Treating technology and treating system for oil sand oil exploitation sewage
A technology for exploiting sewage and processing technology, which is applied in the directions of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc., and can solve the problem that ground facilities cannot operate normally, affecting the safe production of oil sands and oil, formation Blockage hazards and other issues
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Embodiment 1
[0039] The composition of oil sand oil production wastewater with weak alkalinity is shown in Table 1, and Table 1 is the composition of oil sand oil production wastewater. Oil sand oil mining waste water first enters homogeneous tank 1, then add 50-500ppm hydrochloric acid to adjust the pH of wastewater to 6.5-7.5, add 20-100ppm quaternary ammonium salt demulsifier to convert the emulsified oil into suspension oil, the working temperature is 60°C. The homogenized waste water is hydraulically retained in the air flotation degreasing device 2 for 40 minutes, and the working temperature is 40°C. The effluent after air flotation and oil removal treatment enters the flocculation air flotation device 3, and 30-80mg / L polyaluminum chloride-based inorganic polymer flocculant and 3-20mg / L organic polymer flocculant are added respectively, and the hydraulic retention time is 10 minutes .
[0040] The flocculated gas floats out of the water and enters the centrifuge 4 for centrifugati...
Embodiment 2
[0044] The acidified wastewater with strong acidity first enters the homogeneous tank 1, adding 200-1000ppm of common alkali to adjust the pH of the wastewater to 6.5-7.5, adding 20-100ppm of quaternary ammonium salt demulsifier to convert the emulsified oil into suspended oil, and the working temperature is 30°C. The homogenized waste water is hydraulically retained in the air flotation degreasing device 2 for 50 minutes, and the working temperature is 30°C. The air flotation degreasing water enters the flocculation air flotation device 3, and adds 30-80 mg / L polyferric silicate inorganic polymer flocculant and 3-20 mg / L organic polymer flocculant respectively, and the hydraulic retention time is 10 minutes.
[0045] The flocculation gas flotation effluent enters the decanter centrifuge 4 for centrifugation, and the solid waste generated by centrifugation is collected and recycled for making CWS additives, and the treated effluent is used for oil reservoir reinjection water. ...
Embodiment 3
[0047] The weakly alkaline waste liquid first enters the homogeneous tank 1, adding 50-500ppm of common acid to adjust the pH of the wastewater to 6.5-7.5, adding 20-100ppm of quaternary ammonium salt demulsifier to convert the emulsified oil into suspended oil, and work The temperature is 10°C. The homogenized waste water is hydraulically retained in the air flotation degreasing device 2 for 50 minutes, and the working temperature is 20°C. The air flotation degreasing water enters the flocculation air flotation device 3, and adds 30-80 mg / L polyferric silicate inorganic polymer flocculant and 3-20 mg / L organic polymer flocculant respectively, and the hydraulic retention time is 5 minutes. The flocculation gas flotation effluent enters centrifuge 4 for centrifugation, and the solid waste generated by centrifugation is collected and recycled to make CWS additives, and the effluent after centrifugation is used as oil layer reinjection water. The oil content of oil layer reinjec...
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