Method and device for processing polymer-contained waste liquid and fracturing flow-back fluid
A fracturing flowback fluid and treatment method technology, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc. Reuse and re-injection, adverse effects of dosing agents, etc., to achieve the effect of convenient equipment processing and transportation, realizing waste liquid resource utilization, and saving transportation
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Embodiment 1
[0035] like figure 1 As shown, it is a schematic diagram of the treatment device for polymer-containing waste fluid and fracturing flowback fluid provided in this example. As can be seen from the figure, the treatment device consists of a lift pump 1, an ultrasonic generator 9, an ozone generator 8, a sewage reaction tank 2, a multi-media activated carbon device 3, an aeration device 7, a secondary lift pump 4, and a pipeline mixing device 5, dosing device 11 and coagulation-filtration-precipitation integrated device 6, the sewage reaction tank 2, multi-media activated carbon device 3 and coagulation-filtration-precipitation integrated device 6 are connected in sequence through pipelines, and the The ultrasonic generator 9 is placed next to the sewage reaction tank 2, the ozone generator 8 is placed in the sewage reaction tank 2, the carrier activated carbon catalyst is fixed in the multi-media activated carbon device 3, and the aeration device 7 is placed in the At the botto...
Embodiment 2
[0037] The processing device is as described in Example 1.
[0038] Fracturing fluid treatment volume 1m 3 / h, influent water quality: water temperature 48°C, pH=8.6, oil content 532mg / L, COD 4562mg / L, suspended matter: 611mg / L. The treatment method is as follows: the ultrasonic frequency in the sewage reaction tank is controlled at 23kHz, the dosage of ozone is 12mg / L, and the residence time is 30min; the dosage of the catalyst (copper-loaded activated carbon) in the multi-media activated carbon device is 0.6m 3 , the aeration is controlled at an air-to-water ratio of 32:1. Coagulation-sedimentation-filtration integrated device front-end agent dosage is: organic polymer flocculant (polymer polyacrylamide) is 80mg / L, water purifier (OTC-A) is 65mg / L, coagulant aid ( Cationic polyacrylamide) is 0.5mg / L. The working time of the device is 52min. The effluent reaches the standard of "Methods for Performance Evaluation of Water-Based Fracturing Fluids" (SY / T5107-2005).
[0039...
Embodiment 3
[0044] The processing device is as described in Example 1.
[0045] Polymerized sewage treatment capacity 1m 3 / h, influent water quality: water temperature 45°C, pH=8.9, oil content 567mg / L, COD 5279mg / L, suspended matter: 598mg / L. The specific treatment method is that the ultrasonic frequency in the sewage reaction tank is controlled at 25kHz, the dosage of ozone is 14.5mg / L, and the residence time is 30min; the dosage of cobalt-loaded activated carbon in the multi-media activated carbon device is 0.65m 3 , Aeration is controlled at an air-to-water ratio of 35:1. Coagulation-sedimentation-filtration integrated device front-end agent dosage is: organic polymer flocculant (acrylamide and dimethylaminoethyl methacrylate copolymer) is 75mg / L, water purifier (OTC-B) is 55mg / L, coagulant aid (anionic polyacrylamide) is 1mg / L. The working time of the device is 48min. The effluent meets the standards of SYT 5329-2012 Recommended Indexes and Analysis Methods for Injection Water Q...
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