CN116675385A - Air-float synergistic oil-water separation treatment device - Google Patents
Air-float synergistic oil-water separation treatment device Download PDFInfo
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- CN116675385A CN116675385A CN202310812363.4A CN202310812363A CN116675385A CN 116675385 A CN116675385 A CN 116675385A CN 202310812363 A CN202310812363 A CN 202310812363A CN 116675385 A CN116675385 A CN 116675385A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 172
- 238000000926 separation method Methods 0.000 title claims abstract description 67
- 238000011282 treatment Methods 0.000 title claims abstract description 37
- 230000002195 synergetic effect Effects 0.000 title claims description 43
- 239000007788 liquid Substances 0.000 claims abstract description 22
- 239000010865 sewage Substances 0.000 claims abstract description 21
- 238000005188 flotation Methods 0.000 claims description 24
- 239000003921 oil Substances 0.000 description 36
- 238000011065 in-situ storage Methods 0.000 description 11
- 238000005516 engineering process Methods 0.000 description 8
- 238000010992 reflux Methods 0.000 description 8
- 238000004062 sedimentation Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 238000007667 floating Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 239000010779 crude oil Substances 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 238000009434 installation Methods 0.000 description 4
- 239000008213 purified water Substances 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- XLYOFNOQVPJJNP-ZSJDYOACSA-N Heavy water Chemical compound [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000009977 dual effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 238000011284 combination treatment Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003129 oil well Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- -1 pre-diversion device Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention relates to the technical field of oilfield sewage treatment, in particular to an air floatation enhanced oil-water separation treatment device, which comprises a rotational flow air floatation oil-water separator, wherein a first water outlet is arranged on the rotational flow air floatation oil-water separator, the first water outlet is connected with a first water inlet pipe of an air floatation enhanced oil-water separation horizontal tank to form a U-shaped pipe structure, the rotational flow air floatation oil-water separator is communicated with the air floatation enhanced oil-water separation horizontal tank, a second water outlet of the air floatation enhanced oil-water separation horizontal tank is communicated with a sewage treatment system through a water outlet pipeline, a return pipe communicated with the air floatation enhanced oil-water separation horizontal tank and the rotational flow air floatation oil-water separator is arranged on the water outlet pipeline to form a structure for realizing circulation separation of liquid flowing out through the second water outlet through the return pipe, and an air outlet of the rotational flow air floatation oil-water separator and an air inlet of the air floatation enhanced oil-water separation horizontal tank are communicated through a pipeline to solve the problem of low efficiency of separation equipment in the prior art.
Description
Technical Field
The invention belongs to the technical field of oilfield sewage treatment, and particularly relates to an air floatation synergistic oil-water separation treatment device.
Background
With the continuous deep development of various large oil fields, the water content of the oil well is continuously increased, and the development and station building mode in the early stage of low water content is not suitable for the high-water-content oil production mode. For the ultra-high water content oil field with the increase of the remote block oil field or the produced liquid year by year, the oil production sewage needs to be conveyed in a centralized way in a long distance, and the problems of high energy consumption, high treatment cost, incapability of guaranteeing water quality and the like exist. In order to overcome the limitations of the pre-diversion facilities of the existing gathering, transportation and output liquid treatment system, an in-situ diversion treatment device of an oil field with high efficiency, small occupied area and low investment is needed. At present, "in-situ water diversion and in-situ reinjection" has become a main means for improving economic benefit of high-water-content oil fields, and especially, a short-process treatment technology for pre-diversion of short, small and fine oil fields has become an urgent need for simplifying the process, saving investment and reducing energy consumption and running cost of the high-water-content oil fields.
The prior pre-water separation equipment mainly comprises a hydrocyclone, a cavity barrel separator, an inclined tube pre-water separator, a three-phase separator, a multifunctional crude oil treatment combination device, a full-gravity balance oil-gas-water treatment integrated device and an integrated pre-water separator. Most of the current pre-water devices involve only one or a few technologies, and the goals of in-situ water diversion, in-situ treatment and in-situ reinjection cannot be achieved by using the pre-water devices alone.
The operation technology is known to be mainly two, namely a three-phase separator and pressure oil remover technology and an integrated short-flow on-site water diversion technology, wherein the two on-site water diversion technologies can meet the field process requirements, but the integrated short-flow on-site water diversion technology mainly has the defects of complex process and high maintenance cost, and the three-phase separation and oil remover technology mainly has the defects of long flow and unstable water quality. Therefore, the water quality is required to be designed according to the space in the station and the water quality requirement.
At present, three-phase separator equipment is generally adopted for pre-diversion in domestic oil fields, the oil content index of the separated sewage is higher, and a conventional sewage treatment system is required to be constructed in a matched manner, wherein the typical process flow comprises 'high-water-content produced liquid, pre-diversion device, oil removal tank, settling tank, air floatation, buffer tank, lift pump, filter, fine filter and water outlet'. The sewage treatment process flow is complex, the integration and skid-mounted are not realized, the occupied area is large, the investment is high, the process simplification requirement cannot be met, and the separated sewage is basically conveyed to a joint station for treatment, so that the targets of on-site water diversion, on-site treatment and on-site reinjection cannot be realized. In order to overcome the limitation of the pre-diversion facilities of the existing gathering and transportation and produced fluid treatment system, an in-situ diversion treatment device of the oil field with high treatment efficiency, small occupied area and low investment is needed.
Disclosure of Invention
Aiming at the situation, in order to overcome the defects of the prior art, the invention provides the air floatation synergy oil-water separation treatment device which solves the problem of low efficiency of oil-water separation equipment in the prior art.
The technical scheme is that the air floatation synergistic oil-water separation treatment device comprises a rotational flow air floatation oil-water separator, a first water outlet is formed in the rotational flow air floatation oil-water separator, the first water outlet is connected with a first water inlet pipe of an air floatation synergistic oil-water separation horizontal tank, a rotational flow air floatation oil-water separator is communicated with the air floatation synergistic oil-water separation horizontal tank and forms a U-shaped pipe structure, a second water outlet of the air floatation synergistic oil-water separation horizontal tank is communicated with a sewage treatment system through a water outlet pipeline, a backflow pipe communicated with the air floatation synergistic oil-water separation horizontal tank and the rotational flow air floatation oil-water separator is arranged on the water outlet pipeline, a structure for realizing circulation separation of liquid flowing out through the second water outlet through the backflow pipe is formed, and an air outlet of the rotational flow air floatation oil-water separator and an air inlet of the air floatation synergistic oil-water separation horizontal tank are communicated through a pipeline.
Preferably, the horizontal tank for air floatation synergy oil-water separation comprises a tank body, population for access personnel is arranged at two ends of the length direction of the tank body, a rectifying plate is arranged at one end, close to the water inlet pipe, of the tank body, an inclined plate group is arranged at the position, close to the rectifying plate, of the tank body, one end, far away from the rectifying plate, of the inclined plate group is provided with an oil chamber, one end, far away from the inclined plate group, of the inclined plate group is provided with a water chamber, an adjustable weir pipe is arranged in the water chamber, fixed onto the tank body, one end, far away from the tank body, of the adjustable weir pipe is communicated with one end, close to the oil chamber, of the inclined plate group through a second water inlet pipe, and a second water outlet is arranged on one side, far away from the oil chamber, of the water chamber.
Preferably, the first water inlet pipe is communicated with an adjustable weir pipe fixed with the tank body, the position, close to the adjustable weir pipe, on the tank body is connected with a blow-down device through an exhaust port, a sewage outlet is formed in the tank body, and the sewage outlet is multiple.
Preferably, the reflux pipe comprises branch pipes, a reflux port is arranged on the tank body and positioned between the rectifying plate and the sloping plate group, a liquid inlet is arranged on one side surface of the cyclone air-floating oil-water separator, which is far away from the air-floating synergistic oil-water separation horizontal tank, and two branch pipes are respectively communicated with the reflux port and the liquid inlet.
The invention has the beneficial effects that the reflux pipe is arranged, the effluent liquid of the air-flotation synergistic oil-water separation horizontal tank enters the cyclone cylinder through the reflux pipe, oil-water separation is realized under the dual actions of cyclone centrifugation and air flotation, the cyclone air-flotation oil-water separator and the air-flotation synergistic oil-water separation horizontal tank are connected in a U-shaped manner, a fixed liquid level is established by means of the balance principle of the U-shaped pipe, purified water is discharged from the U-shaped water outlet weir pipe, and a top slag layer is automatically collected and discharged from the central slag discharge pipe;
the cyclone air flotation oil-water separator and air flotation synergistic oil-water separation horizontal tank device has the advantages of small volume, convenient installation, high efficiency and large treatment capacity, and the air flotation synergistic reflux mode is adopted, so that the oil-water separation effect is good, and the index is stable; the cyclone air-float oil-water separator is internally provided with a diversion channel, a cyclone cylinder, a sedimentation cylinder, an oil-water cylinder box, and the functions of each part are clear and related, the structure is compact, the air-float synergistic oil-water separation horizontal tank is provided with a coarse-grain filter plate and an inclined plate sedimentation, the air-float separation is carried out, and the air-float synergy is realized in the tank by utilizing the produced gas in the multiple separation areas; the device can be used as a metering station, an oil collecting station or a combined station pre-dehydration device, so that crude oil is dehydrated in situ and treated and reinjected in situ, and the energy consumption for transportation and heating is reduced; the device can also be used as oil-containing sewage oil removal equipment to replace a natural sedimentation tank, and has a wider application range; compared with the conventional treatment equipment, the processing cost can be reduced by more than 50 percent. The workshop prefabricated combined skid-mounted device is small in occupied area and small in field installation workload, and can greatly shorten the construction period.
Drawings
FIG. 1 is a block diagram of an air-float synergistic oil-water separation treatment device of the invention;
the device comprises a 1 rotational flow air flotation oil-water separator, a 2 first water outlet, a 3 air flotation synergistic oil-water separation horizontal tank, a 4 first water inlet pipe, a 5 second water outlet, a 6 water outlet pipeline, a 7 sewage treatment system communication, an 8 backflow pipe, a 9 air inlet, a 10 pipeline, an 11 tank body, a 12 population, a 13 rectifying plate, a 14 sloping plate group, a 15 oil chamber, a 16 water chamber, a 17 adjustable weir pipe, 18 emptying equipment, a 19 sewage outlet, a 20 branch pipe, a 21 backflow port, a 22 liquid inlet, a 23 air outlet and a 24 air outlet.
Detailed Description
The following describes the embodiments of the present invention in further detail with reference to the drawings.
Embodiment one: according to the specification, the drawing shows that the air floatation synergistic oil-water separation treatment device comprises a cyclone air floatation oil-water separator 1, wherein the cyclone air floatation oil-water separator 1 is in the prior art, produced liquid enters a cyclone cylinder from the bottom of the cyclone cylinder along the tangential direction, moves upwards in a spiral rotation mode, rises upwards in a rotation mode to enter the upper part of the cyclone cylinder, under the action of centrifugal force, water with higher density is thrown to the wall surface of the outer wall of the cylinder, crude oil with lower density and oil-gas mixture are thrown to the outer wall of the inner cylinder by heavy water pressure, oil drops and bubbles are combined due to the fact that the density is lower than that of surrounding water, oil drops are floated through rising of the bubbles, the oil-gas mixture flows into a central cylinder after entering the upper part of the cylinder along the outer wall of the inner cylinder in a cyclone mode, and flows out of the device after liquid level control; the water thrown to the outer wall of the cyclone cylinder enters the air flotation separation cylinder and then flows downwards around the wall of the cyclone cylinder in a cyclone way, meanwhile, dissolved gas in the water plays roles of adsorption, coalescence and floating upwards, after the oil and the water are further subjected to sedimentation separation, purified water at the lower part enters the bottom water collecting cabin, then enters the purified water tank through the specially designed U-shaped communicating pipe through the water guide pipe, and flows out of the separator after being metered and liquid level controlled. Thereby achieving the separation effect of oil, gas and water phase. The cyclone air-float oil-water separator 1 is provided with a first water outlet 2, the first water outlet 2 is connected with a first water inlet pipe 4 of the air-float synergistic oil-water separation horizontal tank 3, the cyclone air-float oil-water separator 1 is communicated with the air-float synergistic oil-water separation horizontal tank 3 and forms a U-shaped pipe structure, and a fixed liquid level is established by means of a U-shaped pipe balance principle. The horizontal tank 3 for air floatation synergistic oil-water separation belongs to the prior art, purified sewage after separation treatment by the cyclone air floatation oil-water separator 1 enters the equipment, firstly, inflow water is rectified, coalesced and primarily filtered, coarse-grained filler layers are adopted, the radius of oil beads is increased, meanwhile, large-grain-size impurities are filtered, oil-water separation is carried out by an inclined plate sedimentation area, and separated dirty oil and purified sewage are respectively collected by an adjustable weir and are respectively conveyed into corresponding equipment by pipelines. The equipment has stable working condition and high automation degree, and is convenient to manage. And an air-entrapping reflux device is arranged in the horizontal tank, so that air floatation synergistic effect is realized, the equipment volume is reduced, and the running stability of the equipment is improved. The second water outlet 5 of the air-float synergistic oil-water separation horizontal tank 3 is communicated with a sewage treatment system 7 through a water outlet pipeline 6, a return pipe 8 communicated with the air-float synergistic oil-water separation horizontal tank 3 and the cyclone air-float oil-water separator 1 is arranged on the water outlet pipeline 6, a structure is formed that liquid flowing out from the second water outlet 5 is circularly separated through the return pipe 8, and an air outlet 23 of the cyclone air-float oil-water separator 1 and an air inlet 9 of the air-float synergistic oil-water separation horizontal tank 3 are communicated through a pipeline 10.
In an embodiment, according to the figure, the horizontal air-floating synergistic oil-water separation tank 3 comprises a tank body 11, wherein population 12 for access of maintenance personnel is arranged at two ends of the tank body 11 in the length direction, and population 12 is also arranged in the middle of the tank body 11. The rectifying plate 13 is arranged at one end of the tank 11, which is close to the water inlet pipe, the rectifying plate 13 belongs to the prior art, the inclined plate group 14 is arranged at the position of the tank 11, which is close to the rectifying plate 13, and the oil chamber 15 is arranged at one end of the inclined plate group 14, which is far away from the rectifying plate 13. The oil chamber 15 is provided with the hydroecium 16 far away from the one end of swash plate group 14, is provided with the adjustable weir pipe 17 that is fixed to the jar body 11 in the hydroecium 16, and the one end that adjustable weir pipe 17 kept away from jar body 11 is through second inlet tube and swash plate group 14 near the one end intercommunication of oil chamber 15, and the hydroecium 16 is provided with second delivery port 5 far away from the side of oil chamber 15. The first water inlet pipe 4 is communicated with an adjustable weir pipe 17 fixed with the tank 11, the position, close to the adjustable weir pipe 17, on the tank 11 is connected with a blow-down device 18 through an exhaust port 24, the tank 11 is provided with a plurality of blow-down ports 19, and the blow-down ports 19 are respectively arranged below the oil chamber 15, the water chamber 16, the inclined plate group 14 and the vicinity of the rectifying plate 13. The return pipe 8 comprises branch pipes 20, a return port 21 is arranged on the tank body 11 and positioned between the rectifying plate 13 and the inclined plate group 14, a liquid inlet 22 is arranged on one side surface of the cyclone air-floating oil-water separator 1, which is far away from the air-floating synergistic oil-water separation horizontal tank 3, and two branch pipes 20 are respectively communicated with the return port 21 and the liquid inlet 22.
According to the invention, through arranging the return pipe, effluent liquid of the air-floatation synergistic oil-water separation horizontal tank enters the cyclone cylinder through the return pipe, oil-water separation is realized under the dual actions of cyclone centrifugation and air floatation, the cyclone air-floatation oil-water separator and the air-floatation synergistic oil-water separation horizontal tank are connected in a U shape, a fixed liquid level is established by means of the balance principle of the U-shaped pipe, purified water is discharged by the U-shaped water outlet weir pipe, and a top slag layer is automatically collected and discharged by the central slag discharge pipe; the cyclone air flotation oil-water separator and air flotation synergistic oil-water separation horizontal tank device has the advantages of small volume, convenient installation, high efficiency and large treatment capacity, and the air flotation synergistic reflux mode is adopted, so that the oil-water separation effect is good, and the index is stable; the cyclone air-float oil-water separator is internally provided with a diversion channel, a cyclone cylinder, a sedimentation cylinder, an oil-water cylinder box, and the functions of each part are clear and related, the structure is compact, the air-float synergistic oil-water separation horizontal tank is provided with a coarse-grain filter plate and an inclined plate sedimentation, the air-float separation is carried out, and the air-float synergy is realized in the tank by utilizing the produced gas in the multiple separation areas; the device can be used as a metering station, an oil collecting station or a combined station pre-dehydration device, so that crude oil is dehydrated in situ and treated and reinjected in situ, and the energy consumption for transportation and heating is reduced; the device can also be used as oil-containing sewage oil removal equipment to replace a natural sedimentation tank, and has a wider application range; compared with the conventional treatment equipment, the processing cost can be reduced by more than 50 percent. The workshop prefabricated combined skid-mounted device is small in occupied area and small in field installation workload, and can greatly shorten the construction period.
The present invention has been described in detail by way of specific embodiments and examples, but these should not be construed as limiting the invention. Many variations and modifications may be made by one skilled in the art without departing from the principles of the invention, which is also considered to be within the scope of the invention.
Claims (4)
1. The air-flotation synergistic oil-water separation treatment device comprises a cyclone air-flotation oil-water separator (1), and is characterized in that a first water outlet (2) is formed in the cyclone air-flotation oil-water separator (1), the first water outlet (2) is connected with a first water inlet pipe (4) of an air-flotation synergistic oil-water separation horizontal tank (3), the cyclone air-flotation oil-water separator (1) is communicated with the air-flotation synergistic oil-water separation horizontal tank (3) and forms a U-shaped pipe structure, a second water outlet (5) of the air-flotation synergistic oil-water separation horizontal tank (3) is communicated with a sewage treatment system (7) through a water outlet pipeline (6), a backflow pipe (8) communicated with the air-flotation synergistic oil-water separation horizontal tank (3) and the cyclone air-flotation oil-water separator (1) is arranged on the water outlet pipeline (6), a structure for realizing circulation separation of liquid flowing out through the second water outlet (5) through the backflow pipe (8) is formed, and an air outlet (23) of the cyclone air-flotation oil-water separator (1) and an air inlet (9) of the air-flotation synergistic oil-water separation horizontal tank (3) are communicated through a pipeline (10).
2. The air-floatation synergistic oil-water separation treatment device according to claim 1, wherein the air-floatation synergistic oil-water separation horizontal tank (3) comprises a tank body (11), population (12) used for overhauling personnel to enter is arranged at two ends of the length direction of the tank body (11), a rectifying plate (13) is arranged at one end, close to a water inlet pipe, of the tank body (11), an inclined plate group (14) is arranged at the position, close to the rectifying plate (13), of the tank body (11), an oil chamber (15) is arranged at one end, far away from the rectifying plate (13), of the inclined plate group (14), a water chamber (16) is arranged at one end, far away from the inclined plate group (14), of the oil chamber (15), an adjustable weir pipe (17) is arranged in the water chamber (16), fixed on the tank body (11), one end, close to the oil chamber (15), of the inclined plate group (14) is communicated with one end, close to the oil chamber (15), of the water chamber (16) is provided with a second water outlet (5).
3. The air-floatation synergistic oil-water separation treatment device according to claim 2, wherein the first water inlet pipe (4) is communicated with an adjustable weir pipe (17) fixed with the tank body (11), the position, close to the adjustable weir pipe (17), on the tank body (11) is connected with a blow-down device (18) through an exhaust port (24), a sewage outlet (19) is arranged on the tank body (11), and the sewage outlet (19) is multiple.
4. The air floatation synergistic oil-water separation treatment device according to claim 2, wherein the return pipe (8) comprises branch pipes (20), a return port (21) is arranged on the tank body (11) and positioned between the rectifying plate (13) and the sloping plate group (14), a liquid inlet (22) is arranged on one side surface of the cyclone air floatation oil-water separator (1) away from the air floatation synergistic oil-water separation horizontal tank (3), and the branch pipes (20) are two and are respectively communicated with the return port (21) and the liquid inlet (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310812363.4A CN116675385A (en) | 2023-07-04 | 2023-07-04 | Air-float synergistic oil-water separation treatment device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310812363.4A CN116675385A (en) | 2023-07-04 | 2023-07-04 | Air-float synergistic oil-water separation treatment device |
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| CN116675385A true CN116675385A (en) | 2023-09-01 |
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| CN202310812363.4A Pending CN116675385A (en) | 2023-07-04 | 2023-07-04 | Air-float synergistic oil-water separation treatment device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117298657A (en) * | 2023-11-30 | 2023-12-29 | 中国石油大学(华东) | Oil-gas-water separation system and method for high-water-content produced liquid of ocean platform |
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2023
- 2023-07-04 CN CN202310812363.4A patent/CN116675385A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117298657A (en) * | 2023-11-30 | 2023-12-29 | 中国石油大学(华东) | Oil-gas-water separation system and method for high-water-content produced liquid of ocean platform |
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