A method and device for controlling the viscosity loss of mixed polymers in oil extraction wastewater
A technology for oil production sewage and viscosity loss, applied in the direction of oxidized water/sewage treatment, etc., can solve the problem of large solution viscosity loss, achieve the effects of increasing contact area, reasonable reuse, and ensuring accuracy
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Embodiment 1
[0041] The method and device for controlling the viscosity loss of the mixed polymer solution of the oil extraction wastewater of the present invention were used for confidentiality tests. The polymer flooding oil extraction wastewater was used as the raw water, and the flow rate was 12m. 3 / h Pump into the vertical water collection tank 1, and carry out the first to fifth steps of the present invention. Through the first stage test of the technical scheme of the present invention, the influent flow rate is 12m 3 / h, the oxygen exposure pressure is 0.15MPa, and the oxygen exposure time is 7 seconds, the optimal oxygen content of the sewage system is 6.50mg / L, and the fitting establishes the corresponding inlet water flow and oxygen exposure pressure when the optimal oxygen content is reached. The relationship between the oxygen exposure time is:
[0042] Q=0.21×32×3600×10 6 ×k×P / (8.314×298×D O ×t)
[0043] In the formula: Q——influent flow, m 3 / h;
[0044] P-oxygen exposure pressure,...
Embodiment 2
[0056] Use polymer flooding oil production wastewater as raw water, with a flow rate of 25m 3 / h Pump into the vertical water collection tank 1, and carry out the first to fifth steps of the present invention. Through the first stage test of the technical scheme of the present invention, the influent flow rate is 25m 3 / h, the oxygen exposure pressure is 0.22MPa, and the oxygen exposure time is 15 seconds, the optimal oxygen content of the sewage system is 6.48mg / L, and the fitting is established when the optimal oxygen content is reached, the corresponding inlet water flow and oxygen exposure pressure, The relationship between the oxygen exposure time, the relationship also meets the description of embodiment 1, wherein in this embodiment D O =6.48mg / L.
[0057] Using the optimal oxygen content of the sewage system determined in the first stage above to be 6.48mg / L as a guide, the vertical water collection tank with an inlet flow of 25m 3 / h is pumped into the oil production waste...
Embodiment 3
[0062] Use polymer flooding oil production wastewater as raw water, with a flow rate of 18m 3 / h Pump into the vertical collecting tank 1, and carry out the first to fifth steps of the present invention. Through the first stage test of the technical scheme of the present invention, the influent flow rate is 18m 3 / h, the oxygen exposure pressure is 0.18MPa, and the oxygen exposure time is 10 seconds, the optimal oxygen content of the sewage system is 6.70mg / L, and the fitting is established when the optimal oxygen content is reached, the corresponding inlet water flow and oxygen exposure pressure, The relationship between the oxygen exposure time, the relationship also meets the description of embodiment 1, wherein in this embodiment D O =6.70mg / L.
[0063] Using the optimal oxygen content of the sewage system determined in the first stage above to be 6.70mg / L as a guide, the vertical water collection tank with an inlet flow of 18m 3 / h is pumped into the oil production wastewater,...
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