Method for deeper treatment and reuse of oil production waste water in oil field by membrane separation
A technology for oil extraction wastewater and advanced treatment, which is applied in infiltration/dialysis water/sewage treatment and other directions. Problems such as poor oil-water separation effect, to achieve good social benefits, reduce wastewater discharge, and low operating costs
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Embodiment 1
[0011] Accurately measure 200 liters of oil production wastewater from the oil field and add it to the material tank. Under the operating pressure of 0.4 MPa and operating temperature of 45 degrees Celsius, microfiltration operation is carried out; the concentrated liquid is collected and transported back to the joint station for oil recovery, and the filtrate enters the subsequent nanofiltration Membrane separation system; the nanofiltration operating system performs nanofiltration operation at an operating pressure of 1.5 MPa and an operating temperature of 40 degrees Celsius; the filtrate is sent to the pressurization station for use as reinjection water or polymer configuration water.
Embodiment 2
[0013] Accurately measure 200 liters of oil production wastewater from the oil field and add it to the material tank. Under the operating pressure of 1.5 MPa and operating temperature of 50 degrees Celsius, microfiltration operation is carried out; the concentrated liquid is collected and transported back to the joint station for oil recovery, and the filtrate enters the subsequent nanofiltration Membrane separation system; the nanofiltration operating system performs nanofiltration operation at an operating pressure of 2.0 MPa and an operating temperature of 35 degrees Celsius; the filtrate is sent to the pressurization station for use as reinjection water or polymer configuration water.
Embodiment 3
[0015] Accurately measure 200 liters of oil production wastewater from the oil field and add it to the material tank. Under the operating pressure of 0.5 MPa and operating temperature of 40 degrees Celsius, microfiltration operation is carried out; the concentrated liquid is collected and transported back to the joint station for oil recovery, and the filtrate enters the subsequent nanofiltration Membrane separation system; the nanofiltration operating system performs nanofiltration operation at an operating pressure of 3.0 MPa and an operating temperature of 30 degrees Celsius; the filtrate is sent to the pressurization station for use as reinjection water or polymer configuration water.
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