CN111620482A - Oil-water separation device and electrolytic separation chamber - Google Patents
Oil-water separation device and electrolytic separation chamber Download PDFInfo
- Publication number
- CN111620482A CN111620482A CN201910144453.4A CN201910144453A CN111620482A CN 111620482 A CN111620482 A CN 111620482A CN 201910144453 A CN201910144453 A CN 201910144453A CN 111620482 A CN111620482 A CN 111620482A
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- Prior art keywords
- oil
- separation chamber
- electrolytic
- separation
- chamber
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- 238000000926 separation method Methods 0.000 title claims abstract description 185
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 78
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 37
- 238000005188 flotation Methods 0.000 claims description 28
- 238000007790 scraping Methods 0.000 claims description 15
- 238000001914 filtration Methods 0.000 claims description 13
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 12
- 239000002893 slag Substances 0.000 claims description 10
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 7
- 229910052782 aluminium Inorganic materials 0.000 claims description 7
- 238000005273 aeration Methods 0.000 claims description 6
- 239000004519 grease Substances 0.000 claims description 6
- 229910052742 iron Inorganic materials 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000013049 sediment Substances 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 239000003818 cinder Substances 0.000 claims description 4
- 229910002804 graphite Inorganic materials 0.000 claims description 4
- 239000010439 graphite Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 2
- 239000003792 electrolyte Substances 0.000 abstract description 6
- 238000000746 purification Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 239000010865 sewage Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000002351 wastewater Substances 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
- 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
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
-
- 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/46—Apparatus for electrochemical processes
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
- C02F2201/4619—Supplying gas to the electrolyte
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
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)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses an oil-water separation device and an electrolytic separation chamber, wherein the electrolytic separation chamber comprises an electrolytic chamber and a first electrode plate. According to the electrolytic separation chamber provided by the scheme, the kitchen swill is subjected to oil-water separation by using an electrolysis method, namely after the electrolytic separation chamber is electrified, the kitchen swill (electrolyte) is subjected to an electrolysis reaction through the first electrode plate to generate ferrate, the kitchen swill is subjected to oil-water separation and purification through the ferrate, and compared with the mode of realizing oil-water separation through a standing mode in the prior art, the efficiency is remarkably improved.
Description
Technical Field
The invention relates to the technical field of oil-water separation, in particular to an oil-water separation device and an electrolytic separation chamber.
Background
In the prior art, kitchen swill in catering industry needs oil-water separation, and a common method is standing, and oil-water separation is realized by utilizing different sealing degrees of grease and water. However, the method has low efficiency, and the efficiency of oil-water separation of the kitchen swill is seriously influenced.
Therefore, how to improve the efficiency of oil-water separation of kitchen swill is a technical problem to be solved urgently by those skilled in the art.
Disclosure of Invention
In view of this, the present invention provides an electrolytic separation chamber to improve the efficiency of oil-water separation of kitchen swill. The invention also provides an oil-water separation device.
In order to achieve the purpose, the invention provides the following technical scheme:
an electrolytic separation chamber, which is suitable for oil-water separation of kitchen swill, comprising:
an electrolysis chamber; and
the electrolytic cell comprises a first electrode plate arranged in the electrolytic cell, wherein the cathode of the first electrode plate is a graphite electrode plate, and the anode of the first electrode plate is an iron electrode plate or a stainless steel electrode plate.
The utility model provides an oil-water separator, is applicable to the oil-water separation of kitchen swill, includes:
a coarse slag separation assembly provided with a water inlet;
the oil collecting tank is arranged below the coarse slag separation component;
the oil scraping component is used for scraping the separated grease to the oil collecting tank;
the first air floatation separation chamber is communicated with the coarse slag separation assembly, and an air floatation assembly is arranged in the first separation chamber;
the second electrolytic separation chamber is communicated with the first air flotation separation chamber, a second electrode plate is arranged in the second electrolytic separation chamber, the cathode of the second electrode plate is an aluminum plate, and the anode of the second electrode plate is an aluminum plate or an iron plate;
and the third electrolytic separation chamber is communicated with the second electrolytic separation chamber, a water outlet is formed in the third electrolytic separation chamber, and the third electrolytic separation chamber is the electrolytic separation chamber in claim 1.
Preferably, in the oil-water separator, the number of the third electrolytic separation chambers is plural, the plural third electrolytic separation chambers are sequentially communicated with each other in a flowing direction of the kitchen swill, and a water outlet is provided in the third electrolytic separation chamber located most downstream in the flowing direction of the kitchen swill.
Preferably, in the oil-water separator, the plurality of third electrolytic separation chambers are provided along a first straight line,
the first air flotation separation chamber and the second electrolysis separation chamber are arranged along a second straight line, and the second straight line is parallel to the first straight line.
Preferably, in the oil-water separator, the air flotation unit includes:
an aeration disc; and
the rod is heated.
Preferably, in the oil-water separator, the coarse residue separation module includes:
a U-shaped filter screen;
the water inlet is arranged on the filtering chamber, one end of the filtering chamber is provided with a mounting hole, and the second end of the filtering chamber is provided with a slag discharge port;
the setting is in be used for discharging away the hob of thick sediment on the U type filter screen, the one end of hob can pass through the mounting hole is connected with the motor, the other end of hob with arrange the cinder notch intercommunication.
Preferably, in the oil-water separator, upper ends of the first flotation chamber, the second electrolysis separation chamber and the third electrolysis separation chamber are open ends,
the oil scraping assembly is arranged above the open ends of the first air flotation separation chamber, the second electrolysis separation chamber and the third electrolysis separation chamber.
Preferably, in the oil-water separator, the oil scraping unit includes:
a first sprocket;
the second chain wheel is connected with the first chain wheel through a chain and is connected with the motor; and
the scraper blade is connected with the chain and comprises a vertical plate which is connected with the chain and is vertical to the chain and an inclined plate which is connected with the vertical plate, and the inclined direction of the inclined plate is opposite to the flowing direction of the liquid.
According to the technical scheme, the electrolytic separation chamber comprises the electrolytic chamber and the first electrode plate. According to the electrolytic separation chamber provided by the scheme, the kitchen swill is subjected to oil-water separation by using an electrolysis method, namely after the electrolytic separation chamber is electrified, the kitchen swill (electrolyte) is subjected to an electrolysis reaction through the first electrode plate to generate ferrate, the kitchen swill is subjected to oil-water separation and purification through the ferrate, and compared with the mode of realizing oil-water separation through a standing mode in the prior art, the efficiency is remarkably improved.
This scheme still discloses an oil-water separator, is applicable to the oil-water separation of kitchen swill. The oil-water separation device comprises: the device comprises a coarse residue separation component, an oil collecting tank, an oil scraping component, a first air flotation separation chamber, a second electrolysis separation chamber and a third electrolysis separation chamber. The third electrolytic separation chamber is the electrolytic separation chamber described in the above embodiment. Because the electrolysis separation chamber has the technical effects, the oil-water separation device with the electrolysis separation chamber also has the same technical effects, and the details are not repeated herein.
Drawings
FIG. 1 is a schematic structural diagram of an oil-water separation device according to an embodiment of the present invention;
FIG. 2 is a cross-sectional view A-A of FIG. 1;
fig. 3 is a cross-sectional view of B-B in fig. 1.
1. The device comprises a coarse residue separation component 2, an oil collecting tank 3, an oil scraping component 4, a first air flotation separation chamber 5, a second electrolysis separation chamber 6, a third electrolysis separation chamber 7, an aeration disc 8 and a heating rod.
Detailed Description
The invention discloses an electrolytic separation chamber, which is suitable for oil-water separation of kitchen swill.
The electrolytic separation chamber comprises an electrolytic chamber and a first electrode plate.
The electrolysis chamber is used for containing kitchen swill, and the kitchen swill is used as electrolyte in the scheme.
The first electrode plate is arranged in the electrolytic chamber.
In a first embodiment of the present disclosure, the cathode of the first electrode plate is a graphite electrode plate, and the anode of the first electrode plate is an iron electrode plate.
In a second embodiment of the present disclosure, the cathode of the first electrode plate is a graphite electrode plate, and the anode of the first electrode plate is a stainless steel electrode plate.
The first electrode plate is electrified, and the cathode and the anode of the first electrode plate and electrolyte (kitchen swill) are subjected to electrolytic reaction to generate ferrate. According to the scheme, the kitchen swill is used as the electrolyte to generate the ferrate, the ferrate generated by electrolysis is used for purifying the kitchen swill without independently extracting the ferrate, so that the effective utilization of the kitchen swill is realized firstly, and the purification cost of the kitchen swill is reduced secondly.
According to the electrolytic separation chamber provided by the scheme, the kitchen swill is subjected to oil-water separation by using an electrolysis method, namely after the electrolytic separation chamber is electrified, the kitchen swill (electrolyte) is subjected to an electrolysis reaction through the first electrode plate to generate ferrate, the kitchen swill is subjected to oil-water separation and purification through the ferrate, and compared with the mode of realizing oil-water separation through a standing mode in the prior art, the efficiency is remarkably improved.
In addition, the electrolytic separation chamber provided by the scheme does not need to be added with a reagent independently, ferrate generated by electrolysis is directly utilized to treat sewage, and the ferrate is a recognized green disinfectant and does not bring secondary pollution.
This scheme still discloses an oil-water separator, is applicable to the oil-water separation of kitchen swill. The oil-water separation device comprises: the device comprises a coarse residue separation component 1, an oil collecting tank 2, an oil scraping component 3, a first air flotation separation chamber 4, a second electrolytic separation chamber 5 and a third electrolytic separation chamber 6.
The coarse residue separation component 1 is provided with a water inlet for preliminarily filtering kitchen swill passing through the coarse residue separation component 1 to remove coarse residue with larger granularity in the kitchen swill.
The oil collecting tank 2 is arranged below the coarse residue separation assembly 1 and is used for collecting grease separated by the first air floatation separation chamber 4, the second electrolysis separation chamber 5 and the third electrolysis separation chamber 6. The oil collecting tank 2 is provided with an oil outlet.
The oil scraping component 3 is used for scraping the separated grease to the oil collecting tank 2, manual collection of the grease is not needed, and the labor intensity of oil-water separation is reduced.
The first air flotation separation chamber 4 is communicated with the coarse residue separation component 1, namely kitchen swill subjected to preliminary filtration through the coarse residue separation component 1 firstly enters the first air flotation separation chamber 4, and oil and water are subjected to second-step separation through the air flotation component arranged in the first air flotation separation chamber 4. The air flotation assembly adopts the working principle that highly dispersed micro bubbles are used as carrier adhesion suspended matters, and oil stains and the like float to the water surface through the bubbles to achieve the purpose of removing the oil stains.
The second electrolytic separation chamber 5 is communicated with the first air flotation separation chamber 4, and the second electrolytic separation chamber 5 carries out third-step separation on oil and water by an electrolytic method.
In a first embodiment of the solution, the cathode of the second electrode plate is an aluminum plate and the anode of the second electrode plate is an aluminum plate.
In a second embodiment of the present disclosure, the cathode of the second electrode plate is an aluminum plate, and the anode of the second electrode plate is an iron plate.
And a polyaluminium flocculant is generated during electrolysis, and pollutant particles in the wastewater are combined with the polyaluminium flocculant to aggregate and settle at the bottom of the second electrolytic separation chamber 5. The bottom of the second electrolytic separation chamber 5 is provided with a sewage draining outlet.
The third electrolytic separation chamber 6 is communicated with the second electrolytic separation chamber 5, a water outlet is arranged on the third electrolytic separation chamber 6, and the third electrolytic separation chamber 6 is the electrolytic separation chamber described in the above embodiment. Because the electrolysis separation chamber has the technical effects, the oil-water separation device with the electrolysis separation chamber also has the same technical effects, and the details are not repeated herein.
The oil-water separation device provided by the scheme realizes four-step separation of kitchen swill through the coarse residue separation component 1, the first air flotation separation chamber 4, the second electrolysis separation chamber 5 and the third electrolysis separation chamber 6, thereby completing purification of the kitchen swill. According to the scheme, the oil-water separation of the kitchen swill is realized by adopting a mode of combining the filtering method, the air flotation separation method and the two electrolysis separation methods, and compared with the mode of realizing the oil-water separation by a standing method in the prior art, the oil-water separation efficiency of the kitchen swill is obviously improved.
In a specific embodiment of the present embodiment, the number of the third electrolytic separation chambers 6 is plural.
The plurality of third electrolytic separation chambers 6 are sequentially communicated according to the flowing direction of the kitchen swill, and a water outlet is arranged on the third electrolytic separation chamber 6 which is positioned at the most downstream of the flowing direction of the kitchen swill.
The third electrolytic separation chambers 6 can purify kitchen swill for many times, and the oil-water separation effect of the kitchen swill is guaranteed.
The layout of the oil-water separation device is improved in the scheme. Specifically, the plurality of third electrolytic separation chambers 6 are arranged along a first straight line, and the first air flotation separation chamber 4 and the second electrolytic separation chamber 5 are arranged along a second straight line parallel to the first straight line.
The third electrolytic separation chamber 6 positioned at the most upstream is communicated with the second electrolytic separation chamber 5, and a water outlet is arranged on the third electrolytic separation chamber 6 positioned at the most downstream. In the scheme, the water inlet and the water outlet of the oil-water separation device are positioned at the same side of the oil-water separation device.
The arrangement form shortens the whole length of the oil-water separation device and reduces the space of the oil-water separation device in the length direction.
In another embodiment of the solution, the plurality of third electrolytic separation chambers 6 are arranged along a first straight line, and the first gas flotation separation chamber 4 and the second electrolytic separation chamber 5 are arranged along a second straight line, which is collinear with the first straight line.
In one embodiment of the present disclosure, an air bearing assembly includes: an aeration disc 7 and a heating rod 8.
The heating rod 8 is used for heating kitchen swill in the first air flotation separation chamber 4 to prevent oil stain from solidifying, and the aeration disc 7 is a disc made of high-grade rubber and having one-way air guide performance and is connected with an external air pump. The air pump operates to make the aeration plate 7 generate small bubbles in kitchen swill, so that the sewage is subjected to more sufficient electrolytic reaction in the second electrolytic separation chamber 5.
The coarse slag separation assembly 1 comprises: u type filter screen, filter chamber and hob.
The U-shaped filter screen is a main part for primarily filtering kitchen swill.
The filtering chamber is used for installing a U-shaped filtering net and guiding the filtered kitchen swill to the first air flotation separation chamber 4. The filter chamber is provided with a water inlet, one end of the filter chamber is provided with a mounting hole, and the second end of the filter chamber is provided with a slag discharge port.
The hob sets up and is used for removing the coarse sediment that U type filter screen filtered off on U type filter screen, and the one end of hob can be connected with the motor through the mounting hole, the other end and the row's of hob mouth intercommunication. When needs were cleared up the coarse sediment after filtering in the U type filter screen, opened row's cinder notch, the motor drove the hob and rotates, and the coarse sediment is discharged through row's cinder notch under the effect of hob, realizes the automatic clearance of debris, does not need artifical clearance.
Specifically, the upper ends of the first air flotation separation chamber 4, the second electrolysis separation chamber 5 and the third electrolysis separation chamber 6 are all open ends, the upper ends of the first air flotation separation chamber 4, the second electrolysis separation chamber 5 and the third electrolysis separation chamber 6 are all provided with cover plates, and handles are arranged on the cover plates.
The oil scraping assembly 3 is arranged above the open ends of the first air flotation separation chamber 4, the second electrolytic separation chamber 5 and the third electrolytic separation chamber 6 and is positioned below the cover plate.
Preferably, the oil scraping assembly 3 comprises: the chain scraper comprises a first chain wheel, a second chain wheel, a chain and a scraper.
The first chain wheel is connected with the second chain wheel through a chain, and the second chain wheel is connected with the motor.
The scraper is connected with the chain, and the scraper comprises a vertical plate which is connected with the chain and is vertical to the chain and an inclined plate which is connected with the vertical plate, and the inclined direction of the inclined plate is opposite to the flowing direction of the liquid.
In a specific embodiment of the solution, the angle between the inclined plate and the vertical plate is an obtuse angle.
The scraper is an integrally formed scraper and is fixedly connected with the chain.
Finally, it should be noted that: the above embodiments are only for illustrating the technical solutions of the present invention and not for limiting the same, and although the present invention is described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that: modifications and equivalents may be made to the invention without departing from the spirit and scope of the invention.
Claims (8)
1. The utility model provides an electrolytic separation room, is applicable to the oil-water separation of kitchen swill, its characterized in that includes:
an electrolysis chamber; and
the electrolytic cell comprises a first electrode plate arranged in the electrolytic cell, wherein the cathode of the first electrode plate is a graphite electrode plate, and the anode of the first electrode plate is an iron electrode plate or a stainless steel electrode plate.
2. The utility model provides an oil-water separator, is applicable to the oil-water separation of kitchen swill, its characterized in that includes:
a coarse slag separation assembly (1) provided with a water inlet;
the oil collecting tank (2) is arranged below the coarse slag separation component (1);
the oil scraping component (3) is used for scraping the separated grease to the oil collecting tank (2);
the first air floatation separation chamber (4) is communicated with the coarse slag separation assembly (1), and an air floatation assembly is arranged in the first separation chamber;
a second electrolytic separation chamber (5) communicated with the first air flotation separation chamber (4), wherein a second electrode plate is arranged in the second electrolytic separation chamber (5), the cathode of the second electrode plate is an aluminum plate, and the anode of the second electrode plate is an aluminum plate or an iron plate;
a third electrolytic separation chamber (6) communicated with the second electrolytic separation chamber (5), wherein a water outlet is arranged on the third electrolytic separation chamber (6), and the third electrolytic separation chamber (6) is the electrolytic separation chamber in claim 1.
3. The oil-water separator according to claim 2, wherein the number of the third electrolytic separation chambers (6) is plural, the plural third electrolytic separation chambers (6) are sequentially communicated with each other in the flowing direction of the kitchen swill, and a water outlet is provided in the third electrolytic separation chamber (6) located most downstream in the flowing direction of the kitchen swill.
4. The oil-water separator according to claim 2, wherein a plurality of the third electrolytic separation chambers (6) are arranged along a first straight line,
the first air-flotation separation chamber (4) and the second electrolysis separation chamber (5) are arranged along a second straight line, and the second straight line is parallel to the first straight line.
5. The oil and water separator of claim 2, wherein the air flotation assembly comprises:
an aeration disc (7); and a heating rod (8).
6. The oil-water separator according to claim 2, wherein the coarse residue separation assembly (1) comprises:
a U-shaped filter screen;
the water inlet is arranged on the filtering chamber, one end of the filtering chamber is provided with a mounting hole, and the second end of the filtering chamber is provided with a slag discharge port;
the setting is in be used for discharging away the hob of thick sediment on the U type filter screen, the one end of hob can pass through the mounting hole is connected with the motor, the other end of hob with arrange the cinder notch intercommunication.
7. The oil-water separator according to claim 2, wherein the upper ends of the first flotation chamber (4), the second electrolytic separation chamber (5) and the third electrolytic separation chamber (6) are all open ends,
the oil scraping assembly (3) is arranged above the open ends of the first air-flotation separation chamber (4), the second electrolysis separation chamber (5) and the third electrolysis separation chamber (6).
8. The oil-water separator according to claim 2, wherein the oil scraping assembly (3) comprises:
a first sprocket;
the second chain wheel is connected with the first chain wheel through a chain and is connected with the motor; and
the scraper blade is connected with the chain and comprises a vertical plate which is connected with the chain and is vertical to the chain and an inclined plate which is connected with the vertical plate, and the inclined direction of the inclined plate is opposite to the flowing direction of the liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910144453.4A CN111620482A (en) | 2019-02-27 | 2019-02-27 | Oil-water separation device and electrolytic separation chamber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910144453.4A CN111620482A (en) | 2019-02-27 | 2019-02-27 | Oil-water separation device and electrolytic separation chamber |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111620482A true CN111620482A (en) | 2020-09-04 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910144453.4A Pending CN111620482A (en) | 2019-02-27 | 2019-02-27 | Oil-water separation device and electrolytic separation chamber |
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| Country | Link |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20040166040A1 (en) * | 2002-02-27 | 2004-08-26 | Zoran Minevski | Electrochemical method and apparatus for producing and separating ferrate(VI) compounds |
| CN105692813A (en) * | 2016-01-07 | 2016-06-22 | 沈阳建筑大学 | Electrocoagulation and electrocatalytic oxidation coupling device and use method thereof |
| CN106082413A (en) * | 2016-08-02 | 2016-11-09 | 黎明职业大学 | A kind of ferrate synthesizes and organic matter degradation equipment and technique online |
| CN108947032A (en) * | 2018-06-28 | 2018-12-07 | 北京金泰鸿业物业管理有限公司 | A kind of efficient water and oil separator of electric flocculation |
-
2019
- 2019-02-27 CN CN201910144453.4A patent/CN111620482A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20040166040A1 (en) * | 2002-02-27 | 2004-08-26 | Zoran Minevski | Electrochemical method and apparatus for producing and separating ferrate(VI) compounds |
| CN105692813A (en) * | 2016-01-07 | 2016-06-22 | 沈阳建筑大学 | Electrocoagulation and electrocatalytic oxidation coupling device and use method thereof |
| CN106082413A (en) * | 2016-08-02 | 2016-11-09 | 黎明职业大学 | A kind of ferrate synthesizes and organic matter degradation equipment and technique online |
| CN108947032A (en) * | 2018-06-28 | 2018-12-07 | 北京金泰鸿业物业管理有限公司 | A kind of efficient water and oil separator of electric flocculation |
Non-Patent Citations (1)
| Title |
|---|
| 邝生鲁: "现代精细化工高新技术与产品合成工艺", vol. 1, 科学技术文献出版社, pages: 650 * |
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Application publication date: 20200904 |