium oxide is 10g / L, the addition of aluminum sulfate is 2g / L, and the addition of ferrous sulfate is 8g / L. After fully stirring for 0.5-2h, the precipitation is allowed to stand for 2h. Separation, and then the supernatant overflows into the buffer tank; the effluent after the pretreatment step and the precipitation separation step is pumped out from the buffer tank through the lift pump, adjust the pH of the effluent to pH=4-6, and then add 1g of ferrous sulfate and 3ml of 30% hydrogen peroxide Fenton reagent, after the reaction time of 4 hours, adjust the pH of the effluent to 8 and undergo precipitation separation, then overflow the supernatant generated by the precipitation separation into the buffer tank; after the Fenton oxidation ste...
Embodiment 2
[0052]Add gel-breaking and flocculant agents to the 250L oil and gas field fracturing operation and return to the ground. The gel-breaking and flocculant is calcium oxide, aluminum sulfate, and ferrous sulfate. Calcium oxide was added in an amount of 15g / l, aluminum sulfate was added in an amount of 8g / l, and ferrous sulfate was added in an amount of 12g / l. After fully stirring for 0.5h, the precipitate was separated for 3h, and then the precipitate was separated. The supernatant produced by the separation overflows into the buffer tank; the effluent from the pretreatment step and the precipitation separation step is extracted from the buffer tank through a lift pump, and the pH of the effluent is adjusted to pH=4-6 with sulfuric acid and then under aeration conditions (50L / h) Carry out iron-carbon micro-electrolytic oxidation treatment for 1 hour, use 15% sodium hydroxide solution to adjust the pH of the reaction effluent to 9, then precipitate and separate for 3 hours, then ...
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