A kind of recycling treatment method of oil refinery wastewater
A technology for oil refining wastewater and treatment methods, which is applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. Treatment and reuse, stable operation effect
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Embodiment 1
[0013] Using the refinery wastewater reuse treatment method of the present invention, the process flow is oil separation-flotation-SBR-OMBR, and the specific test conditions are as follows:
[0014] The effluent from the oil separation and flotation of the sewage treatment plant of the upper refinery is treated with a 10LSBR small test device. The main operating conditions are: wastewater temperature 25°C, pH 7.0, sludge concentration (MLSS) 3500mg / L, hydraulic retention time 15h, The sludge residence time is 25 days, the SBR operation cycle is 12 hours, and the method is water intake-(aeration-stirring) repeated 3 times-sedimentation-decanting water, in which water intake is 1.0h per cycle, aeration (aerobic) / stirring (anaerobic) Oxygen) 8.0h, precipitation 2.0h, decanting 1.0h, the time ratio of aeration and stirring is 1:1.
[0015] The SBR effluent is treated with a 10LOMBR small-scale test device. The OMBR membrane is a 0.1m×0.5m triacetate fiber forward osmosis membrane ...
Embodiment 2
[0020] Using the method for treating oil refinery wastewater of the present invention, the technological process is oil separation-flotation-SBR-OMBR, and the above-mentioned wastewater is treated under optimized technological conditions.
[0021] In the present invention, the oil removal and suspended matter treatment effluent is treated with SBR. The operating conditions of SBR are: wastewater temperature 30°C, pH 7.0, sludge concentration (MLSS) 5000mg / L, hydraulic retention time (HRT) 20h, sludge retention time (SRT) 20d, volume load (organic load) 0.40kgCOD / (m 3 d) The dissolved oxygen in the aerobic process is 2.0mg / L, and the dissolved oxygen in the anaerobic process does not exceed 0.4mg / L. The SBR operation cycle is 20h, and the method is water intake-aeration-stirring (anaerobic)-sedimentation-decanting, Among them, water intake is 1.0h, aeration (aerobic) / stirring (anaerobic) is 17.0h, precipitation is 1.0h, decanting is 1.0h, and the time ratio of aeration and st...
Embodiment 3
[0026] Using the refinery wastewater treatment method of the present invention, the process flow is oil separation-flotation-SBR-OMBR, and the above-mentioned wastewater is treated under optimized process conditions. The main indicators of the influent and treated effluent are shown in Table 3.
[0027] In the present invention, the oil removal and suspended matter treatment effluent is treated with SBR. The operating conditions of SBR are: wastewater temperature 40°C, pH 6.5, sludge concentration (MLSS) 3000mg / L, hydraulic retention time (HRT) 15h, sludge retention time (SRT) 15d, volumetric load (organic load) 0.30kgCOD / (m 3d) The dissolved oxygen in the aerobic process is 4.0mg / L, and the dissolved oxygen in the anaerobic process does not exceed 0.3mg / L. The SBR operation cycle is 12h, and the method is water intake-aeration-stirring (anaerobic)-sedimentation-decanting, Among them, water is fed for 1.0h, aeration (aerobic) / stirring (anaerobic) is 10.0h, sedimentation is 0...
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