CN111422938A - Cavitation air flotation three-phase separation system - Google Patents
Cavitation air flotation three-phase separation system Download PDFInfo
- Publication number
- CN111422938A CN111422938A CN202010202635.5A CN202010202635A CN111422938A CN 111422938 A CN111422938 A CN 111422938A CN 202010202635 A CN202010202635 A CN 202010202635A CN 111422938 A CN111422938 A CN 111422938A
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- oil
- pipe
- separator body
- separator
- air flotation
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- 238000005188 flotation Methods 0.000 title claims abstract description 43
- 238000005191 phase separation Methods 0.000 title claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 238000007667 floating Methods 0.000 claims abstract description 42
- 238000000926 separation method Methods 0.000 claims abstract description 28
- 239000002893 slag Substances 0.000 claims abstract description 20
- 239000010802 sludge Substances 0.000 claims description 30
- 238000005086 pumping Methods 0.000 claims description 26
- 239000003129 oil well Substances 0.000 claims description 16
- 239000013049 sediment Substances 0.000 claims description 3
- 238000000638 solvent extraction Methods 0.000 claims 1
- 239000010865 sewage Substances 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 7
- 238000005192 partition Methods 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 description 9
- 238000007789 sealing Methods 0.000 description 6
- 238000007599 discharging Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000007790 scraping Methods 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 235000015110 jellies Nutrition 0.000 description 2
- 239000008274 jelly Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000005273 aeration Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
Classifications
-
- 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
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/204—Keeping clear the surface of open water from oil spills
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Removal Of Floating Material (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention relates to a cavitation air flotation three-phase separation system, which comprises a cavitation air flotation machine, a three-phase separator and an air flotation system water outlet pipeline, wherein the three-phase separator comprises a separator body with an opening at the top and a hollow inner part and a supporting device; a plurality of floating oil observation pipes are arranged on the outer side of the separator body, an oil discharge pipe is arranged on each floating oil observation pipe, and an oil discharge valve is arranged on each oil discharge pipe; the inside of separator body is provided with the oil removal board, and the oil removal board separates the separation oil removal district and deoiling drainage area with the inside partition of separator body, and the slag inlet pipe is linked together with the separator oil removal district, and the drain pipe is linked together with the drainage area that deoils, and the drain pipe is linked together with air supporting system outlet conduit. The invention aims to solve the problem that floating oil cannot be thoroughly removed from the whole disposal system in the use process of cavitation air floatation, and simultaneously reduce the flow of sewage entering a mud storage tank through an air floatation machine.
Description
Technical Field
The invention relates to the technical field of sewage treatment, in particular to a cavitation air flotation three-phase separation system.
Background
The cavitation air floating machine is a sewage treatment equipment mainly used for removing grease, jelly and suspended solid in industrial or urban sewage. A three-phase mixed system of water, gas and scum is formed by mainly utilizing a large amount of generated micro-bubbles, and after the bubbles are adhered to particles, flocs with apparent density smaller than that of water are formed and float to the water surface to form a scum layer to be scraped. When the cavitation air floatation works, a negative pressure area exists at the bottom of the air floatation tank, so that the wastewater at the bottom of the tank flows back to the aeration section, then returns to the air floatation section, is fully aerated, and 30-50% of the wastewater flows back. In the slag scraping and discharging device, under the action of a slag scraping machine and a traction chain, a large amount of foam and low-density flocculating constituents are gathered at a slag discharging port, and scum is discharged in a spiral propelling mode.
In the using process, dosing flocculation and air flotation are often combined for use, the coagulant coagulates impurities in water and plays a role in demulsification, and finely dispersed oil and emulsified oil can enter a sludge storage tank together with scum, jelly and surface sewage from a residue discharge port. During the sludge deposition and pressing process, a part of the floating oil is returned to the disposal system through the sludge clear liquid and is not completely removed from the treatment system. On the other hand, the air flotation machine can discharge a considerable amount of wastewater through slag scraping and discharging, and excessive sewage enters the sludge treatment system to increase the sludge treatment pressure and weaken the treatment effect.
In the actual operation of the air flotation machine, about 4% of sewage can be scraped along with the air flotation scraper blade every day and directly enters a subsequent sludge storage tank, and the part of sewage enters the sludge storage tank and returns to a primary sewage collection tank without being treated by a subsequent process. In contrast, the front-end process treatment of this portion of water is a waste of resources, and the water returned to the initial collection tank is relatively dirty in the form of sludge filtration or sludge clear liquid overflow in the later period, and the sludge disposal pressure is increased if the amount of water is large.
Disclosure of Invention
The invention aims to provide a cavitation air flotation three-phase separation system, which aims to solve the problem that floating oil cannot be thoroughly removed from the whole disposal system in the cavitation air flotation use process and simultaneously reduce the sewage flow entering a sludge storage tank through an air flotation machine.
The above object of the present invention is achieved by the following technical solutions:
a cavitation air flotation three-phase separation system comprises a cavitation air flotation machine, a three-phase separator and an air flotation system water outlet pipeline, wherein the air flotation system water outlet pipeline is communicated with a water outlet of the cavitation air flotation machine, the three-phase separator comprises a separator body with a hollow top opening and a supporting device for supporting the separator body, a slag inlet pipe and a water outlet pipe which are used for communicating the inside of the separator body with a slag outlet of the cavitation air flotation machine are arranged on the separator body, and a sludge discharge pipe and a control piece for controlling the opening and closing of the sludge discharge pipe are arranged at the bottom end of the separator body; the outer side of the separator body is provided with a plurality of transparent floating oil observation pipes which are arranged at intervals along the height direction of the separator body, the floating oil observation pipes are communicated with the inside of the separator body, the floating oil observation pipes are all positioned below the slag inlet pipe, one end of each floating oil observation pipe, which is far away from the separator body, is provided with an oil discharge pipe, and the oil discharge pipe is provided with an oil discharge valve which is opened or closed by the oil discharge pipe; the inside of separator body is provided with the oil removal board of vertical setting, leave the distance between the bottom of oil removal board and the bottom plate of separator body, the oil removal board separates the separation oil removal district and the drainage area that deoils that sets up side by side with the inside partition discharge of separator body, it is linked together with separator oil removal district to advance the sediment pipe, the drain pipe is linked together with the drainage area that deoils, the one end that the separator body was kept away from to the drain pipe is linked together with air supporting system outlet conduit.
By adopting the technical scheme, the residue discharged from the residue discharge port of the cavitation air flotation machine is sent into the separator body of the three-phase separator through the residue inlet pipe, the residue is separated into oil, water and residue in the separator body, when the thickness bottom end of the floating oil reaches a set position, the oil discharge pipe is opened, the floating oil is separated from the separator body through the oil discharge pipe, and in the standing process, when the liquid level reaches the position of the water discharge pipe, the water in the separator body is discharged through the water discharge pipe; when the residue is discharged, the sludge discharge pipe is opened through the control part, and the residue is discharged out of the three-phase separator through the sludge discharge pipe. The residue discharged from the cavitation air flotation machine is treated by a three-phase separator, so that the floating oil in the residue is removed, and the flow of sewage entering a mud storage tank through the air flotation machine is reduced.
The invention is further configured to: the oil pumping device is arranged on the oil separation plate and comprises an oil well pump, an oil pumping pipe and an oil delivery pipe, the oil pumping pipe is communicated with an oil inlet of the oil well pump, the oil delivery pipe is communicated with an oil outlet of the oil well pump, the oil pumping pipe is positioned inside the oil removing and water draining area, an oil inlet end of the oil pumping pipe is positioned below the height of the water draining pipe, and an oil outlet end of the oil delivery pipe is communicated with the separated oil separation area.
Through adopting above-mentioned technical scheme, when appearing the oil slick in the drainage zone of deoiling, and when the oil pumping pipe stretched into the liquid level inside of oil slick, start the oil-well pump, take out oil from the drainage zone of deoiling until there is not the oil slick on the surface of water of drainage zone of deoiling.
The invention is further configured to: the oil pumping pipe is a hose, and the oil inlet end of the oil pumping pipe is provided with a floater capable of floating on the oil surface.
By adopting the technical scheme, the liquid inlet end of the oil pumping pipe is always positioned below the liquid level of the floating oil when oil pumping is carried out.
The invention is further configured to: and a water baffle which is obliquely arranged is arranged in the separation oil separation area below the oil outlet end of the oil delivery pipe.
Through adopting above-mentioned technical scheme, slow down the speed that the oil of taking out from the drainage zone of deoiling falls into the separation and separates the inside of oil district to the reduction is to the stirring of the inside liquid of separation and oil district, guarantees the effect of the separation of stewing.
The invention is further configured to: the bottom plate of the separator body is of a cone hopper structure.
Through adopting above-mentioned technical scheme, set up to the awl structure of fighting through the bottom with the separator body to the residue of being convenient for assembles mud pipe department and discharges.
The invention is further configured to: and the floating oil observation pipes are respectively provided with a control valve.
Through adopting above-mentioned technical scheme, can select different oil slick observation pipes to carry out the oil extraction according to the thickness of actual oil slick and the height that oil slick was located.
In conclusion, the beneficial technical effects of the invention are as follows:
1. treating the residue discharged from the cavitation air flotation machine through a three-phase separator, removing floating oil in the residue, and simultaneously reducing the flow of sewage entering a mud storage tank through the air flotation machine;
2. by arranging the oil pumping device, the content of oil in water discharged from the water discharge pipe can be ensured.
Drawings
FIG. 1 is a schematic structural view of example 1;
FIG. 2 is a cross-sectional view of a three-phase separator;
FIG. 3 is a schematic structural view of example 2;
fig. 4 is a schematic structural diagram of the oil pumping device.
In the figure, 1, a cavitation air flotation machine; 2. a three-phase separator; 21. a separator body; 22. supporting legs; 23. a slag inlet pipe; 24. a drain pipe; 25. a sludge discharge pipe; 251. a mud valve; 26. an oil removal plate; 27. separating the oil separating area; 28. a deoiling and draining area; 29. a floating oil observation pipe; 291. a control valve; 210. an oil discharge pipe; 2101. a communicating pipe; 2102. an oil discharge valve; 3. an outlet pipeline of the air floatation system; 4. a water baffle; 5. an oil pumping device; 51. an oil well pump; 52. an oil pumping pipe; 521. a float; 53. and (5) feeding an oil pipe.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
Example 1:
referring to fig. 1 and 2, the cavitation air flotation three-phase separation system disclosed by the present invention comprises a cavitation air flotation machine 1, a three-phase separator 2 and an air flotation system water outlet pipeline 3, wherein the air flotation system water outlet pipeline 3 is communicated with a water outlet of the cavitation air flotation machine 1. The water treated by the cavitation air flotation machine 1 is sent into an air flotation system water outlet pipeline 3 through a water outlet of the cavitation air flotation machine 1 and flows out.
The three-phase separator 2 comprises a separator body 21 with an opening at the top and a hollow inside, and the separator body 21 is of a rectangular body structure. The four corners of the bottom end of the separator body 21 are respectively provided with a plurality of supporting legs 22, the supporting legs 22 are vertically arranged, and the tops of the supporting legs 22 are fixedly connected with the separator body 21 in a welding mode. The bottom end of the separator body 21 is spaced from the ground by the support legs 22.
A slag inlet pipe 23 and a water outlet pipe 24 which are communicated with the inner space of the separator body 21 are respectively arranged on a group of side walls opposite to the separator body 21, one end of the slag inlet pipe 23 is fixedly welded with the separator body 21, the other end of the slag inlet pipe is communicated with a slag outlet of the cavitation air flotation machine 1, and the slag inlet pipe 23 is fixedly connected with the cavitation air flotation machine 1. One end of the water discharge pipe 24 is welded and fixed with the separator body 21, the other end of the water discharge pipe is communicated with the water outlet pipeline 3 of the air floatation system, and the water discharge pipe 24 is fixedly connected with the water outlet pipeline 3 of the air floatation system. The height of the water outlet pipeline 3 of the air floatation system is lower than that of the water outlet pipe 24.
A sludge discharge pipe 25 which is vertically downward is arranged at the bottom end of the separator body 21, and the sludge discharge pipe 25 is communicated with the inside of the separator body 21. The sludge discharge pipe 25 and the separator body 21 are welded and fixed. A sludge discharge valve 251 is arranged on the sludge discharge pipe 25, and the opening and the closing of the sludge discharge pipe 25 are controlled by the sludge discharge valve 251. The feeding end of the mud valve 251 is fixedly connected with the mud pipe 25 in a sealing way.
An oil separation plate 26 which is vertically arranged is arranged inside the separator body 21, and the oil separation plate 26 and the side wall of the separator body 21 are welded and fixed. The bottom end of the oil baffle 26 is spaced from the bottom plate of the separator body 21. Thereby make the inside of separator body 21 form the separation oil interceptor 27 and the drain region 28 of deoiling that sets up side by side through the oil interceptor 26 of vertical setting, wherein advance sediment pipe 23 and separate oil interceptor 27 and be linked together, drain pipe 24 is linked together with the inside of drain region 28 of deoiling.
A plurality of floating oil observation pipes 29 which are arranged along the height direction of the separator body 21 at intervals are arranged on the side wall of the separator body 21 and below the slag inlet pipe 23, and the floating oil observation pipes 29 are transparent pipes. The floating oil observation tube 29 communicates with the inside of the separation oil-separating region 27 inside the separator body 21. The floating oil observation pipe 29 is fixedly connected with the separator body 21 in a sealing way. A section of the floating oil observation pipe 29 far away from the separator body 21 is respectively fixed with a control valve 291, and the liquid inlet end of the control valve 291 is fixedly connected with the floating oil observation pipe 29 in a sealing manner. An oil discharge pipe 210 which is vertically arranged is arranged outside the separator body 21, the oil discharge pipe 210 is arranged outside one end of the floating oil observation pipe 29 which is far away from the separator body 21, a communicating pipe 2101 which is communicated with the liquid discharge end of a control valve 291 on the floating oil observation pipe 29 is respectively arranged at the position where the oil discharge pipe 210 is opposite to the floating oil observation pipe 29, and the communicating pipe 2101 and the oil discharge pipe 210 are integrally formed.
One end of the oil drain pipe 210 is open and the other end is closed, the closed end of the oil drain pipe 210 is located above, and the open end of the oil drain pipe 210 faces downward. An oil discharge valve 2102 is arranged at the bottom end of the oil discharge pipe 210, and the oil inlet end of the oil discharge valve 2102 is fixedly connected with the oil discharge pipe 210 in a sealing mode.
When the oil-water-slag separation is carried out on the residues, firstly, water is injected into the separator body 21 through the opening at the top end of the separator body 21, the water surface is higher than the bottom end face of the oil separating plate 26, the residues in the cavitation air flotation machine 1 are sent into the oil separating area 27 inside the separator body 21 through the residue inlet pipe 23 and are kept still, the residues entering the oil separating area 27 are kept still for a long time, the waste residues sink to the bottom of the water, the oil in the residues floats on the water surface, and therefore the oil-water-slag separation is carried out.
The floating oil on the water surface in the separation oil separation zone 27 is thickened gradually after long-time standing separation, the floating oil thickness can be observed through the floating oil observation pipes 29 arranged at a plurality of different heights outside the separator body 21, and when the position of the bottom end of the floating oil reaches a set position, the floating oil is discharged from the separation oil separation zone 27 inside the separator body 21 through the floating oil observation pipes 29 and the oil discharge pipe 210. The floating oil can be recovered and treated in a mode of externally connecting a tonnage box.
When the water level in the deoiling drain area 28 reaches the position of the drain pipe 24, the water flows into the water outlet pipeline 3 of the air floatation system through the drain pipe 24 and is discharged.
When the residue is treated, the sludge discharge valve 251 is opened and the residue flows out through the sludge discharge pipe 25.
In order to facilitate the outflow of the sludge from the sludge discharge pipe 25. The bottom plate of the separator body 21 is a cone bucket structure with the cross-sectional area gradually decreasing from top to bottom, and the sludge discharge pipe 25 is located at the lowest position of the bottom plate of the separator body 21. Because the bottom plate of the separator body 21 is of a cone bucket structure, residues are prevented from being accumulated on the bottom plate of the separator body 21.
Example 2:
referring to fig. 3 and 4, in order to provide a cavitation air flotation three-phase separation system disclosed in the present invention, the difference between the embodiment 2 and the embodiment 1 is: the oil pumping device 5 is arranged on the top of the oil separation plate 26, the oil pumping device 5 comprises an oil well pump 51 fixed on the oil separation plate 26, an oil pumping pipe 52 communicated with an oil inlet of the oil well pump 51 is arranged at the oil inlet of the oil well pump 51, and the oil pumping pipe 52 is fixedly connected with the oil inlet of the oil well pump 51 in a sealing manner. An oil feeding pipe 53 communicated with the oil discharge port of the oil well pump 51 is arranged at the oil discharge port of the oil well pump 51, and the oil feeding pipe 53 is fixedly connected with the oil discharge port of the oil well pump 51 in a sealing manner.
The oil suction pipe 52 is located inside the oil drain area 28 inside the separator body 21 using a hose, and the oil inlet end of the oil suction pipe 52 is located below the level of the water discharge pipe 24. A floater 521 capable of floating on the oil surface is fixed at the oil inlet end of the oil pumping pipe 52, and a distance is reserved between the end surface of the oil inlet end of the oil pumping pipe 52 and the floater 521. When the float 521 floats on the oil surface, the oil well pipe 52 extends below the oil surface. The oil outlet end of the oil feed pipe 53 communicates with the inside of the separation oil-separating region 27 inside the separator body 21.
When floating oil is present on the water surface inside the oil drainage area 28, the oil inside the water surface of the oil drainage area 28 is drawn out through the oil drawing pipe 52 and sent into the inside of the separation oil compartment 27 through the oil sending pipe 53.
The water baffle 4 which is obliquely arranged is arranged in the separated oil separating area 27 and below the oil outlet end of the oil delivery pipe 53, and the water baffle 4 is fixedly connected with the oil separating plate 26. The water guard 4 slows down the speed of the oil and water flowing out of the oil feed pipe 53, and the oil and water flow slowly into the oil separating region 27.
The embodiments of the present invention are preferred embodiments of the present invention, and the scope of the present invention is not limited by these embodiments, so: all equivalent changes made according to the structure, shape and principle of the invention are covered by the protection scope of the invention.
Claims (6)
1. The utility model provides a cavitation air supporting three-phase separation system, includes cavitation air supporting machine (1), three-phase separator (2) and air supporting system outlet conduit (3), air supporting system outlet conduit (3) are linked together its characterized in that with the outlet of cavitation air supporting machine (1): the three-phase separator (2) comprises a separator body (21) with an opening at the top and a hollow interior and a supporting device for supporting the separator body (21), wherein a slag inlet pipe (23) and a water outlet pipe (24) which are used for communicating the interior of the separator body (21) with a slag outlet of the cavitation air flotation machine (1) are arranged on the separator body (21), and a sludge discharge pipe (25) and a control piece for controlling the opening and closing of the sludge discharge pipe (25) are arranged at the bottom end of the separator body (21); a plurality of transparent floating oil observation pipes (29) which are arranged at intervals along the height direction of the separator body (21) are arranged on the outer side of the separator body (21), the floating oil observation pipes (29) are communicated with the inside of the separator body (21), the floating oil observation pipes (29) are all positioned below the slag inlet pipe (23), an oil discharge pipe (210) is arranged at one end, far away from the separator body (21), of each floating oil observation pipe (29), and an oil discharge valve (2102) opened or closed by the oil discharge pipe (210) is arranged on each oil discharge pipe (210); the inside of separator body (21) is provided with oil removal board (26) of vertical setting, leave the distance between the bottom of oil removal board (26) and the bottom plate of separator body (21), oil removal board (26) separate oil district (27) and deoiling drain zone (28) with the separation that the internal partitioning discharge of separator body (21) set up side by side, it is linked together with the separator oil district to advance sediment pipe (23), drain pipe (24) are linked together with deoiling drain zone (28), the one end that separator body (21) was kept away from in drain pipe (24) is linked together with air supporting system outlet conduit (3).
2. The cavitation air flotation three-phase separation system according to claim 1, wherein: be provided with oil jack (5) on oil removal board (26), oil jack (5) are including oil-well pump (51), oil pumping pipe (52) and send oil pipe (53), oil pumping pipe (52) are linked together with the oil inlet of oil-well pump (51), send oil pipe (53) to be linked together with the oil drain port of oil-well pump (51), oil pumping pipe (52) are located the inside of deoiling drainage zone (28), the oil feed end of oil pumping pipe (52) is located drain pipe (24) the below of place height, the oil end and the separation oil removal zone (27) of sending oil pipe (53) are linked together.
3. The cavitation air flotation three-phase separation system according to claim 2, wherein: the oil pumping pipe (52) is a hose, and a floater (521) capable of floating on the oil surface is arranged at the oil inlet end of the oil pumping pipe (52).
4. The cavitation air flotation three-phase separation system according to claim 2, wherein: and a water baffle (4) which is obliquely arranged is arranged in the separation oil separation area (27) below the oil outlet end of the oil delivery pipe (53).
5. The cavitation air flotation three-phase separation system according to claim 1, wherein: the bottom plate of the separator body (21) is of a cone bucket structure.
6. The cavitation air flotation three-phase separation system according to claim 1, wherein: and control valves (291) are respectively arranged on the floating oil observation pipes (29).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010202635.5A CN111422938B (en) | 2020-03-20 | 2020-03-20 | Cavitation air floatation three-phase separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010202635.5A CN111422938B (en) | 2020-03-20 | 2020-03-20 | Cavitation air floatation three-phase separation system |
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| Publication Number | Publication Date |
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| CN111422938A true CN111422938A (en) | 2020-07-17 |
| CN111422938B CN111422938B (en) | 2024-08-30 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202010202635.5A Active CN111422938B (en) | 2020-03-20 | 2020-03-20 | Cavitation air floatation three-phase separation system |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08168753A (en) * | 1994-12-20 | 1996-07-02 | Hiwada Denshi Kk | Treatment of sewage |
| CN1579594A (en) * | 2003-08-15 | 2005-02-16 | 中国科学院沈阳应用生态研究所 | Oil-water separator for treating oil-containing waste water |
| KR20130115744A (en) * | 2012-04-13 | 2013-10-22 | 삼성중공업 주식회사 | Wastewater separating apparatus for vessel |
| CN107619122A (en) * | 2017-09-22 | 2018-01-23 | 宁波创蓝环境科技有限公司 | Sewage from catering business processing equipment and its method of work with oil-collecting reflux |
| CN109019738A (en) * | 2018-09-25 | 2018-12-18 | 哈尔滨北方环保工程有限公司 | Air floatation machine dross separation apparatus in a kind of tobacco processing sewage disposal process system |
| CN212127586U (en) * | 2020-03-20 | 2020-12-11 | 北京生态岛科技有限责任公司 | Cavitation air flotation three-phase separation system |
-
2020
- 2020-03-20 CN CN202010202635.5A patent/CN111422938B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08168753A (en) * | 1994-12-20 | 1996-07-02 | Hiwada Denshi Kk | Treatment of sewage |
| CN1579594A (en) * | 2003-08-15 | 2005-02-16 | 中国科学院沈阳应用生态研究所 | Oil-water separator for treating oil-containing waste water |
| KR20130115744A (en) * | 2012-04-13 | 2013-10-22 | 삼성중공업 주식회사 | Wastewater separating apparatus for vessel |
| CN107619122A (en) * | 2017-09-22 | 2018-01-23 | 宁波创蓝环境科技有限公司 | Sewage from catering business processing equipment and its method of work with oil-collecting reflux |
| CN109019738A (en) * | 2018-09-25 | 2018-12-18 | 哈尔滨北方环保工程有限公司 | Air floatation machine dross separation apparatus in a kind of tobacco processing sewage disposal process system |
| CN212127586U (en) * | 2020-03-20 | 2020-12-11 | 北京生态岛科技有限责任公司 | Cavitation air flotation three-phase separation system |
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| Publication number | Publication date |
|---|---|
| CN111422938B (en) | 2024-08-30 |
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