A method for remediating petroleum hydrocarbon-contaminated soil using in-situ oxidation-synchronous air flotation
An in-situ oxidation and contaminated soil technology, applied in the restoration of contaminated soil, etc., can solve the problems of unsatisfactory removal of heavy oil, long bioremediation cycle, lack of remediation technology, etc., to achieve resource utilization and fast remediation , The effect of simple process
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Embodiment 1
[0028] Embodiment 1 repairs the method for petroleum hydrocarbon contaminated soil:
[0029] Weigh 10g of petroleum-contaminated soil (soil moisture content 60%, oil content 18%), place in a 100mL glass reactor, add 0.15mL of 0.6mol / L citric acid solution, 0.6mol / L sodium hydroxide Solution 0.15mL, 1.5mL of 1.2mol / L hydrochloric acid and 0.3mL of 0.3mol / L ferrous sulfate solution, mix and stir evenly, finally slowly add 0.9mL of hydrogen peroxide with a mass concentration of 28% in the mud, keep stirring to make it fully Reaction, scrape off the oil slick on the liquid surface while the bubbles are continuously escaping from the liquid surface and bring out the oil slick. The time for in-situ oxidation and air flotation is 10 hours. Petroleum hydrocarbon content in post-silt.
[0030] After the oil-contaminated soil above was treated by the new in-situ oxidation-synchronous air flotation process, the removal rate of petroleum hydrocarbons in the soil reached 83.1%.
Embodiment 2
[0031] Embodiment 2: take by weighing 10g petroleum-contaminated soil (soil moisture content is 60%, and oil content is 16%), is placed in 100mL glass reactor, adds the citric acid solution 0.10mL of 0.6mol / L successively, 0.6mol / L 0.10mL of sodium hydroxide solution, 0.8mL of 1.2mol / L hydrochloric acid and 0.2mL of 0.3mol / L ferrous sulfate solution, mix and stir evenly, finally slowly add 0.9mL of mass concentration to the mud and be 28% hydrogen peroxide, in Under normal temperature, keep stirring to make it fully react, realize the in-situ oxidation decomposition of some petroleum hydrocarbons; use the micro-bubbles generated in the in-situ oxidation process as the carrier, adhere to the petroleum hydrocarbon oil droplets in the sewage, and the micro-bubbles continue to escape from the liquid The oil slick is brought out on the surface, after the bubbles burst, and the oil droplets are gathered, and the scraping device is used to scrape off the slick oil on the liquid surfac...
Embodiment 3
[0033] Embodiment 3: take by weighing 10g petroleum-contaminated soil (soil moisture content is 60%, and oil content is 18%), is placed in 100mL glass reactor, adds the citric acid solution 0.15mL of 0.6mol / L successively, 0.6mol / L 0.15mL of sodium hydroxide solution, 1.5mL of 1.2mol / L hydrochloric acid and 0.3mL of 0.3mol / L ferrous sulfate solution, mix and stir evenly, and finally add 0.6mL of hydrogen peroxide with a mass concentration of 28% slowly in the mud, and continue Stir to make it fully react, and scrape off the oil slick on the liquid surface while the bubbles continuously escape from the liquid surface to bring out the oil slick. The time for in-situ oxidation and air flotation is 10 hours. The petroleum hydrocarbon content in the treated mud sand was determined by gravimetric method.
[0034] After the above-mentioned petroleum-contaminated soil is treated by the new in-situ oxidation-synchronous air flotation process, the removal rate of petroleum hydrocarbons ...
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