Ternary compound oil drive water exit processing method
A technology of ternary compounding and processing method, applied in the field of environmental engineering, can solve problems such as public reporting of processing technology, and achieve the effect of resource utilization
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Embodiment 1
[0023] Take the effluent from the AP flooding production water settling tank of the Xingerzhong Experimental Station of the Fourth Oil Production Plant of Daqing Oilfield. The oil content is 106 mg / L, the suspended solid (SS) content is 156 mg / L, and the median diameter of oil droplets is 38 μm. Its pH is 9.6. Adjust its pH to 9 with dilute sulfuric acid, introduce the water in the pH adjustment tank into stirring tank 1, add 3.18mmol / L (moles / produced water volume) of magnesium sulfate (i.e. 3.18mmol / L magnesium ion), and stir Stir in tank 1 for 5 min. At this time, the pH of the produced water is 8.6, and the pH does not need to be further adjusted; The water in the mixing tank 3 is introduced into the stirring tank 3, and the aluminum sulfate (that is, 2.12mmol / L aluminum ion) of 1.06mmol / L (number of moles / produced water volume) is added, and the stirring reaction is carried out for 5min; after that, the water in the stirring tank 3 is introduced into the settling tank, st...
Embodiment 2
[0025] The produced water from the AP flooding production water settling tank of the Xingerzhong Experimental Station of the No. 4 Oil Production Plant of Daqing Oilfield was taken. The oil content was 380 mg / L, the suspended solid (SS) content was 556 mg / L, and the median diameter of oil droplets was 98 μm , its pH is 9.6, its pH is adjusted to 7 with dilute sulfuric acid, the water in the pH adjustment tank is introduced into stirring tank 1, the magnesium sulfate (being 38mmol / L magnesium ion of 38mmol / L (number of moles / production water volume)) ), stirring 10min, at this moment, the pH of produced water is 6.3; Add liquid caustic soda to adjust pH to 7; Stir for 10min; introduce the water in the stirring tank 2 into the stirring tank 3, add 15.2mmol / L (number of moles / volume of produced water) aluminum sulfate (that is, 30.4mmol / L aluminum ion), and stir for 10min; the water in the stirring tank 3 Introduce it into a settling tank and let it stand for 45 minutes. The oil ...
Embodiment 3
[0027]Take the produced water before the settling tank and the effluent water after the settling tank from the ASP flooding production water produced by the No. 4 Oil Production Plant of Daqing Oilfield Xingerzhong Test Station, and mix the two according to a certain ratio. The oil content is 218mg / L, and the suspended solids (SS) content It is 216mg / L, the median diameter of oil droplets is 42μm, and its pH is 9.6. Adjust its pH to 8 in the pH adjustment tank with dilute sulfuric acid; introduce the water in the pH adjustment tank into the stirring tank 1, add 10.9mmol / L (moles / produced water volume) of magnesium sulfate (i.e. 10.9mmol / L magnesium ions), stirring for 8min, at this time, the pH of the produced water is 7.3, and it is not necessary to adjust the pH; the outlet water in the stirring tank 1 is introduced into the stirring tank 2, and the humic acid of 650mg / L (quality / produced water volume) is added, and stirred for 8min; stirring The water from tank 2 is introdu...
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